Findings Of Fact Upon consideration of the oral and documentary evidence adduced at the hearing, the following relevant facts are found: Petitioner L. C. Prevatt is the owner and operator of the Riverview Speed Wash, Inc., a coin operated laundry which has been in existence for over ten years. The facility has twelve top load washers, four double load washers, one triple load washer and seven gas dryers. It is open from 7:00 a.m. to 9:00 p.m., seven days a week. The facility is located in a shopping center in space which petitioner rents on a month-by-month basis. The facility utilizes a 0.0075 mgd waste treatment plant with effluent disposal to a county-owned drainage ditch which is connected and discharges to the Alafia River approximately 0.6 miles south of the facility. On or about May 29, 1981, petitioner submitted an application for a temporary operation permit for his Riverview laundry facility. Temporary operation permits are issued by the DER when a facility is not currently meeting State water quality standards and the applicant needs or desires a period of time to bring the facility up to the applicable standards. Here, the petitioner stated on his application that no upgrade of the waste treatment facility was planned. The application further stated that the facility would be connected to an area wide regional waste treatment system when that system became available. After numerous requests for further information from the applicant and various inspections of the facility, the DER issued its notice of intent to deny petitioner's application for a temporary operation permit. Reasons for the intended denial included failure to provide requested background water quality information, failure to provide a proposed water quality standards compliance schedule, failure to provide reasonable assurance that a municipal sewer would be available as an alternative means of disposal and improper and deficient operation and maintenance of the facility. Numerous inspections of the petitioner's facility by personnel from the DER and the Hillsborough County Environmental Protection Commission revealed that the facility was not functional in terms of operating correctly and that the design of the plant was inadequate to meet State water quality standards. Specifically, these inspections revealed that the chlorination equipment was not operational, that the trickling filter was not operational, that the removal rates for BOD and suspended solids were consistently and significantly less than the State standard of 90 percent, that the discharge and effluent were of a milky color and would not meet the State standards for turbidity and color, that the water quality of the drainage ditch was extremely low and that the water quality results were actually worse after going through the existing system. It was determined that the discharge was degrading the quality of the receiving waters and that, even if the petitioner's operational and maintenance problems were solved, the design of the facility is not adequate to assure future compliance with State standards. Petitioner admits that his facility does not currently meet State water quality standards. In mitigation, it is contended that many other laundries in the area also do not meet State standards, that it is not economically feasible to redesign the facility to attain compliance, that he has no land available upon which to discharge effluent and that he would be willing to install a sand filter and did have the permission of the manager (not the owner) of the property to discharge effluent into the parking lot drain ponds. No written evidence of this agreement was adduced and there was no demonstration that such runoff ponds would be able to hold and/or treat effluent from the petitioner's facility. There was also no evidence offered to demonstrate that a municipal or regional sewer system would be available in the near future to serve the laundry facility.
Recommendation Based upon the findings of fact and conclusions of law recited above, it is RECOMMENDED that petitioner's application for a temporary operation permit for Riverview Speed Wash, Inc. be DENIED. Respectfully submitted and entered this 7th day of September, 1982, in Tallahassee, Florida. DIANE D. TREMOR, Hearing Officer Division of Administrative Hearings The Oakland Building 2009 Apalachee Parkway Tallahassee, Florida 32301 (904) 488-9675 Filed with the Clerk of the Division of Administrative Hearings this 7th day of September, 1982. COPIES FURNISHED: L. C. Prevatt Post Office Box 998 Gibsonton, Florida 33534 William W. Deane, Esquire Assistant General Counsel Department of Environmental Regulation Twin Towers Office Building 2600 Blair Stone Road Tallahassee, Florida 32301 Victoria Tschinkel, Secretary Department of Environmental Regulation Twin Towers Office Building 2600 Blair Stone Road Tallahassee, Florida 32301
The Issue In their Prehearing Stipulation, the parties described the nature of the controversy as follows: This matter involves a challenge to a Technical Staff Report and Recommendation made by Respon- dent's staff on a consumptive use permit applica- tion for water submitted to Respondent by Petitioner. Petitioner owns a recreational facility where water is being used. The Staff Report recommends that certain conditions be imposed upon the permit proposed to be issued to Petitioner placing limitations on the amount of water which may be consumed by Petitioner and requiring Petitioner to report on numbers of persons utilizing Respondent's facility. In that same stipulation, the parties described their respective positions as follows: Petitioner's Position: The present use of water at the Wekiva Falls Resort is a reasonable beneficial use which should not be reduced or limited by permit conditions. The standpipes through which the water flows are not wells and therefore should not be subject to any regulation by Respondent. The placement of the standpipes did not increase the flow of water but rather captured the already existing flow from natural springs which existed on the property prior to the placement of the standpipes. Petitioner feels his use does not come within the permitting power of Respondent, and that if it does, its use should be allowed to continue without any reductions in flow. Respondent's Position: After review of Petitioner's consumptive use permit application for the use of water emanating from two standpipes, one twenty-four (24) inches in diameter and the other fourteen inches in diameter, the staff of the District determined that the standpipes were wells subject to the District's regulation under Chapter 40C-2, Florida Administrative Code, and recommended approval of the permit with certain conditions requiring a reduction in flow during certain low or non-use periods. This matter arose from Petitioner's application to the District for a consumptive use permit that would allocate water to the Petitioner from water flowing from a 24-inch metal pipe and a 14-inch metal pipe for use at Petitioner's campground. The District maintains that, not only is the water that is drawn from the metal pipes and used at the campground regulated pursuant to Part II of Chapter 373, Florida Statutes, but also that the remaining water that flows from the two metal pipes and is used by Petitioner to maintain a swimming area is regulated pursuant to Part II of Chapter 373, Florida Statutes. The Petitioner has not applied for an allocation of water for maintaining the swimming area. Even though the Petitioner has not applied for such an allocation, the use of water for maintaining the swimming area has been evaluated because the Petitioner maintained that, even if the water used to maintain the swimming area is regulated pursuant to Part II of Chapter 373, Florida Statutes, the flow of water from the metal pipes should not be restricted in any fashion from the ongoing flow. Thus, the issues presented are whether the application that was applied for should be granted, whether the Petitioner has to apply for an additional allocation in order to continue using water to maintain the swimming area, and what, if an additional allocation is sought, the permit would be. In their Prehearing Stipulation the parties also agreed to the following issues of law. The Division of Administrative Hearings has jurisdiction over the subject matter of and the parties to this proceeding subject to Section 120.57(1), Florida Statutes. To the extent the standpipes located on Petitioner's property are determined to be wells, they are governed by and subject to the provisions of Chapter 373, Florida Statutes, and Chapter 40C-2, Florida Administrative Code. The procedural rules which apply to this proceeding are Chapters 40C-1, 28-5, and 22-I, Florida Administrative Code. The parties also agreed to the following as being the ultimate issues of fact which remained to be litigated. Whether the two standpipes constitute an excavation that was drilled, cored, washed, driven, dug, jetted, or otherwise constructed with the intended use of such excavation to be for the location, acquisition, development, or artificial recharge of water. Whether the continued use by Petitioner of water at pre-permit levels is a use of water in a quantity necessary for economic and efficient utilization for a purpose and in a manner which is both reasonable and consistent with the public interest. Whether the continued use of water by Petitioner at pre-permit levels would increase the danger of saline water encroachment. Whether a reduction in flow of water will result in a reduction in water quality for the uses made of the water by Petitioner. Whether a reduction in flow of water would have adverse impacts on the quality of water in the Wekiva River. Subsequent to the hearing, a transcript of the proceedings at hearing was filed on December 22, 1986, and, pursuant to request of the parties, they were allowed 30 days from that date within which to file their proposed recommended orders. Both parties filed proposed recommended orders containing proposed findings of fact and conclusions of law. The proposed recommended orders have been carefully considered and a specific ruling on each proposed finding of fact submitted by each party is contained in the Appendix which is attached to and incorporated into this Recommended Order.
Findings Of Fact Based on the stipulations of the parties, on the exhibits received in evidence, and on the testimony of the witnesses at the hearing, I make the following findings of fact. Findings based on admissions in prehearing stipulation Petitioner is a private individual who owns and does business as the Wekiva Falls Resort in Lake County, Florida. Respondent, a special taxing district created by Chapter 373, Florida Statutes, is charged with the statutory responsibility of the administration and enforcement of permitting programs pursuant to Part II of Chapter 373, Consumptive Uses of Water, specifically Sections 373.219 and 373.223, Florida Statutes, and Chapter 40C-2, Florida Administrative Code. The District is the agency affected in this proceeding. The District has assigned Petitioner's permit application, which is the subject of this proceeding, the permit number 2-069-0785AUS. On September 4, 1985, Petitioner submitted to Respondent a CUP application number 2-069-0785AUS to withdraw water from two wells, one 14 inches in diameter and the other 24 inches in diameter, located on Petitioner's property in Lake County, Florida. The water which flows from the two standpipes flows through a creek which was improved by Petitioner, said creek having as its terminus the Wekiva River. The standpipes were put in place by Petitioner or his authorized agents or employees in 1972. The area of the Wekiva River into which the creek leading from the two standpipes flows has been designated as an aquatic preserve and an "Outstanding Florida Water." On May 23, 1986, Respondent's staff gave notice of its intent to recommend approval with conditions of Petitioner's CUP application number 2-069- 0785AUS. Petitioner's Petition for Administrative Hearing was timely filed with the District. Findings based on evidence at hearing Petitioner filed his CUP application on September 4, 1985, one week in advance of the September 11, 1985, deadline for existing users of water to file applications which would establish and protect their existing user status. Petitioner's application requests an allocation of 31.7 million gallons per year (mgy) for the following uses: 8 per cent for cooling and air conditioning, 3 per cent for outside use, and 89 per cent for commercial and industrial use. Petitioner has made no application for any allocation of water for water based recreation. The Wekiva Falls Resort property consists of approximately 140 acres stretching 4800 feet in length between Wekiva River Road and the Wekiva River. The property is located along the Wekiva River between State Road 46 and the Orange County, Florida, line. Seminole County, Florida, is on the opposite side of the Wekiva River from the subject property. Petitioner purchased the subject property in 1968. At that time it was a heavily overgrown rural tract. Petitioner observed a stream which came under Wekiva River Road, passing through seven culverts, and running the length of the property to the Wekiva River. This stream carries runoff from Petitioner's property as well as runoff from areas west of the property on the opposite side of Wekiva River Road. At a point approximately midway between the Wekiva River and Wekiva River Road, along the stream, a depressional area was located by Petitioner, through which the stream flowed. Petitioner observed that more water was flowing downstream from the depressional area than upstream. Petitioner's property is located in an area of natural artesian flow where springs or seeps are not uncommon. Because the area in which the subject property is located is one of natural artestian flow, it is likely that a surficial seep of water existed in the depressional area which generated a flow of water. None of the available geological or hydrogeological information or data would indicate the existence of a spring or springs on this site prior to the drilling undertaken by Petitioner. At the time the first well was drilled by Dick Joyce Well Drilling, Inc., no spring was observed by the driller. Further, in conversations with the Executive Director of the District in 1974, no mention was made by the Petitioner of the existence of a spring or springs at the site prior to drilling. On July 17, 1969, Petitioner measured the stream flow and calculated same to be 23.97 cubic feet per second. The methodology utilized by Petitioner in measuring the stream flow in its natural state was an accepted methodology. However, this measurement did not discriminate between the water flowing into the depressional area from the stream carrying runoff from the lands upstream of the depressional area and the water originating from surficial seeps in the depressional area. Thus, this amount cannot be utilized or relied upon as a measurement of the amount of water emanating from seeps in the depressional area before drilling was undertaken by Petitioner. Nevertheless, other evidence indicates that the total volume of water flowing from Petitioner's property into the Wekiva River was probably substantially the same both before and after the installation of the two wells on Petitioner's property. In any event, the installation of Petitioner's wells does not appear to have increased the flow of the Wekiva River downstream of where Wekiva Canoe Creek discharges. In undertaking the development of his property as a resort/campground/recreational vehicle facility, Petitioner dug out the depressional area and used a dragline to open up the creek from the depressional area downstream to the Wekiva River. At a point approximately 200 feet west of the Wekiva River, Petitioner dredged a wide area to construct a marina with access through the creek to the Wekiva River. In an effort to obtain a controlled flow of water, Petitioner contracted Dick Joyce of Dick Joyce Well Drilling Inc. to drill a well fourteen inches in diameter at a site along the bank of the depressional area designated by Petitioner. The well was drilled by Joyce in August of 1972. The well was drilled using a cable rig to a depth of 107 feet, with casing being driven to a depth of 58 feet. The drilling procedure excavated a hole in the ground, penetrated rock, and resulted in the flow of ground water to land surface. The top of the 14-inch well extends 4 to 5 feet above land surface. In a further effort to obtain a controlled flow of water, Petitioner subsequently contracted Central Florida Drillers to drill a second well, twenty- four (24) inches in diameter. This well was drilled in 1973 along the bank of the depressional area, at a spot identified by Petitioner, in the same general vicinity as the previously drilled 14-inch well. The well was also drilled using a cable rig to a depth of 120 feet with casing being driven to a depth of 84.7 feet. The drilling procedure excavated a hole in the ground, penetrated rock, and resulted in the flow of ground water to land surface. The top of the 24-inch well extends 5 feet above land surface. Central Florida Well Drillers Inc. prepared and maintained a driller's log of the 24-inch well, recording the composition of the stratigraphic column through which the drilling equipment passed. The lithology shown in the stratigraphic column is indicative of the geology normally found in a well drilled in this geographical area. The log shows penetration of the normal stratigraphic column for this area and does not show a spring bore that had been filed in by materials at an earlier date. The drilling of the two wells by Petitioner substantially altered the natural conditions on the property as they existed prior to 1972. The top of the Floridan aquifer in the geographical region in which Petitioner's wells are located is encountered at depths ranging from 50 to 100 feet below land surface. The amount of water flowing from the wells has been variously reported and calculated since the wells were installed. Petitioner's promotional materials, which bill the resort as home of the "world's largest flowing well," asserts the maximum free flow capacity to be 72 million gallons per day (mgd). At another point in time, flow from the larger well was said to be 28.8 mgd and the flow from the smaller well 11.5 mgd. Respondent's staff, in preparing its technical staff report, calculated the total flowage from the two wells to be 18 mgd. In his application for a permit to operate a public bathing facility filed with the Florida Department of Health and Rehabilitative Services (HRS), Petitioner indicated the total flowage to be 16 mgd. For purposes of the determination to be made by this Order, the parties stipulated at the hearing to a total flowage figure of 12.47 mgd. Petitioner has operated and continues to operate the facility as a campground and water based recreational site. The central theme of the use of Petitioner's property is the recreational use of water. The water based recreation includes swimming, boating, tubing, and fishing, and is centered around the two flowing wells. The designated swimming area extends from a retaining wall located just west of the westernmost of the two wells to a footbridge which crosses Canoe Creek west of the Marina. The supply of water for recreational use comes primarily from the two wells. The stream which originally existed on the property and which carries runoff from the more western part of Petitioner's property and from off-site enters the designated swimming area at the retaining wall on its westernmost edge. The water which comes from this stream and which is introduced into the western end of the swimming area contains high levels of bacteria and coliforms. Between the hours of 6:00 a.m. and 6:00 p.m., Petitioner operates a sump pump which redirects this high coliform water eastward around a major portion of the swimming area to a point still within the swimming area. For the remaining twelve hours per day, this high bacteria, high coliform water is allowed to flow directly into the swimming area. Petitioner could reduce the level of bacteria and coliforms in the swimming area by simply operating the sump pump for 24 hours a day and/or introducing the water so pumped back into Canoe Creek at a point further downstream east of the designated swimming area. In addition, runoff from a storm drain which was constructed by Lake County, Florida, as a result of an easement granted to them by Petitioner, enters Canoe Creek at a point downstream from the wells but east of the footbridge, within the designated swimming area. When stormwater is conveyed through this storm drain, it also introduces coliforms into the swimming area at the point where the storm drain intersects Canoe Creek. The gate valves on each of the two wells are frozen in a completely open position. The wells are presently flowing at maximum capacity 24 hours a day without regard to whether the facility is being used or not. Petitioner does not presently have the capability to incrementally control the flow of water, short of utilizing a plug to completely shut off the flow of water from one or the other or both of the two wells. Petitioner does, however, have the capability of installing a hydraulic cylinder remote control system in the wells which would allow him to control the flow of water incrementally from the wells via a phone line. The use of Petitioner's facility varies by season, month, day of the week, and time of day, and according to weather conditions on a particular day. Although Petitioner did not have records available showing the number of persons utilizing a particular part of the facility for a particular purpose on a particular day, most of Petitioner's revenue, at least during the summer months, is generated by day use swimmers and picnickers. The swimming facility is most heavily used during daylight hours in the summer months. More customers use the swimming facilities on Saturday and Sunday than during the weekdays. Use is lower during the winter months and during times of inclement weather such as cloudy or rainy days. The evidence fails to show the average number of bathers who use Petitioner's facilities at any particular season or during any particular weather conditions. Petitioner holds a Swimming Pool-Bathing Place Operating Permit for the swimming area issued by the Florida Department of Health and Rehabilitative Services pursuant to Section 10D-5.120, Florida Administrative Code. Responsibility for enforcement of these administrative regulations is with the Lake County, Florida, Public Health Unit. Petitioner's permit allows him to have a maximum swimming pool population of 2000 bathers per day, but there is no evidence that he has ever had that many bathers on a single day since he received the permit. There are two primary water quality parameters which Petitioner is required to maintain within the swimming area, which are delineated in Rule 10D- 5.120, Florida Administrative Code. The first is a flow-through requirement of 500 gallons of water per anticipated bather per 24 hours. On a day when the swimming facility is being utilized by the maximum number of bathers allowable, 2000, the flow requirement for that day would then be one million gallons. For any day when the bathing population fell below 2000, the gallon flow-through requirement would be proportionately reduced. The second water quality parameter Petitioner is required to maintain relates to coliform densities. High coliform count can result in serious illness. The coliform density in the swimming area must not exceed 1000 most probable number of coliform organisms per 100 milliliters. Coliform levels in the swimming area at any given time are dependent upon several variable factors. Among these factors is the number of coliforms being introduced into the swimming area. As has previously been discussed, when the sump pump which reroutes high coliform water around the upper part of the swimming area is not operating, the number of coliforms would increase. Also during periods of rainfall, coliforms are washed into the swimming area in runoff which enters from overland and through the storm drain which enters the lower part of the swimming area. Temperature is a variable factor which affects coliform levels. As temperatures increase, bacteria multiply more rapidly, and thus coliform levels increase. The number of human beings utilizing the water at a given time impacts coliform levels in that, since humans are producers of coliforms, when greater numbers of humans are in the water, higher coliform levels would normally result. These factors coalesce in that high temperatures normally occur during the summer months which contain the days of most intense usage, and thus high coliform levels would be expected during these times if all other factors remain constant. Conversely, during the winter months, when facility usage is lowest and temperatures are lowest, lower coliform levels would be expected. One additional variable factor which affects coliform levels is the amount of water flowing through the swimming area. Water dilutes any contaminants or pollutants that come into the system. Petitioner attempted to show a correlation between rate of flow and coliform levels in excess of 1000 parts per 100 milliliters (ppm). (Petitioner's Exhibit #1) However, because the date collected did not control for and did not take into account the presence or non-presence of the variable factors which affect coliform levels, no conclusions could be reached regarding whether water quality could be maintained in the swimming area in accordance with HRS standards, with periodic adjustments to flow from the wells. No competent substantial evidence was offered to show that periodic adjustments to flow would prevent Petitioner from meeting HRS standards for water quality and therefore prevent Petitioner's continuing the operation of his public bathing facility. The original permit application filed by Petitioner only requested an allocation of 31.7 million gallons per year (mgy), this amount being only the water utilized for the campground. The construction of Petitioner's potable water supply for the campground was approved by the Florida Department of Environmental Regulation and meets all water quality standards applicable to the campground. Although the water used for the campground comes from a pipe connected to the 24-inch well, this request for water is not related to and does not account for the water which flows from the wells into the swimming area and out through Canoe Creek and is used for recreational purposes. The technical staff report (TSR) prepared by Respondent's staff recommends granting an allocation of 31.7 mgy of water to Petitioner for commercial and household uses (to supply the campground) and an allocation of 2.55 billion gallons per year (bgy) of water for recreational uses. The recommended allocation for recreational use breaks down to an average daily use of 7 million gallons per day (mgd), representing a 44 per cent reduction in the amount of water presently flowing from the wells for recreational purposes. The TSR further recommends a maximum daily use for any one day of the year of 18 million gallons of water. This recommendation actually exceeds the present production capacity of the wells. The TSR further recommends that the overall 44 per cent reduction in use of water for recreational purposes be achieved by adjustment of well discharges during non-use periods each day and seasonal non-use periods when bathing and marina use are minimal. This would require installation of operable valves on each of the wells as is also recommended in the TSR. Subject to the limitation imposed by the annual allocation and subject to the maximum daily allocation, Petitioner would make the flow adjustments as conditions warrant and as he sees fit. The Floridan aquifer in the region surrounding Petitioner's property is not expansive; thus there is a maximum amount of water which can be stored within it. Water will tend to discharge at some point within the system when flow is stopped at another point. The drawdown effect on the potentiometric head caused by the 24-inch well after flowing for a period of twenty-four hours can be calculated to extend up to two miles west of that well and further to the east. The excess water flowing through Petitioner's wells, over and above that required for recreational purposes, could be tapped and used by other potential consumers of water within the same vicinity, if Petitioner reduced the flow from his wells. Underlying the Floridan aquifer in the Wekiva River Basin Area is a layer of saline water, the degree of salinity being measured by the chloride concentrations in said water. This underlying saline water is relic sea water and is not salt water being pulled in from the oceans. When water is discharged from the Floridan aquifer and potentiometric pressures are thereby reduced, saline water is allowed to move upward and closer to the Floridan aquifer, resulting in higher chloride concentrations in the water discharged from the Floridan aquifer. The converse is also true. Reductions in discharge tend to increase potentiometric pressures which, in turn, would push the saline water further away from the Floridan aquifer. Chloride concentrations are the basic measurement of water quality. In measuring chloride concentrations in water, 250 milligrams of chloride per liter of water is the significant figure because this measuring point is the highest concentration of chloride that is recommended for public drinking water supplies. Data has been collected regarding chloride concentrations in water taken from the Floridan aquifer beneath the Wekiva River basin and shows significant changes during the period from 1973 to 1986. In a United States Geological Survey (USGS) study of water quality in the Floridan aquifer beneath the Wekiva River basin, conducted in 1973-74, an area or isochlor of water with chloride concentrations exceeding 250 (ppm) was identified. Petitioner's wells were included in this study, and the chloride level in his wells was measured at 230 ppm. The isochlor depicting water with chloride concentrations exceeding 250 ppm extended southward to a point north of Petitioner's property. A follow-up study begun in 1986 shows that the area or isochlor of water with chloride concentrations exceeding 250 ppm has extended itself, moving southward to include and pass the Petitioner's wells, past the Lake County border line which lies to the south of Petitioner's property and into Orange County, Florida. In 1986 Petitioner's wells produced water which measured 296 ppm and 312 ppm respectively. Because the 1986 study was not complete as of the time of hearing, no clear determinations can be made as to the extent to which the Petitioner's wells have contributed to the southward migration of the 250 mg/1 of chloride base line. At a minimum, the withdrawals of water from Petitioner's wells is having a localized impact in the immediate vicinity of those wells. Reduction of the flows from Petitioner's wells would, at a minimum, result in an improvement in the chloride levels in a localized area. That improvement in conjunction with similar improvements at other wells in the area could ultimately result in a more regional improvement of the chloride levels. Because of the factors observed indicating a deterioration of the aquifer systems in the face of increased demand, Respondent's staff has created Special Condition Zones in an effort to identify areas within the Wekiva River basin where hydrologic conditions warrant concern and special attention. Zone One, in which Petitioner's property is located, is the area of greatest concern because of observed changes within the hydrologic regime. Special permit conditions have been created for these zones to insure that no more water than is needed for a specific purpose is allocated to any user in the area. The flows from Petitioner's wells provide a benefit to the Wekiva River by diluting the pollutants which flow into the river. The cascading water from the standpipes aerates the water, which in turn increases the oxygen levels which is of benefit to the invertebrates, fish, and other animals that live in the water. The flows from Petitioner's wells account for approximately six or seven per cent of the flow of the Wekiva River at the gauging station at State Road 46. Nevertheless, no persuasive competent substantial evidence was offered to show that an overall 44 per cent reduction in flow from Petitioner's wells would in any significant way impact the quality of water in the Wekiva River. The District staff recommended that numerous "standard general conditions" and numerous "other conditions" which relate specifically to this project be incorporated in Petitioner's CUP permit. Those conditions are set forth at length in Respondent's Exhibit No. 6 and it would serve no useful purpose to repeat them all here.
Findings Of Fact Petitioner is the owner and developer of real property in Brevard County, Florida. On February 17, 1982, Petitioner filed with DER an application for a permit to construct three docks in the Indian River adjacent to its property. Subsequently, Petitioner withdrew its three-dock application and re- filed its application seeking approval for one dock pursuant to the exemption requirements contained in Rule 17-4.04(9)(c), Florida Administrative Code. The permit for the exempt dock was received by Petitioner on October 1, 1982. Petitioner then filed an application to construct three new docks, while retaining the exempt dock, by application dated November 4, 1982. DER issued an intent to deny this permit application. The three docks which Petitioner proposes to construct are designed to provide a total of 58 mooring slips. The docks are proposed to be constructed in the Indian River adjacent to Petitioner's upland development which is designed to contain 214 units at build-out. Construction of the three docks will involve expenditure of approximately 845,000, and provide approximately five jobs. At the site of the proposed dock construction, the Indian River is navigable, and is classified as a Class II water body. The area of the Indian River in which the proposed docks are to be constructed has been conditionally approved for shellfish harvesting by the Department of Natural Resources. Sampling conducted by both Petitioner and DER confirm the presence of edible clams on the project site and in adjacent areas. Clams are filter feeders which ingest water and entrap suspended particles which are utilized as food. Any contaminants contained in water ingested by clams are concentrated inside the clam until naturally purged. Human consumption of contaminated clams poses a public health hazard. Petitioner proposes to construct the docks by driving pilings into the river bottom with an air-driven hammer. As the air hammer drives the piling into the soil, it displaces the soil beneath the pilings, and densifies it into the shear zone on both sides of the pile. The piles are supposed to be driven approximately four to five feet into the river bottom. The construction and operation of the marina is not expected to diminish the amount of benthic activity in the project area. The habitat provided by pilings is expected to more than offset the loss of the area displaced by their installation. However, the potential for contamination of shellfish in the project area by fecal coliform bacteria and other pollutants will be significantly increased. Although the number of shellfish might not be severely impacted, their fitness for human consumption by virtue of ingestion of pollutants associated with operation of the facility is expected. In order to attempt to offset this expected impact, Petitioner has proposed several restrictions on persons utilizing the docking facilities. Among these are prohibiting detergents for washing boats; prohibiting dockside fueling facilities; prohibiting discharge of bilge water from inboard craft into the river; prohibiting the use of toilet facilities onboard water craft; and requiring boats and equipment to be maintained in good order. Petitioner proposes to have on-site personnel or a subsequently formed condominium association to enforce these requirements; however, no specific workable mechanism for enforcing these procedures was established of record by Petitioner. Petitioner submitted testimony concerning water quality sampling performed in the project area and in areas adjacent to the proposed site. However, no analysis was conducted over and extended period of time to show existing water quality, or to give any credible comparison between the proposed site and other nonresidential marinas in the area. Further, Petitioner conducted no analysis of bottom sediments in the proposed project area in order to determine the type and extent of any pollutants existing on-site which could be expected to be re-suspended in the water column as a result of intense marine activity. These omissions are significant in view of the fact that the waters of the Indian River in this area have been approved for shellfish harvesting. There are several existing marinas and boat ramps within close proximity to the Petitioner's development. Consequently, both the general public and residents at the development have ample access to the waters of Indian River and its surroundings. Petitioner has made no showing of any hardship which would justify the granting of a variance from DER permitting requirements.
The Issue The issue concerns the entitlement of GJPS Lukas, Inc. to be granted a consumptive use of water permit from the St. Johns River Water Management District. See Chapter 373, Florida Statutes, and Chapter 40C-2, Florida Administrative Code.
Findings Of Fact On December 7, 1990, the Applicant applied for a consumptive use of water permit under application no. 2-127-0808AN as submitted to St. Johns. The Applicant asked that it be allowed to withdraw water from the Floridian aquifer to irrigate a 240 acre sod farm by the use of four wells and a pipeline ditch irrigation system. This was a new use. On January 9, 1991, St. Johns prepared a technical staff report recommending approval of the application. Petitioner was provided notice of this pending disposition on January 15, 1991 leading to his protest to the grant of the permit. Petitioner's property is adjacent to the Applicant's property. Petitioner has a well which he uses for domestic water needs which is in the vicinity of the proposed project. He also has a commercial fish operation with a number of fish ponds including fresh water ponds. Both these uses may potentially be affected by the proposed consumptive water use contemplated by the Applicant. St. Johns calculated that the irrigation of 240 acres of sod, by calculation using the modified Blaney-Criddle formula pertaining to evapotranspiration, calls for a maximum extraction of 169.4 million gallons a year. In any one month the amount withdrawn should not exceed 37.4 million gallons. The Floridian aquifer at the place where the Applicant proposes to draw water is capable of the production of 169.4 million gallons of water per year and 37.4 million gallons per month without promoting environmental or economic harm. Extraction of this water for purposes of irrigation is an acceptable arrangement in that no wastewater treatment plants are within a five mile radius of the site of the proposed use. Therefore it would not be economically, technically or environmentally feasible for the Applicant to use reclaimed wastewater as a source for its irrigation needs. The aquifer in that area is stable. There was no showing in the hearing by competent evidence that saline water intrusion problems now exist in the area of the proposed site of withdrawal. There was no showing that the withdrawal of as much as 169.4 million gallons per year would cause a saline water intrusion problem. The fields where the Applicant intends to apply the extracted water for irrigation purposes are surrounded by a system of ditches and water control structures to confine the water as applied to the sod and any mixing of that water with any surface or subsurface waters that are contributed by rain events. The ditches and control structures keep the water on the property and prevent flooding downgradient of the subject property. As a consequence flood damage on adjacent properties is not to be expected. On a related issue, the ditches and control structures will prevent water from discharging into receiving bodies of water and thereby degrading water in those receiving bodies such as the fish ponds operated by the Petitioner. The water quality of the Floridian aquifer will not be harmed by the activities of the Applicant in withdrawing this water. In the worse circumstances the well used by the Petitioner will be affected by the Applicant extracting the water from the aquifer to the extent of .25 to .4 drawdown in feet in the well the Petitioner uses. This is not a substantial impediment to the Petitioner's ability to withdraw needed water from the well he uses. The Floridian aquifer in the area in question is semi-confined. The four wells that would be used in withdrawing water for the Applicant's purposes will extract the water at 110 feet below the surface. Between that level and the surface are three confining areas of clay totaling approximately 40 feet in thickness. Those confining units of clay would protect the water at the surface when the Applicant withdraws water and induces a gradient. In particular, the nature of the stratification in the soils in the area in question and the topography are such that the Petitioner's fish ponds, when taking into account the distance between the Applicant's operation and those fish ponds, the clay confining units and the gradient between the Applicant's property and the Petitioner's fish ponds, would not lead to a reduction in the water levels of the Petitioner's fish ponds when the water was extracted by the Applicant. The proposed use by the Applicant would not require invading another use reserved by a permit issued from St. Johns. St. Johns has not established minimum levels or rates of flow for the surface water in the area where the Applicant proposes to extract the water. Nor has St. Johns established a minimum level for a water table aquifer or a minimum potentiometric surface water for an aquifer in the area where the Applicant proposes to extract the water. The surficial aquifer water table beneath the property where the Applicant intends to apply the extracted water should not be raised inordinately should the Applicant follow the best management practice as recommended as special condition No. 9 to the Consumptive Use Technical Staff Report pertaining to this project. Nonetheless if the water table beneath the Applicant's property were to be raised to a level which is too high or if the activities by the Applicant would result in excessive surface water runoff the ditches and water control structures that isolate the Applicant's property would prevent the water level in the Petitioner's fish pond from being increased by the Applicant's proposed activities. The application of the extracted water and the expected flow pattern of water applied to the surface and control of that water is set out in St. Johns' Exhibit No. 5 and described in the testimony of Jack Caldwell Lawrence, Jr., employee of St. Johns and an expert in geology and hydrology. See pages 61 and 62 of the transcript. Concerning water quality in the Petitioner's fish pond, it will not be affected by the Applicant's proposed activities in extracting the water. The gradients and distances between the Petitioner's fish pond and the Applicant's fields do not allow surface water or water in the surficial aquifer, which is groundwater above the confining clay unit, to flow from the Applicant's fields into the Petitioner's fish ponds. Again the ditches and control structures related to the project offer additional protection against a compromise to the water quality in the Petitioner's fish ponds. The Technical Staff Report on this project is an apt description of the project and the necessary conditions to granting a permit which would protect the public and environment. One modification has been made to that report and that modification is appropriate. It changes the intended disposition from one of allowing surface water from the onsite management system to be used as the primary irrigation supply with the Floridian aquifer serving as a supplementary source to one in which the Applicant would not use the onsite management system as a water supply source but would use the onsite management system simply as a discharge holding area.
Recommendation Based upon the facts found and the conclusions of law reached, it is, RECOMMENDED: That a Final Order be entered which approves the application for consumptive use of water subject to the conditions set forth in the Technical Staff Report, excepting the need to have the Applicant utilize water from the onsite management system as the primary source of irrigation of its sod. DONE and ENTERED this 4th day of November, 1991, in Tallahassee, Florida. CHARLES C. ADAMS, Hearing Officer Division of Administrative Hearings The DeSoto Building 1230 Apalachee Parkway Tallahassee, Florida 32399-1550 (904) 488-9675 Filed with the Clerk of the Division of Administrative Hearings this 4th day of November, 1991. APPENDIX TO RECOMMENDED ORDER The following discussion is made of the suggested facts set forth in the proposed recommended orders. Petitioner's Facts Paragraphs 1-6 are subordinate to facts found. Concerning Paragraph 7, Petitioner does not have standing to take issue with the quality of notice provided to other adjacent landowners. As to Paragraph 8, the witness had sufficient understanding of the location and nature of the surficial or sand aquifer and the clay confining units to have his testimony credited. As to Paragraph 9 the fact that the witness is unaware of the exact depth of the Petitioner's fish pond does not cause his testimony to be disregarded in deciding that the fish ponds would not be negatively impacted by the activities contemplated in this permit application. As to Paragraph 10, this proposed fact is inconsequential given the de novo nature of this proceeding. As to Paragraph 11, see discussion of Paragraph 7. As to Paragraph 12, it is rejected. As to Paragraph 13, that knowledge was not necessary in determining the outcome here. As to Paragraph 14, it is accepted in hypothetical terms, however, no showing was made that chlorides would increase in this instance and adversely affect the Petitioner's fish based upon the evidence adduced at hearing. As to Paragraph 15, the soil samples from Petitioner's property are inclusive and less reliable that the description of soil in the general area as set forth by the witness for St. Johns. COPIES FURNISHED: Clayton D. Simmons, Esquire Stenstrom, Mackintosh, Julian, Colbert, Whigham and Simmons, P.A. 200 West First Street, Suite 22 Sanford, FL 32772-4848 Michael D. Jones, Esquire 996 Westwood Square, Suite 04 Oviedo, FL 32765 Michael D. Jones, Esquire Post Office Box 3567 Winter Springs, FL 32708 Eric T. Olsen, Esquire St. Johns River Water Management District Post Office Box 1429 Palatka, FL 32178-1429 Henry Dean, Executive Director St. Johns River Water Management District Post Office Box 1429 Palatka, FL 32178-1429
The Issue The issue for consideration in this hearing is whether the Respondent, W. B. Persico, should be issued a permit to construct a commercial marina as described in the Department's Intent to Issue, in Class III waters of the state in Charlotte County, Florida.
Findings Of Fact At all times pertinent to the issues herein, the Petitioner, Burnt Store Isles Association, Inc., was an association of property owners whose property is located in the Burnt Store Isles subdivision located in Charlotte County, Florida. The applicant, W. B. Persico, is the owner of a piece of property located adjacent to the subdivision and applicant for a permit to construct a marina on his property. The Department of Environmental Regulation is the state agency responsible for the regulation and permitting of dredge and fill activities in the waters of the state. Mr. Persico's property is located on a dead end basin canal in Charlotte County, Florida. The canal is a Class III water but is not classified as an Outstanding Florida Water. On July 31, 1989, Mr. Persico applied to the Department for a permit to construct a 75 slip, 5660 square foot commercial marina on his property within this artificial, dead end basin. Because of objections by the Department to several aspects of the proposed project, on February 27, 1990, Mr. Persico submitted a modification proposal in which he eliminated the use of pressure treated lumber for pilings, substituting concrete pilings; incorporated boat lifts in each slip; reduced the number of slips from 75 to 65; committed himself to installing a sewage pump-out facility at the site; committed to creating an inter-tidal littoral shelf planted with mangroves; agreed to face the existing vertical bulkhead seawall in the basin with rip-rap; and incorporated a commitment to include, as a part of his rental contract, long term agreements prohibiting vessel maintenance and liveaboards on boats at the site, and insuring the perpetual use of boat lifts and pump out facilities provided. He now proposes to market the marina as a condominium ownership operation. The basin in which the Persico project is proposed is 136 feet across at the entrance, (the narrowest point), and 326 feet across at the widest point. The length of the basin is more than 900 feet. The docking structure to be created will have fingers extending no more than 39 feet into the water from the existing vertical seawall. It will have a 4 foot wide walkway parallel to and 10 feet from the existing seawall from which the arms will extend 25 feet into the basin. The basin which is the proposed location for the marina is at the end of the easternmost canal in the Burnt Store Isles subdivision. It is located just west of and parallel to US Route 41, and at the entrance point, joins a perimeter waterway which meanders approximately 1 mile seaward toward a lock which joins that waterway to Alligator Creek which is an Outstanding Florida Water. The waterway from the basin through the lock into Alligator Creek and thereafter to the Gulf provides the only navigable access for most vessels moored in the Burnt Store canals and which would be moored in the proposed marina between Charlotte Harbor and the Gulf of Mexico. The lock which joints the Burnt Store canals to Alligator Creek consists of two hydraulically operated swinging gates which are operated by a boater entering or exiting the canal system. This lock was constructed as a part of a 1973 agreement between Punta Gorda Isles, Inc., a developer, and the state to prevent the construction and runoff polluted waters of the canal from freely mingling with the Outstanding Florida Water in Alligator Creek. The lock is now maintained in an open position from November 15 to May 15 because boaters complained of the inconvenience of having to operate the lock system. Available evidence indicates that a complete passage through the lock, one way when closed, takes 15 minutes. No more than 24 boats can complete a round trip in a 12 hour boating day. When the lock is open there is no appreciable delay. The residential lots which abut the Burnt Store canals are still mostly vacant. The City of Punta Gorda has assumed the responsibility of conducting a 5 year water quality monitoring program which was previously agreed to by Punt Gorda Isles, Inc. when the lock was built. The 1973 agreement was amended in 1984 to permit the operation of the lock in a closed position for an entire year if water quality monitoring should indicate a degradation of water quality in either Alligator Creek of the Burnt Store Isles canals. This has not been necessary. The Petitioners fear that pollution generated by the addition of 65 additional boats moored at and operating from the proposed marina will cause the Department to implement that clause and order the lock to operate from a closed position year round. This does not mean that the lock would not be opened for boats, but that it would be closed when not being used. Petitioners contend that the increased usage would create an intolerable traffic jam at the lock which would, for the most part, make their use of the waterway to the Gulf intolerable. Mr. Persico is a former road and bridge contractor. Though he has never owned a marina, at one time he rehabilitated one in the Chicago area. He has owned the property in question here for four years and now plans to develop a condominium ownership marina. When he decided to do so, he hired Mr. James M. Stilwell, an environmental consultant, to prepare and submit to the Department the application for the required dredge and fill permit. Initial discussions between Mr. Stilwell and the Department dealt with many environmental issues. Mr. Stilwell pointed out that the water in the canal might already be stale and avenues were explored to mitigate that problem. They did not discuss the type of docks to be installed or the potential for destruction of mangrove stands along the seawall, but even though the original plan called for the docks to be placed against the seawall, it was to be done in such a way as not to disturb the mangroves. The modified plan removing the docks to a point 10 feet off from the wall will obviate any damage to the mangroves. Admittedly, the original submittal prepared by Mr. Stilwell contained factors which were considered unacceptable to the Department. These included construction of the finger piers with pressure treated wood. To eliminate possible pollution from leaching, the pressure treated wood was replaced with a floating dock using concrete pilings. Liveaboards, and the potential contamination from that activity, have been prohibited. The provision and required use of a sewage pump-out facility should prevent any escape of polluting sewage into the waters of the basin. The use of power hoists at each slip should prevent pollution from bottom paint leaching, and boat maintenance at the marina is to be prohibited. Fueling of the vessels will not be permitted at the site thereby obviating the potential of polluting fuel spills. The construction of a 10 foot wide littoral shelf, planted with mangroves, between the dock and the sea wall will provide increased water filtration and improve water quality. It would also help the development of the fish and wildlife population and would reduce the flushing time. Air released into the water from the use of the boat lifts should add oxygen and contribute to improved water quality. At the present time, the ambient water quality in the basin, as it pertains to dissolved oxygen, is probably below standards in the lower depths of the basin, and of the outside channels as well, due to poor light penetration. The channel depth is anywhere from 20 to 25 feet. The oxygen level at the bottom is undoubtedly depleted. Mangroves are currently located along 300 feet of the 1,300 foot seawall. Mr. Stilwell's proposal, and that approved by the Department, does not call for removal of the mangroves, but they would be built around or possibly trimmed. Mr. Stilwell is of the opinion that provision for trimming of the mangroves is inherent in the granting of the permit though such permission was not specifically sought. There is no evidence to contradict this thesis. Water quality issues were raised subsequent to the filing of the original application, and the facility as now planned is designed to minimize impacts on the environment as best as can be done. Water quality would be improved, or at worst not adversely affected, by the prohibitions against liveaboards and fueling, the provision of boat lifts and a pump station, and the prohibition against other structures beyond the dock and slips. Flushing of the water is important considering the fact that the dissolved oxygen content in the water is already low. However, Mr. Stilwell is satisfied, and it would so appear, that water quality would be improved by the implementation of the proposals as included in the conditions to the permit. Mr. Stilwell, admittedly, did no dissolved oxygen tests because they were not considered as a part of the permit application. If the Department requests them, they are done, but they were not requested in this case. It is clear that the original application did not address all the environmental concerns that Petitioners feel are pertinent. Nonetheless, those items already discussed were treated, as were turbidity control during construction. As to others of concern to Petitioners, many are included in the state standards and need not be specifically addressed in the application. The Department considered the application in light of the state standards, and by the use of the conditions appended to the Intent to Issue, provided for the water quality and other environmental standards to be sufficiently addressed and met. In his February 22, 1990 letter to the Department, Mr. Stilwell directly addressed the public interest concerns including the mangroves and the construction of the littoral shelf. The Department was satisfied that the public interest criteria were met, and considered the plans to be environmentally sound. They appear to be so. Petitioners have raised some question as to the effect of the 39 foot long dock fingers interfering with navigation within the basin. Mr. Stilwell does not feel that the facility would create this problem, even at the narrowest point, and it is so found. The width of the canal there is 136 feet. The portion of the slip designed to accommodate vessels is no more than 25 feet long, and presumably, vessels of a length much greater than that would not visit the basin. Even subtracting 39 feet from the 136 feet narrow point, 97 feet of turning space remains, and this is almost four times the length of the normal vessel anticipated in the basin. Mr. Stilwell did not address the subject of the lock as it relates to navigation, but primarily as it relates to the impact on water quality and the environment. Nonetheless, he is of the opinion, and there is no evidence to the contrary, that keeping the lock open on a year round basis would not trigger a change to the ongoing program under the agreement between the state and Punta Gorda Isles and result in the lock being closed year round. Mr. Shultz, the environmental specialist with the Department, reviewed the application here initially for file completeness, and when all required information was in, made a site visit. He evaluated the application and the attachments for permitability. For Class III waters, the project must meet water quality standards outlined in the Department's rules. Only one of the water quality criteria, that of dissolved oxygen, was shown to be not met. Since the water was already below that standard, the test to be applied then is whether the project will create some improvement." In Mr. Shultz' opinion, planting the mangroves, as proposed by the applicant, does this, as does the use of the lifts. The existing mangroves will not be impacted by the project as it is proposed, and the use of rip-rap, as proposed, will provide additional surface area for organisms which will improve the water quality. When first reviewed, the Department had some concern about on-water storage of boats. These concerns were treated by the use of hoists to hold the boats out of the water when not in use, and as a result, pollutants will not be introduced by bottom paint leaching and, presumably, bilge pumping. Standard conditions included in all Department Intents to Issue, require the project to comply with applicable state water quality standards or to give assurances that such general standards for surface waters and Class III waters will be met. In this case, Mr. Shultz is satisfied that the applicant has demonstrated that water quality standards will be maintained, and there was no evidence presented by the Petitioners to contradict this. Once water quality standards are shown to be protected, then the project is balanced against the public interest criteria outlined in the statute. Here, the requirement is for a showing that the project is not contra to the public interest. It does not, because of its nature, require a positive showing that the project is in the public interest. In his opinion this project, as modified, will not adversely affect the health, safety and welfare of the public, (it will have no environmental effect on other property). It will not adversely affect the conservation of fish or wildlife in their habitats, (the planting of mangroves will provide a net improvement to species habitat in the area). The project will not adversely affect navigation, flow of water, or erosion, (the width and length of the dock system appear to pose no threat to navigation in the basin and there would appear to be no obstruction or potential therefor as a result of this project; the project is within a no-wake zone; and the size of vessels is limited by the slip size). The permit will not adversely affect marine productivity, (there is currently very little productivity in the area now since waters below 0 depth of 6 feet are already low in oxygen, and the project would, at least minimally, improve this condition). The project is permanent and would not adversely affect historical or archeological resources in the area, (there are no objects or known resources in the area, but a standard condition in the permit requires immediate notification if known resources or objects are found). The project would not adversely affect the current condition and relative value of functions being performed in the area since the area is currently a real estate development which is far from completely built. Based on his consideration of these criteria, Mr. Shultz concludes that the project is not contrary to the public interest and this appears to be a valid conclusion. There appears to be no evidence of sufficient weight, presented by the Petitioners, either through direct evidence or through cross examination of the applicant and Department witnesses that would tend to diminish the credibility of Mr. Shultz' analysis. If there are subsequent violations, the Department has enforcement action available. There is, consistent with the multiple use zoning category applied to the area across the basin from the marina, the potential for up to an additional 100 docks to be constructed in the basin beyond those treated here. Nonetheless, the Department does not consider 165 boats to be a problem either in the basin or at the lock. This is not necessarily a supportable conclusion, however. Those 100 additional docks do not currently exist and their potential should not be considered in determining whether to approve the permit under consideration here. In opposition to the applicant, Mr. Konover and Mr. Forsyth both indicated that the addition of 65 more boats would seriously overtax the operation of the lock and make it difficult, if not hazardous, to operate boats in that area between the Burnt Store Isles subdivision and Alligator Creek. Both individuals agree, and it is so found, that in general, motor boats pollute to some degree the waters on which that are operated as a result of oil leaks from engine operation, leakage of bilge oil, escape of sewage, and leaching of copper paint and other solvents. In addition, manatee have been seen in the area, and the increase of boating operations could present some hazard to the manatee population. There is, however, no indication that a manatee population is permanently in residence there or is even there frequently. It is also accepted that boat wake has an adverse effect on sea walls, and all of these factors should have been and, in fact were, considered in the analysis of the permitability of the project. The concerns of Mr. Konover and Mr. Forsyth were echoed by Mr. Gunderson who, over 30 years operating boats, has seen what he considers to be a definite lack of concern for the environment by many boaters who pump bilges directly into the water, throw debris overboard, and use detergents to wash their boats at marinas. He is of the opinion that renters of slips are generally less concerned about water quality than those who live on the water, and take a more cavalier approach to water quality standards. These sentiments are also held by Mr. Young who, over the years, has owned marinas in Connecticut and has observed the approach of nonowning slip users to the water at their disposal. His concerns could be met by the strict enforcement of standards at the marina. Mr. Powell, a nurseryman who owns the lot across the basin from the site of the proposed marina, fishes from his lot and has observed the an increase of pollution in the canal. He routinely sees floating dead fish, palm leaves, cocoanuts, bottles, slicks and other debris, and though he owns a multifamily lot, would have a difficult time putting in many slips since his lot, at the entrance to the basin at the narrow point, would be across from the slips proposed by applicant and their proximity would, he feels, hinder his ability to build out into the basin as well.
Recommendation Based on the foregoing Findings of Fact and Conclusions of Law, it is, therefore: RECOMMENDED that the Department of Environmental Regulation enter a Final Order issuing Permit No. 081679445, to W. B. Persico as modified and outlined in the Intent to Issue dated March 16, 1990. RECOMMENDED this 9 day of November, 1990, in Tallahassee, Florida. ARNOLD H. POLLOCK, Hearing Officer Division of Administrative Hearings The DeSoto Building 1230 Apalachee Parkway Tallahassee, Florida 32399-1550 (904) 488-9675 Filed with the Clerk of the Division of Administrative Hearings this 9 day of November, 1990. APPENDIX TO RECOMMENDED ORDER IN CASE NO. 90-3093 The following constitutes my specific rulings pursuant to S 120.59(2), Florida Statutes, on all of the Proposed Findings of Fact submitted by the parties to this case. FOR THE PETITIONER: 1. & 2. Accepted and incorporated herein. 3. & 4. Accepted. Accepted but applicable only when the locks are closed. Accepted. - 9. Accepted and incorporated herein. Accepted. & 12. Accepted and incorporated in substance herein. 13. & 14. Accepted and incorporated herein. Accepted and incorporated herein. Rejected as contrary to the weight of the evidence. Accepted and incorporated herein. & 19. Accepted and incorporated herein. 20. & 21. Unsupported by convincing evidence of record. Accepted as valid when the lock is operated from a closed position. However, the evidence indicates that currently the lock is left open from November 15 to May 15 of each year and this does not cause delay. Accepted if the lock is operated from a closed position. Unsupported by convincing evidence of record. FOR THE APPLICANT: 1. - 6. Accepted and incorporated herein. 7. - 15. Accepted and incorporated herein. Accepted and incorporated herein. & 18. Accepted and incorporated herein. Accepted and incorporated herein. Accepted. Accepted. - 32. Accepted and incorporated herein. FOR THE DEPARTMENT: Accepted. and incorporated herein. - 4. Accepted and incorporated herein. Accepted and incorporated herein. Accepted and incorporated herein. Accepted and incorporated herein. & 9. Accepted and incorporated herein. 10. - 14. Accepted and incorporated herein. 15. - 18. Accepted and incorporated herein. COPIES FURNISHED: Joseph F. Lynch Burnt Store Isles Association, Inc. P.O. Box 956 Punta Gorda, Florida 33951-0956 Michael P. Haymans, Esquire P.O. Box 2159 Port Charlotte, Florida 33949 Cecile I. Ross, Esquire Department of Environmental Regulation 2600 Blair Stone Road Tallahassee, Florida 32399-2400 Dale H. Twachtmann Secretary Department of Environmental Regulation 2600 Blair Stone Road Tallahassee, Florida 32399-2400 Daniel H. Thompson General Counsel Department of Environmental Regulation 2600 Blair Stone Road Tallahassee, Florida 32399-2400
Findings Of Fact B. D. Taylor, Respondent, is the owner of a wastewater treatment facility near Panama City, Florida, which serves a community of some 125-150 mobile homes at Lane Mobile Home Estates. The facility has a 24,000 gallons per day capacity to provide secondary treatment of wastewater with percolating ponds. It was first permitted in 1971 upon construction and has been in continuous operation since that time. In 1980 Respondent employed the services of a consultant to apply for a renewal of its temporary Permit to operate a wastewater treatment facility. This application stated the temporary operating permit (TOP) was needed to give Respondent time to connect to the regional wastewater treatment facility. The schedule contained in the following paragraph was submitted by Respondent at the time needed to accomplish this objective, Following inspection of the facility, a TOP was issued December 5, 1980 (Exhibit 1), and expired January 1, 1983. TOPs are issued to facilities which do not comply with the requirements for Wastewater treatment. Exhibit 1 contained a schedule of compliance to which Respondent was directed to strictly comply to stop the discharge of pollutants from the property on which the facility is located. These conditions are: Date when preliminary engineering to tie into regional will be complete and notification to DER. July 1, 1981; Date when engineering to tie into regional system will be complete and notification to DER - June 1, 1982; Date construction application will be submitted to phase out present facility - March 1, 1982; Date construction will commence - June 1, 1982; Date construction is to be complete and so certified - October 1, 1982; and Date that wastewater effluent disposal system will be certified "in compliance" to permit - January 1, 1903. None of these conditions or schedules has been met by Respondent. The regional wastewater treatment facility was completed in 1982 and Respondent could have connected to this system in the summer of 1982. This wastewater treatment facility is a potential source of pollution. The holding ponds are bordered by a ditch which is connected to Game Farm Greek, which is classified as Class III waters. The size of Game Farm Creek is such that any discharge of pollution to this body of water would reduce its classification below Class III. On several occasions in the past there have been breaks in the berm surrounding the holding ponds which allow the wastewater in the holding ponds to flow into the ditch and into Game Farm Creek. Even without a break in the berm, wastewater from these holding ponds will enter Game Farm Creek either by percolation or overflow of the holding ponds caused by the inability of the soil to absorb the effluent. On January 28, 1983, this facility was inspected and the results of the inspection were discussed with the operators of the facility. The plant was again inspected on February 8 and February 18, 1983. These inspections disclosed solids were not settling out of the wastewater in the settling tanks; inadequate chlorination of the wastewater was being obtained in the chlorination tanks; samples taken from various points in the system, the ditch along side the holding tanks and in Game Farm Creek, disclosed excess fecal coliform counts; and that very poor treatment was being afforded the wastewater received at the plant as evidence by high levels of total Kejhdal nitrogen and ammonia, high levels of phosphates, high biochemical oxygen demand, and low levels of nitrates and nitrites. In July, 1983, in response to a complaint about odors emanating from the plant, the facility was again inspected. This inspector found the aeration tanks anaerobic, effluent had a strong septic odor, the clarifier was cloudy, the chlorine feeder was empty, no chlorine residual in contact tank, final effluent was cloudy, both ponds were covered with duckweed and small pond was discharging in the roadside ditch (Exhibit 14) Expenses to Petitioner resulting from the inspections intended to bring Respondent in compliance with the requirements for wastewater treatment facilities are $280.32 (Exhibit 9)
The Issue Whether, under the facts and circumstances of this case, Respondent's license to practice engineering in the State of Florida, should be revoked, suspended, or otherwise disciplined.
Findings Of Fact Upon consideration of the oral and documentary evidence adduced at the hearing, the following relevant facts are found: At all times material to this proceeding, Respondent, L. Thomas Hubbard d/b/a The Hubbard Association, was licensed to practice professional engineering in the State of Florida, having been issued license number PE 006634 on August 17, 1962. Certificate of authorization number EB0003297 was issued to the firm, The Hubbard Association, Inc., on September 25, 1981. In March 1986, Respondent prepared a set of plans for the proposed City of Macclenny Wastewater Treatment Works Improvement Program, Sewage Treatment Facility ("Macclenny project"), and one volume of "Contract Documents and Specifications" ("specifications"), which were submitted to the State of Florida Department of Environmental Regulation, Bureau of Wastewater Management and Grants (Bureau) on or about April 24, 1986. All wastewater treatment plans designs must go to the DER for approval prior to construction, and if a public entity wants grant funding for its wastewater treatment facility, the project must be reviewed and approved by the Bureau (now called Bureau of Local Government and Waste Water Financial Assistance) which administers State grant programs for wastewater treatment facilities. The Bureau reviews grant project plans and specifications to ensure that they: (a) comply with administrative requirements of the grants programs; (b) comply with minimum Federal and/or State technical standards for wastewater facilities; (c) are suitable for bidding; and (d) present a constructible project. The plans for the Macclenny project depict an existing treatment facility, a new clarifier to improve the removal of solids (an expansion of about 130,000 gallons per day in treatment capacity), and a new effluent pumping station to pump to an overland flow field (field) through a force main pipeline to spray risers. The risers would spray the water laterally across the field. Water would collect in a central collection ditch, and run through a final chlorine contact chamber prior to discharge in Turkey Creek. A new agricultural building for equipment storage, and a new holding pond, which is an off-line pond for storage of inadequately treated water, are also depicted. The field in the Macclenny project is roughly 24 acres and is located in a large area between the chlorine contact chamber and the holding pond. The field in this system has 5 cells. A cell is an area of land that can be independently controlled to allow loading/resting cycles in the treatment process. Each cell in a given field should be as near equal in size as possible to provide for equal treatment of the wastewater during the loading/resting cycles. Loading/resting cycles allows a cell within the field to "rest" (no effluent being pumped on to that cell) so maintenance mowing or harvesting can be accomplished and to "load" the other cells to revitalize the bacteria that renews the treatment process. "Load" means to apply the effluent or treated wastewater from the existing facility to the field. Generally, forty percent of the field would be loaded with wastewater at any one time. On December 9, 1985, the Bureau had a predesign conference with Respondent in Macclenny to discuss design items. No plans or specifications for the Macclenny project had been submitted at that time, nor were they submitted at this conference. On February 18, 1986, an in-progress design review was held at Macclenny, with the Bureau staff available to answer Respondent's questions. On March 5, 1986, another in-progress design review meeting was held in Macclenny, with the Bureau staff present, at which time the plans were "fifty percent" (50%) complete. The unsigned and unsealed plans were given to the Bureau for a preliminary review. On March 25, 1986, the Bureau issued a few preliminary comments on the 50% completed plans and specifications. The purpose of the 50% complete review is to help the design engineer complete his plans and specifications. On March 31, 1986, Respondent transmitted to the Bureau a set of plans for the proposed Macclenny project. Respondent's transmittal letter, which the Bureau received with the plans on April 11, 1986, stated that "completed plans" were being transmitted. On April 21, 1986, Respondent transmitted to the bureau an additional set of the same plans for the Macclenny project, which Respondent again referred to as "completed plans" on his transmittal letter form which were received by Bureau on April 24, 1986. This transmittal also included specifications, a design data check list, design calculations, cost estimate, and plan of operation. The plans in this submittal are referred to as "the plans." It was Respondent's understanding that signing and sealing a set of engineering drawings signified a legal obligation that if someone takes the plans and builds a project it will work. Respondent's signature and seal are on the first sheet of the set of plans which was in the April 1986 submittal but not on the specifications. The plans were prepared, signed, sealed and submitted to the Bureau for review by Respondent. Respondent did not place any conditional language or qualification on the plans or write a letter advising the Bureau that the plans were not complete. It was Respondent's understanding that the Bureau would not review a set of plans unless they were signed and sealed, notwithstanding the completeness of the plans. Respondent did not consider the plans as completed, notwithstanding that he had signed, sealed and submitted them to Petitioner as "completed". It was Respondent's understanding that the plans were being submitted for review only, not complete for construction. An engineer may get answers from the Bureau without submitting plans that are signed and sealed as completed, such as the predesign conference or 50% review that occurred in this case. The Bureau considers plans that are signed, sealed and submitted as "completed" for review to be 100% complete and ready to bid. The Bureau considered the plans and specifications which Respondent submitted on April 24, 1986 as being final, complete plans and specifications for final review by the Bureau. The Bureau reviewed the plans assuming them to be complete and followed normal procedures for reviewing a complete set of plans and specifications. On June 19, 1989, the Bureau issued 52 written comments based on its review of the plans and specifications it had received in the April 24, 1986 submittal from Respondent. The plans and specifications were submitted to the Department of General Services (DGS) by the Bureau for a review and opinion because the Bureau was concerned about the structural design. DGS responded to this request through Jim Berkstresser, P.E. on June 25, 1986. By cover letter dated July 18, 1989, Respondent filed written responses to the Bureau's 52 comments. The Bureau did not approve Respondent's plans and specifications for the Macclenny project submitted on April 24, 1986. On September 5, 1986, Respondent resubmitted plans in response to the Bureau's 52 comments. These plans had the same configuration as the April submittal regarding the overland flow treatment. On September 29, 1986, Respondent met with David Wolfe to discuss the field configuration for the proposed overland flow system and other outstanding issues related to the revised contract documents. The principal concerns were non- uniform flow and significant erosion potential. Respondent's plans did not follow accepted design criteria. At this meeting field configurations were discussed, as well as guidelines to be followed in design of the overland flow field, and a general field layout were developed. Respondent submitted another set of plans which the Bureau received on October 30, 1986, and that set was approved and stamped accepted by DER-BWMG on December 22, 1986. All sheets in the approved set are dated August 20, 1986, with the exception of the cover sheet on which Respondent failed to date his seal and signature, and sheets G-6 and G-7 which are dated October 24, 1986. Respondent signed and sealed the cover sheet and sheet G-7 of the approved set of plans, but did not seal any other sheets in the approved set of plans. A signature and seal on a set of plans indicates that the plans were prepared by, or under the direct supervision of the person signing and sealing them, and that the plans are complete and depict a project that will perform its intended function. A signature and seal on a set of plans means the engineer assures that the design is his design and that the plans and specifications are ready to be bid for construction. The design should contain criteria and information significant to ensure the project will work. Sheet flow is the primary treatment mode in an overland flow system. Sheet flow is where a thin layer of water is induced to flow in a very controlled atmosphere across a length of land that is functioning very similarly to a trickling filter. The acceptable range of slope of an overland flow system is 2% to 8% with the best results obtained in the lower range because of a longer "residence time". "Residence time" is the amount time the wastewater is on the field for treatment. The slopes must be even and uniform to maintain a constant velocity so as to minimize the potential for erosion and to maintain a constant depth of water throughout the filed so as to maximize the treatment. Cross slopes should be minimized and topographic lines should be as close to parallel as possible on the field. The plans for the Macclenny project shows: (a) slopes ranging from less than 2% up to 6%; (b) multiple compound slopes across the field and; (c) topographic lines that are not parallel. The specifications for the field do not set out the acceptable tolerances on the slopes or the acceptable level of compaction of the field for the contractor who is to construct the field and; therefore, lacks control over the final product. Contours in an overland flow field are important, and while it is desirable for them to be on 1-foot intervals, contours at intervals of 2 feet are acceptable provided the plans and specifications address what happens between the contours. Respondent's plans and specifications show contours at intervals of 2 feet but do not address what happens between the contours. The plans of the facilities that were approved prior to the submittal of any plans by Respondent called for a 2- 3 week loading/resting cycle. The standard practice is to have all cells within an overland flow field to be of equal size so that the area to be loaded at any given period of time is the same size. The cells in the overland flow field in the Macclenny project as depicted by the plans are not of equal size, and if operated on a 2-3 week loading/resting cycle would not provide a consistent amount of treatment and thereby result in varying levels of treatment of the effluent. It is standard practice to provide performance specifications for seeding the field with the primary grass cover and for overseeding when necessary to prevent wind and water erosion. There were no performance specifications in the plans and specifications on the Macclenny project submitted by the Respondent. Agricultural equipment is an integral part of the overland flow field system and has a direct bearing on whether the system will function over the long run. Specifications for agricultural equipment are necessary to determine if the system will work properly. There were no specifications for agricultural equipment submitted by the Respondent in the plans. It is standard practice to furnish spray nozzle specifications, such as nozzle size, degree of fanning, characteristics under varying pressures and how much water will be discharged by the nozzle, in a set of plans and specifications for an overland flow field. Respondent's specifications for the Macclenny project did not contain the necessary specifications for the spray nozzles. Compacting is a standard practice, and it is standard practice to show compaction requirements on plans or specifications. The usual practice is to investigate the soil and specify compaction, usually based on a foundation report by a geo-technical engineer, showing the safe beading capacity of the soil in what condition, with recommendations for compaction. The Respondent's specifications do not call for compaction of the soil under the clarifier slab. However, the Respondent's specifications do call for compaction in the holding pond and situations where an area is over-excavated and backfilled. Should the area under the clarifier slab be over- excavated and backfilled, then compaction is covered in the specifications but compaction would not be covered unless this occurs. Therefore, since the weight of the slab is carried by the soil beneath it, specifications for compaction should have been included in Respondent's specifications for any situation. Changes in temperature causes concrete to expand or contract which may result in cracking. Placement of a concrete slab may result in the slab bending which may result in cracking. Therefore, reinforcing a concrete slab is required to maintain the slab's integrity. The thickness of a concrete slab will determine the distribution of the reinforcing so that cracking is minimized. The clarifier slab in the Macclenny project is depicted as being 12 inches thick and shows number 6 bar reinforcing on 6 inch centers in the top of the slab but no reinforcing in the bottom of the slab. Failure to require reinforcing in the bottom of the slab could result in the slab cracking due to significant changes in temperature and soft spots in the soil beneath the slab. Failure to place reinforcing in the bottom as well as in the top of the slab is not in accordance with standards of the code of the American Concrete Institute (ACI), revised in 1983, and is a structural weakness. The chlorine contact chamber as detailed on sheets 5-6 and 5-7 is like a rectangular concrete box beneath the earth where the earth is within a few inches of the top of the walls. The walls are vertically reinforced with number 4 bars on 12 inch centers placed in the center of the 8 inch thick wall. When the tank is empty the reinforcing bars will be approximately 160 per cent overstressed from the active pressure of the earth. Additional reinforcing is needed in the walls to meet ACI standards. There are deficiencies in the vertical wall reinforcing of the chlorine contact chamber as detailed on sheets 5-6 and 5-7 of the Plans. On sheets 5-3, 5-4 and 5-7 of the plans, reinforcement through the construction joints is incorrectly detailed to assure that cracking of the concrete will not occur. Construction joints occur between different pours of concrete, such as where the walls meet the top of the bottom slab. The concrete bottom of the holding pond as detailed in sheet 5-8 of the Plans is large enough to require expansion joints to prevent cracking as the slab expands and contracts due to changes in the weather, yet no expansion joints are shown for the slab as detailed on sheet 5-8 of the plans. Neither the collection ditches nor the spray riser bases as detailed on the plans show any reinforcing to maintain the integrity of the concrete. While this is not a major structural weakness, it indicates a failure to comply with standard structural engineering practices. Although the plans call for relocation of an existing drainage ditch, the Respondent failed to consult DER regarding the permitting of such drainage ditch. A detention time of 30 minutes is required to properly disinfect wastewater and is-basic knowledge for all civil engineers, yet the plans called for only a fifteen minute detention time. It is standard engineering practice to provide flood level elevations on the site plans. Respondent failed to provide flood level elevations for the Macclenny facility site plans. The plans failed to: (a) provide elevations for high water alarm and pump off settings; (b) provide specifications for flume liner on sheet M-4; (c) show how to close an existing outlet on the chlorine contact chamber; (d) show where an effluent pump station was to be located; (e) show pressure relief valve locations and; (f) indicate quantities for purpose of contract bidding. The specifications list equipment and work items, such as pumping equipment, grit storage tank, case-out assembly, telescoping valve, air diffusers, portable pump, hose and couplings, that are inapplicable to the Macclenny project. There are inconsistencies in the plans and specifications, such as: (a) the plans showing one clarifier while the specifications call for two clarifiers, (b) the plans showing a 150 pound chlorine cylinder as opposed to a 1-ton chlorine cylinder in the specifications and; (c) the plans showing the clarifier with a 38-foot diameter while the specifications calls for a clarifier with a 40-foot diameter. Respondent was negligent in submitting incomplete plans to the Bureau as "completed plans" and in failing to utilize due care and failing to have due regard for acceptable standards of engineering principles, with regard to the content of those plans which he submitted as "completed plans".
Recommendation Having considered the foregoing Findings of Fact and Conclusions of Law, the evidence of record, the candor and demeanor of the witnesses and the circumstances surrounding this case, it is, therefore, RECOMMENDED that the Board enter a Final Order finding Respondent, L. Thomas Hubbard guilty of violating Section 471.033(1)(g), Florida Statutes, and for such violation impose an administrative fine of $1,000.00 and suspend from the practice of engineering for a period of thirty (30) days, stay the suspension and place the Respondent on probation for a period of one year under terms and conditions the Board deems appropriate. DONE AND ENTERED this 20th day of June, 1990, in Tallahassee, Leon County, Florida. WILLIAM R. CAVE Hearing Officer Division of Administrative Hearings The DeSoto Building 1230 Apalachee Parkway Tallahassee, Florida 32301 (904) 488-9675 Filed with the Clerk of the Division of Administrative Hearing this 20th day of June, 1990. APPENDIX TO THE RECOMMENDED ORDER IN CASE NO. 89-0096 The following constitutes my specific rulings pursuant to Section 120.59(2), Florida Statutes, on the Proposed Findings of Fact submitted by the Petitioner in this case. Specific Rulings on Proposed Findings of Fact Submitted by the Petitioner Adopted in Findings of Fact 1. Rejected as not being necessary to the conclusions reached in this Recommended Order. 3.-12. Adopted in Findings of Fact 2, 3, 4, 5, 6, 7, 8, 9, 10, and 11, respectively, but modified. 13. Rejected as being immaterial or irrelevant or unnecessary or subordinate. 14.-19. Adopted in Findings of Fact 12, 13, 14, 15, 16, and 17, respectively, but modified. Rejected as being immaterial or irrelevant or subordinate or unnecessary. Adopted in Findings of Fact 17 and 18 but modified. 22.-33. Adopted in Findings of Fact 19, 20, 21, 22, 23, 24, 24, 25, 26, 27 and 27, respectively, but modified. 34. Adopted in Findings of Fact 17 and 18, but modified. 35-37. Rejected as being immaterial or irrelevant or unnecessary or subordinate. 38. Adopted in Findings of Fact 28 and 29, but modified. 39.-40. Rejected as being immaterial or irrelevant or unnecessary or subordinate, but see Findings of Fact 37 and 38. 41.-5O. Adopted in Findings of Fact 28, 32, 29 (28-31), 29, 29, 32, 30, 32 and 32, respectively, but modified. 51. Rejected as being immaterial or irrelevant or unnecessary or subordinate. 52.-53. Adopted in Findings of Fact (28-33) and 32, respectively, but modified. 54.-55. Rejected as being immaterial or irrelevant or unnecessary or subordinate. Adapted in Finding of Fact 55. Rejected as being immaterial or irrelevant or unnecessary or subordinate. 58.-62. Adopted generally in Findings of Fact 28-33. 63.-66. Adopted generally in Findings of Fact 34-36. 67.-72. Adopted generally in Finding of Fact 37. 73.-74. Adopted generally in Finding of Fact 38. 75.-76. Adopted generally in Finding of Fact 39. 77.-79. Adopted generally or covered in Findings of Fact 13-15 and 28-39. 80.-82 Adopted generally or covered in Findings of Fact 40- 41. 83.-90. Adopted generally or covered in Findings of Fact 42 and 43. 91.-96. Adopted generally or covered in Findings of Fact 44 and 45. 97.-104. Adopted generally or covered in Finding of Fact 46. 105.-107. Adopted generally or covered in Finding of Fact 47. 108.-109. Adopted in Finding of Fact 48. 110.-115. Adopted generally or covered in Finding of Fact 55. 116.-117. Adopted in Finding of Fact 49 and 50. 18. Rejected as being immaterial or irrelevant or unnecessary or subordinate. 119. Adopted in Finding of Fact 51. 120.-124. Adopted in Finding of Fact 52. 125. Rejected as immaterial or irrelevant or unnecessary or subordinate. 126.-127. Adopted in Finding of Fact 52. Adopted in Finding of Fact 53. Adopted in Finding of Fact 54. Adopted in Finding of Fact 53. Adopted in Finding of Fact 55. Specific Rulings on Proposed Findings of Fact Submitted by the Respondent Adopted in Findings of Fact 13-15. Adopted in Finding of Fact 19 except last sentence that is rejected as being immaterial or irrelevant. Rejected as being a restatement of Administrative Complaint and not a Finding of Fact but see Findings of Fact 15 and 19. Rejected as being a restatement of John Sowerby's testimony and not a Finding of Fact, but see Findings of Fact 15, 17 and 18. Adopted in Finding of Fact 15. 6. Restatement of David Wolfe's testimony COPIES FURNISHED: Rex Smith Executive Director Department of Professional Regulation 1940 North Monroe Street Suite 60 Tallahassee, Florida 32399-0792 Kenneth Easley, Esquire General Counsel Department of Professional Regulation Northwood Centre 1940 North Monroe Street Tallahassee, FL 32399-0750 Wings S. Benton, Esquire 1020 D. Lafayette Street, Suite 205 Post Office Box 5676 Tallahassee, Florida 32314-5676 L. Thomas Hubbard, pro se THA Building 3110 Spring Glen Road Jacksonville, Florida 32207
The Issue The issues set forth in DOAH Case No. 84-3810 concern the question of whether the State of Florida, Department of Environmental Regulation (DER) should issue a permit to Homer Smith d/b/a Homer Smith Seafood (Homer Smith) to construct a wastewater treatment facility which is constituted of a screening mechanism, dissolved air flotation treatment system, sludge drying bed, pumping station and subaqueous pipeline. In the related action, DOAH Case No. 84-3811, the question is raised whether DER should issue a dredge and fill permit to Homer Smith for the installation of the aforementioned pipeline along submerged lands in Trout Creek, Palmo Cove and the St. Johns River.
Findings Of Fact Introduction and Background In 1982, Homer Smith, under the name of Homer Smith Seafood, established a calico scallop processing facility in the vicinity of the intersection of State Road 13 and Trout Creek in St. Johns County, Florida. From that point forward, Smith has owned and operated the processing plant. His plant adjoins Trout Creek, which is a tributary to the St. Johns River. Both Trout Creek and the St. Johns River are tidally influenced waters that are classified as Class III surface waters under Rule 17-3.161, Florida Administrative Code. The processing undertaken by Smith's operation at Trout Creek contemplates the preparation of the scallops for human consumption. In particular, it involves the purchase of calico scallops from Port Canaveral, Florida, after which the scallops are transported by refrigerated trucks to the processing plant. They are then unloaded into metal hoppers and directed into rotating tumblers which separate out the scallops from sand, mud and other extraneous material. The scallops are placed in a steam tumbler that removes the shells and then passed through a flow tank that washes away sand, grit and shell particles. The scallops are next passed through eviscerators. These eviscerators are long tubes of aluminum with roughened surfaces that pull the viscera off of the scallops. The detached scallops are then sent along a conveyor belt, with scallops in need of further cleaning being picked out and sent to a second eviscerator. The eviscerated scallops are then chilled and packed for marketing. It is the viscera and wastewater associated with this material that is the subject of permitting. Homer Smith is one of about six automated scallop processing plants located in Florida. Two other plants are within St. Johns County, on the San Sebastian River in St. Augustine, Florida. Three other plants are located in Port Canaveral, Florida. When Smith commenced his operation of the scallop processing plant in the summer of 1982, he discharged the scallop processing wastewater into an area described as a swamp with an associated canal which connected to Trout Creek. By the fall of 1982, Smith had been told by representatives of the Department of Environmental Regulation that to operate his facility with the discharge would require a permit(s) from DER. At the time of this discussion, automatic scallop processing was an industry for which appropriate wastewater treatment alternatives had not been specifically identified by the Department of Environmental Regulation or the United States Environmental Protection Agency. This was and continues to be the case as it relates to the promulgation of technology-based effluent limitations designed for calico scallop processors. This circumstance is unlike the situation for most other industries for which DER has established technology-based effluent limitations. To rectify this situation, Florida Laws 85-231 at Section 403.0861, Florida Statutes, requires DER to promulgate technology-based effluent limitations for calico scallop processors by December 1986. In the interim, consideration of any permits that might be afforded the calico scallop processors by the exercise of DER's regulatory authority must be done on a case-by-case basis, when examining the question of technology-based effluent limitations. DER sent a warning letter to Smith on April 20, 1983, informing the processor that discarding its wastewater into Trout Creek without a DER permit constituted a violation of state law. After the warning letter, scallop harvesting declined to the point that by mid-June of 1983 the plant had closed down, and it did not reopen until the middle part of September 1983. Upon the recommencement of operations, DER issued a cease and desist notice and ordered Smith to quit the discharge of wastewater from the facility into Trout Creek. On the topic of the cease and desist, through litigation, Smith has been allowed the right to conduct interim operation of his business which involves direct discharge of wastewater into Trout Creek, pending assessment of wastewater treatment alternatives and pursuit of appropriate DER permits. 1/ When Smith filed for permits on April 10, 1984, he asked for permission to dredge and fill and for construction rights pertaining to industrial wastewater discharge into the St. Johns River. The application of April 10, 1984, involved the installation of a wastewater treatment system and an associated outfall pipeline to transport treated wastewater to the St. Johns River from the plant location. This system would utilize a series of settling tanks and a shell-filter lagoon as the principal wastewater treatment. DER, following evaluation, gave notice in October 1984 of its intent to issue permits related to dredge and fill and the construction of the wastewater treatment facility. In the face of that notification, the present Petitioners offered a timely challenge to the issuance of any DER permits. In considering treatment alternatives, Homer Smith had employed various consultants and discovered that treatment beyond coarse screening had not been attempted in processing calico scallop wastewater. Those consultants were of the opinion that conventional treatment methods such as clarification, sand filtration, vortex separation, breakpoint chlorination, polymers and spray irrigation were of limited viability due to the inability to remove key constituents within the waste stream or based upon certain operational difficulties that they thought would be experienced in attempting those methods of treatment. As envisioned by the April 10, 1984, application for permit, interim treatment of the wastewater was provided by the use of a series of settling tanks and a shell-filter lagoon, within which system adjustments were made to the delivery of wastewater treatment. The April 10, 1984, permit application by Smith did not envision any chemical treatment of the wastewater aside from that which might occur in association with the settling and filtration through the shell-filter lagoon. Following DER's statement of intent to issue a permit for construction of the wastewater treatment facility as described in the April 10, 1984, application by Smith, DER became concerned about the potential toxicity of calico scallop wastewater, based upon its own studies. As a consequence, Smith amended the application for wastewater treatment facility to include use of chemical coagulation and flotation. This amendment occurred in March 1985, and the wastewater treatment process in that application envisioned the use of an electroflotation wastewater system. In view of toxicity problems experienced with the testing related to the use of an electroflotation wastewater treatment system, this treatment alternative was discarded in favor of a dissolved air flotation (DAF) system. This system was pursuant to an amendment to the application effective May 31, 1985. This amendment of May 1985 was in furtherance of the order of the hearing officer setting a deadline for amendments to the application. DER issued an amended intent to grant permits for the DAF unit and the associated pipeline and that action dates from June 28, 1985. The Petitioners oppose the grant of these permits for the DAF unit and pipeline, and under the auspices of their initial petition have made a timely challenge to the grant of a permit for the installation of the DAF wastewater treatment unit and associated pipeline. It is the DAF unit and pipeline that will be considered in substance in the course of this recommended order. On July 6, 1984, Smith sought an easement from the State of Florida, Department of Natural Resources (DNR) for the installation of the pipeline. This was necessary in view of the fact that the pipeline would traverse sovereignty lands which were located beneath Trout Creek, Palmo Cove and the St. Johns River. On December 17, 1984, DNR issued a notice of intent to submit that application to the Board of Trustees of the Internal Improvement Trust Fund with a recommendation of approval. This action was challenged by the Petitioners on January 7, 1985, in a petition for formal hearing challenging the grant of the easement. DOAH Case No. 85-0277 concerns this challenge to grant of an easement. Originally, by action of January 28, 1985, the easement case was consolidated with the present DER permit actions. At the instigation of DNR, the easement case was severed from consideration with the present action. The order of severance was entered on July 31, 1985. The DNR case will be heard on a future date yet to be established. The DNR case was severed because that agency preferred to see test results of treatment efficiencies following the construction of the DAF unit. By contrast, the present DER cases contemplate a decision being reached on the acceptability of the construction of the DAF unit and attendant features, together with the pipeline on the basis of theoretical viability of this entire system. This arrangement would be in phases in which the construction of the upland treatment system would occur within 90 days of the receipt of any construction permit from DER, followed by a second phase within which Smith would construct the pipeline within 60 days of receipt of any other necessary governmental approval, such as the DNR easement approval. Furthermore, DER would wish to see the results of an integrated treatment system involving the upland treatment by the DAF unit and its attendant features and the use of the pipeline and the availability of a mixing zone, that is to say the end of pipe discharge, before deciding on the ultimate question of the grant of an operating permit for the wastewater treatment system. The quandary presented by these arrangements concerns the fact that discharge from the DAF treatment unit would be temporarily introduced into Trout Creek, pending the decision by DNR to grant an easement for the pipeline and the necessary time to install that pipeline. Given the difficult circumstances of these actions, there is raised the question of the propriety of discharging wastewater into Trout Creek pending resolution of the question of whether DNR wishes to grant an easement to place the pipeline over sovereignty submerged lands. This is a perplexing question in view of the fact that DNR requested severance from the present action, thereby promoting further delay in the time between any installation of the upland treatment system and the pipeline. Finally, Trout Creek is an ecosystem which has undergone considerable stress in the past, and it is more susceptible to the influences of pollution than the St. Johns River would be as a point of ultimate discharge from the pipeline. This dilemma is addressed in greater detail in subsequent sections within the recommended order. Petitioner River Systems Preservation, Inc., is a nonprofit organization comprised of approximately seven hundred persons. The focus of the organization is to protect and enhance the environment of northeast Florida. The individual Petitioners, Pinkham E. Pacetti, Robert D. Maley, Ruth M. Whitman and others, are members of the corporation who own property or live near the scallop processing plant of Respondent Smith. In addition, Pacetti owns a marina and recreational fishing camp that is located across Trout Creek from Smith's plant. Pacetti's fish camp dates from 1929. On the occasion of the opportunity for the public to offer their comments about this project, a significant number of persons made presentations at the public hearing on August 29, 1985. Some members of the public favored the project and others were opposed to the grant of any permits. St. Johns County Board of County Commissioners, in the person of Commissioner Sarah Bailey, indicated opposition to the project, together with Bill Basford, President of the Jacksonville City Council. Warren Moody, the vice-chairman of the Jacksonville Waterways Authority spoke in opposition to the project. The Florida Wildlife Federation and the Jacksonville Audubon Society expressed opposition to the project. The officials related the fact of the expenditure of considerable amounts of public tax dollars to improve water quality in the St. Johns River and their concern that those expenditures not be squandered with the advent of some damage to the St. Johns River by allowing the permits in question to be issued. These officials considered the St. Johns River to be a significant resource which they are committed to protecting. The City of Jacksonville, Clay County, Green Cove Springs, the Jacksonville Waterways Authority, the Northeast Florida Regional Planning Council and St. Johns County expressed opposition to the project contemplated by the present permit application, through the adoption of certain resolutions. These broad-based statements of opposition were not spoken to in the course of the hearing by members of any technical staffs to these governmental institutions. Private members of the public, some of whom are affiliated with River Systems Preservation, Inc., expressed concern about water quality violations, harm to fish and other environmental degradations that have been caused by the Homer Smith operation in the past and their belief that these problems will persist if the permits at issue are granted. Those persons who favored the project, in terms of public discussion, primarily centered on the idea that, in the estimation of those witnesses, fairness demanded that Smith be afforded an opportunity to demonstrate that this proposed system of treatment was sound and the quality of the water being discharged from the Homer Smith plant was not as bothersome as had been portrayed by the persons who opposed the grant of environmental permits. Industrial Wastewater Construction Permit Treatment System Description of Homer Smith's Plant and Its Operation. The source of water used for the processing of the scallops at the Homer Smith plant is a well which is located on that property. Homer Smith is allowed to withdraw 300,000 gallons of water per day in accordance with a consumptive use permit that has been issued by the St. Johns River Water Management District. To ensure Smith's compliance with this permit, a metering device is located on the well. Typically, the plant operates an eighteen-hour day, five days a week, using water at a rate of 200 gallons per minute. This would equate to 215,000 gallons per day over an eighteen-hour day. Prior to the imposition of restrictions by the Department of Environmental Regulation through the consent order, this facility had processed as much as 40,000 pounds of scallops each day, for a total of 36,000 gallons each week, at a gross revenue figure of $225,000 per week. Characteristics and Frequency of Effluent Discharge The wastewater generated by the scallop processing that is done at the Homer Smith plant is principally constituted of the well water used to clean the scallops, proteinaceous organic materials, and metals. The metals are introduced into the wastewater stream from the scallop tissue. The wastewater stream also has a certain amount of sand and grit, together with shell fragments. The concentrations of organic materials within the wastewater stream are at high levels. There is also an amount of fecal coliform bacteria and suspended solids. The pollution sources within the wastewater stream include total suspended solids (TSS), biochemical oxygen demand (BOD), nutrients (nitrogen and phosphorus) and the coliform bacteria. In the neighborhood of 30 percent of the BOD in the wastewater is soluble. The balance of the BOD is associated with the suspended solids. With time the organic materials in the wastewater stream will decompose and with the decomposition present certain organic decomposition products, which would include ammonia, amines and sulfides. Heavy metals in the wastewater have been in the scallop tissue and are released with the cleaning of the scallops. These metals include cadmium, copper, zinc, iron, manganese, silver and arsenic. The presence of these metals within the tissues of the scallops are there in view of the fact that the scallops are "filter-feeders" which have taken in these elements or metals that naturally occur in the ocean water. The permit application contemplates an average of five days a week of operation for eighteen hours a day. Notwithstanding the fact that in the past the Homer Smith Seafood operation had processed scallops seven day week, twenty- four hours per day, Smith does not desire to operate more than five and a half days a week in the future. That is perceived to mean five eighteen-hour days and a twelve-hour day on the sixth day. The treatment system contemplated here is for a flow volume of around 200 gallons per minute during normal operation. The system can operate as high as 300 gallons per minute. That latter figure approaches the design capabilities of the treatment system proposed. Wastewater is discharged only when scallops are being processed. There is basically 1:1 ratio between the volume of well water used to process the scallops and the amount of wastewater discharged. Proposed Treatment System and Alternatives As already stated, there is no specific industry standard set forth in the DER rules which would describe technology-based standards for the treatment of calico scallop wastewater. In those instances where the agency is confronted with an industry for which technology-based standards have not been established, DER examines the question of whether that effluent is amenable to biological treatment as contemplated in Rule 17-6.300(1)(n)1., Florida Administrative Code, as an alternative. Biological treatment is a treatment form normally associated with domestic waste and the imposition of this treatment technique is in furtherance of achieving a secondary treatment standard found in Chapter 17-6, Florida Administrative Code, which results in 20 mg/L of BOD and TSS, or 90 percent removal of those constituents, whichever is the greater performance in removal efficiency. In the absence of specific standards related to the calico scallop industry, and in the face of the interpretation of its rules in which DER calls for an examination of the possibility of biological treatment as an alternative to treatment specifically described for a given industry, it was incumbent upon this Applicant to examine the viability of biological treatment of the scallop wastewater product. The Applicant has considered biological treatment as an alternative and rejected that treatment form, in that Smith's consultants believe the wastewater is not amenable to biological treatment. By contrast, Petitioners' consultants believe that biological treatment should be the principal focus in treating the scallop wastewater and contend that biological treatment is a more viable choice when contrasted with the option chosen by the Applicant. If this waste is not amenable to biological treatment, Rule 17-6.300(1)(n)1., Florida Administrative Code, envisions an acceptable or minimum level of secondary treatment shall be determined on a case-by-case basis. In the instance where biological treatment is not a reasonable choice, the Applicant is expected to achieve treatment results which are comparable to those arrived at in treating domestic waste by the use of biological treatment techniques. On this occasion, DER had not established what they believe to be a comparable degree of treatment for calico scallop waste, assuming the unavailability of biological treatment. The present case is a matter of first impression. As a result, the idea of a comparable degree of treatment shall be defined in this hearing process, assuming the inefficacy of biological treatment. In that event, DER must be assured that the proposed treatment plan has an efficiency that rivals the success which biological treatment promotes with domestic waste, taking into account the quality of the effluent prior to treatment, available technology, other permitting criteria and the ambient conditions where the waste stream is being discharged. In arguing in favor of biological treatment, Petitioners pose the possibility of an integrated system in which primary settling tanks or clarifiers would be used together with a biological treatment step, which is referred to as a trickling filter, followed by final settling by the use of tanks or clarifiers in an effort to achieve BOD concentrations in the range of 200 mg/L to 400 mg/L. In this connection, the dissolved air flotation system is seen in the role of alternative to the initial stage of settling of the constituents within the wastewater stream. It is not regarded as the principal means of treatment of the waste. The trickling filter system as a biological treatment medium involves the use of a bacterial culture for the purpose of consuming the oxygen-demanding constituents, BOD. The trickling filter technique, if a viable choice, has the ability to remove 70 to 75 percent of BOD and TSS. Petitioners suggest further treatment of the waste beyond primary and final settling and trickling filter can be afforded by involving activated sludge, which according to their experts would end up with a biological oxygen demand in the 20 mg/L range. Although the constituents of the Smith plant's waste are of a highly organic nature, and, at first blush a candidate for biological treatment by use of the trickling filter, the problem with this form of treatment has to do with the intermittent flow in the Smith operation. This intermittent flow is caused by the fact that the plant does not operate throughout the year. The plant operations are seasonal, depending on calico scallop harvesting which does not occur on a routine basis. Therefore, the problem is presented of trying to keep the biological treatment system "alive" and operating at levels of efficiency which can be expected to maintain the percentage of removal of BOD and TSS that a healthy system can deliver. The bacteria colonies which are vital to the success of the biological treatment system must be fed on a continuous basis to maintain balance in the population of the colony. This would be a difficult undertaking with the Smith operation, given the interruptions in operations which could lead to the decline in the bacterial population and a poorer quality of treatment once the operations were resumed. This finding takes into account the fact that the colony can survive for a week or two by simply recirculating water over the filter. Obviously, in order to maintain necessary efficiencies within this biological treatment, the bacteria must do more than survive. The further suggestion that has been offered that the bacteria could be sustained for longer periods of time by feeding them seafood waste or dog food are not found to achieve the level of efficiency in the operation that would be necessary in posing biological treatment as an alternative. Again, it is more of an intervening measure designed to assure the survival of bacteria pending the continuation of the operations of the plant, as contrasted with a system which is continual and taking into account the uniformity of the waste product more efficient. Another problem with feeding the bacteria when the plant is not operating is that of disposing of the waste produced when this auxiliary feeding is occurring. Just as importantly, biological treatment is questionable given the long retention times necessary for that process and the build-up of toxic levels or concentrations of ammonia. The Applicant had employed an aerated lagoon in attempting to treat the waste and experienced problems with ammonia build up. Although this system did not call for the degree of treatment of the waste prior to the introduction into the lagoon that is contemplated by the present proposal of the Applicant, it does point to the fact of the problems with ammonia in the biological treatment system. Dr. Grantham, a witness whose testimony was presented by the Petitioner, conceded the difficulty of removing ammonia from the trickling filter. Moreover, the biological treatment system is not especially efficient in removing metals and phosphorus from the wastewater. Alternative treatment would be necessary to gain better efficiency in removals of those constituents. The trickling filter is expected to gain 50 percent metals removal, which is inadequate given the concentrations of heavy metals found in the scallop wastewater. Phosphorus could be removed after treatment by the trickling filter by the use of lime or alum. Assuming optimum conditions in the use of biological treatment after primary and final settling, thereby arriving at a BOD level of 200 mg/L, it would then be necessary to make further treatment by the use of activated sludge to see 20 mg/L BOD. The problem with activated sludge is related to the fact that this form of treatment is particularly sensitive to interruptions in flow, which are to be expected in this wastewater treatment setting. On balance, biological treatment does not present a viable choice in treating scallop waste. That leaves for consideration the question of whether the Applicant's proposal would afford a comparable degree of treatment to that expected in the use of biological treatment of domestic waste. The manufacturer of the dissolved air flotation unit or DAF system proposed, known as the Krofta "Supracell," offers another piece of equipment known as the "Sandcell" which in addition to the provision for dissolved air flotation provides sand filtration. The Sandcell might arrive at BOD levels of 400 mg/L. However, the testimony of the witness Lawrence K. Wang, who is intimately familiar with the Krofta products, in responding to questions about the use of the Sandcell system and suggestion that the system would arrive at 400 mg/L BOD responded "could be." This answer does not verify improvement through the contribution of sand filtration. For that reason inclusion of a Sandcell for filtration of BOD is not suggested in this fact finding and the system as proposed must be sufficient in its own right. Having realized the need to provide greater treatment than screening or filtering the waste stream, the Applicant attempted to design a treatment system using flotation technology together with chemical precipitation and coagulation. At first the Applicant examined the possibility of the use of electroflotation (EF). This involved the collection of wastewater in a retention tank and the generation of an electric current to create a series of bubbles to float insoluble flocs. Those flocs are caused by the use of ferric chloride, sodium hydroxide and various polymers which are added to the waste stream. The flocs are then pushed to the top of the chamber by the air bubbles, and this particulate matter is skimmed off by the use of a paddle. Pilot testing was done of the electroflotation technology and showed promising results, so promising that a full-scale electroflotation unit was installed and tested. The full-scale electroflotation showed reasonable removal of BOD, TSS, nutrients, coliform and trace metals. This technique was discarded, however, when bioassay testing of the treated effluent was not successful. In examining the explanation for the failure, the experts of the Applicant were of the opinion that certain chemical reactions were occurring as a result of the passage of the electrical current through the wastewater stream. When this problem with acute toxicity could not be overcome through a series of adjustments to the process, the Applicant decided to test another form of flotation, which is referred to as dissolved air flotation (DAF). This system employs the use of chemicals to create insoluble flocs. Unlike the electroflotation unit, though, it does not utilize electrical currents to create the air bubbles employed in the flotation. The dissolved air flotation thereby avoids problems of toxicity which might be attributed to the passage of electrical current through the water column. The present system as proposed by the Applicant has a number of components. The first component of treatment involves the passage of raw wastewater through a mechanical screening device, which is designed to remove a certain number of particulates by catching those materials on the screen. That material is then removed from the plant and disposed of off site. The balance of the wastewater after this first stage of treatment passes into a sump area and from there into a primary mix/ aeration tank. This water is then chemically treated to facilitate the formation of insoluble flocs. The chemically treated wastewater then enters a premanufactured Krofta Supracell 15 DAF unit which is designed to form bubbles by the use of pressurized air, with those bubbles floating the waste materials within the floc to the surface. Again, this method does not use electrolysis. The floated solid materials are then skimmed from the surface and directed to a holding tank and subsequently pumped to sludge drying beds. Some of the treated wastewater is recycled through the DAF unit after pressurization and in furtherance of forming the necessary bubbles for the DAF unit. The balance of the water is directed to a force main lift station. This water would then be transported through the eight-inch PVC pipe some 13,000 feet into the main channel of the St. Johns River where it is distributed through a five port diffuser. The screening mechanism spoken of had been installed in mid-December 1984 and has been used since that time to filter the wastewater. The screening mechanism is in substitution of settling tanks and shell pits. The shell pits which had been used before presented problems with odors as well as the ammonia build up which has been addressed in a prior paragraph. The removal efficiency of the screening mechanism is 30 percent of particulates associated with pollution parameters, as example BOD, total Kjeldahl nitrogen, total phosphorus and TSS. The frequency of the transport of these screened materials to the off site disposal is four to six times a day and the screen is decontaminated at the end of each day when the operations are closed. The application contemplates the same operating procedures of disposal and maintenance with the advent of any construction permit. The primary mix/aeration tank aerates the wastewater and through that process and the retention time contemplated, equalizes the flow regime and promotes a more balanced concentration of waste materials prior to the introduction of that wastewater for chemical coagulation and flotation. This step in the treatment process enhances the treatment efficiency. Some question was raised by the Petitioners on the size of the primary mix-aeration tank as to whether that tank was sufficient to equalize the flow, and conversely, the impacts of having too much retention time built into that tank, which would promote the build-up of toxic concentrations of ammonia in the wastewater. The retention time within the sump and the primary mix-aeration tank approximates one and one-half hours. The retention time and size of the primary mix-aeration tank are found to be acceptable. This design appropriately addresses concerns about the build-up of decomposition products and toxicity, to include ammonia. The sludge which collects in the primary mix-aeration tank will be pumped back to the sump pit by return flow. The sump pit itself will be pumped out in the fashion of cleaning a septic tank on the basis of once a week. The sump pit also receives the return flow of leachate from the sludge drying bed. Once equalization of flow is achieved in the primary mix-aeration tank, that wastewater is then treated by the use of alum, sodium aluminate and polymers. The purpose of this treatment is to convert soluble and insoluble organic matter such as TSS and BOD, trace elements and phosphorus into insoluble flocs that can be removed by flotation. These combinations of chemicals and dosage rates have been tested in electroflotation and dissolved air flotation bench and pilot scales for use associated with this project and a list of appropriate chemicals and ranges of dosage rates has been determined. It will be necessary for these chemicals and general dosages to be adjusted in the full- scale operation under terms of the construction permit. This facet of the treatment process must be closely monitored. Once the wastewater stream has received the chemical treatment, it is introduced into the Krofta Supracell 15 DAF unit. This unit is 15 feet in diameter, and within this cylinder bubbles are generated by pressurizing some of the chemically treated wastewater and potentially clean tap water. The use of clean tap water promotes dilution of the wastewater stream as well as greater efficiency in the production of the bubbles. Chemically treated wastewater is brought into the cylinder through the back of a revolving arm that moves around a center column of the DAF unit at the speed of the effluent flow. The purpose of this mechanical arrangement is to eliminate horizontal water velocity, to protect the integrity of the flocs that are being formed by the use of the chemicals. Those flocs float to the surface in a few minutes' time, given the normal turbulence and shallow depth of the DAF unit. This limited retention time also avoids ammonia build up. The floating material is then scooped and poured into a stationary center section and is discharged by gravity to the sludge holding tank. Wiper blades which are attached to the revolving arm scrape the bottom and sides of the tank and discharge any settled sludge to a built-in sump in the DAF unit. These materials which are settled in the bottom of the DAF cylinder are transported through the sludge holding tank and eventually placed in the sludge drying beds. The treated wastewater is removed by an extraction pipe associated with the center section of the DAF unit. It is then discharged. The use of clean tap water from the well and the ability to recycle the waste stream can promote greater treatment efficiency in terms of removal of undesirable constituents of the waste stream and the reduction of concentrations of those materials. As a measurement, approximately 8 percent of the wastewater flow will be removed as sludge. This sludge is sufficiently aerated to be reduced in volume by about one-half over a period of ten to thirty minutes in the sludge holding tank. It is then sent to the sludge drying beds. The sludge drying beds are designed to accommodate 30,000 gallons of sludge. They are 60 feet long, 25 feet wide and 4 feet deep. Those drying beds are of greater size than is necessary to accommodate the volume of sludge. The sludge drying beds have a sand and gravel bottom. The water drains from the sludge as leachate and returns to the sump pit in the treatment system at a rate of five to ten gallons a minute. Some concern has been expressed that the "gelatinous" nature of the sludge will make it very difficult to dewater or dry. This opinion is held by experts of the Petitioners, notwithstanding the fact that polymers are used in the treatment process. One expert in particular did not believe that the sludge would adequately dry. Having Considered the evidence, the opinion that the sludge will not dry sufficiently is rejected. Nonetheless, it is incumbent upon the Applicant to monitor drying conditions of the sludge very carefully and, if need be, to add some chemical such as calcium hydroxide to enhance the drying capacity of the sludge material. It is anticipated that the sludge will be removed once a day and this arrangement should be adhered to. With adequate drying, the sludge material can be removed with the use of shovels, rakes and a front-end loader as proposed by the Applicant. With frequent removal and adequate drying, problems with odors can be overcome, and problems with ammonia build up and the generation of unreasonable levels of bacteria can be avoided. Should problems with odors, ammonia and bacteria occur, it would be necessary for the Applicant to purge the drying beds, to include the sand and gravel which had been invested with the sludge materials that had caused the problems. Although Smith has not tested the drying bed leachate as to specific nature, the treatment process can be expected to deal with problems of any build-up of ammonia concentrations, fecal coliform bacteria and other organic decomposition products. This pertains to the ability to remove these offending substances from the site in terms of removal of the residual solids and the ability to treat those parameters within the leachate as the wastewater is cycled through the system. The treated wastewater will be transported to a pumping station by gravity flow and then pumped via the pipeline to the proposed point of discharge in the main channel of the St. Johns River. This pipeline is constituted of fabricated sections of pipe 20 feet in length, connected with bell and spigot joints, rubber gaskets and solvent welding. The treated wastewater is released into the river through a five point diffuser which has three-quarter inch openings angled at ten degrees from the horizontal bottom. The pipeline is anchored with prefilled 80-pound concrete bags attached with polypropelene straps which are placed at 8-foot intervals. These are placed to keep the pipe from floating. The diffuser is supported by four piles driven into the river bottom and surrounded by a series of concrete bags. The purpose of this arrangement is to hold the diffuser in place and to protect it against potential damage from anchors or other possible impact. The Applicant acquiesces in the choice to have the pipeline tested for leaks once a month in the period June through September and every other month during other parts of the year. If leaks are found, the Applicant would be responsible for repairing those leaks. As stated before, it is necessary for the Applicant to receive permission from the State of Florida to be granted an easement before the pipe can be installed. Prior to that permission being granted, the treated wastewater would be placed in Trout Creek, which is adjacent to the processing plant. Predicted End of Pipeline Quality of the Effluent In trying to predict the quality of effluent at the end of the pipeline, bench scale and pilot scale testing was done related to the DAF technology. This testing was done related to screened wastewater that was collected from the plant in April 1985. In this connection two series of DAF bench scale tests were performed. They related to samples collected on April 18 and 19, 1985, which were packed in ice and shipped directly to a research laboratory in Lenox, Massachusetts, where they were treated with chemicals and a laboratory size DAF unit. The concentration of the wastewater parameters were measured and recorded before and after treatment, and the results of those tests are set forth in the Applicant's Exhibit A-4(B)(3), at Table 2-1. The pilot scale testing that was done in this case related to a 4-foot diameter DAF unit which had been installed at the Homer Smith plant. This testing occurred in April 1985. The basis of the testing was samples taken on April 15 and 19, 1985. Again, wastewater parameters were measured before and after treatment and the results are set forth in Applicant's Exhibit A-4(B)(3), at Table 2-1. When the initial testing was done with the DAF, results for total coliform bacteria uniformly fell below a range of 35 organisms/100 ml. Subsequent pilot tests yielded higher bacterial counts which would indicate that there was a build-up of bacteria within the DAF unit. This verifies the need to require that the DAF unit contemplated by the application be routinely cleaned or sanitized to avoid the build-up problem. TSS in the pilot unit effluent was reduced to 40 mg/L and lower. The capacity for metals removal in the pilot scale testing was good pertaining to copper and zinc. The ability to remove cadmium showed a result of 0.013 and 0.015 mg/L. The best performance in the pilot scale testing related to BOD removal showed a value of 510 mg/L. It should be noted that the bench scale testing and pilot scale testing were in the face of significant variations in the amount of BOD presented by the screened wastewater. This identifies the need to pay close attention to the removal efficiency of the system related to the BOD parameter in order to achieve consistent levels of BOD following treatment. The system under review is referred to as full-scale treatment. This treatment can be expected to exceed the levels achieved in the DAF bench and pilot scale testing because: (a) As a general proposition, treatment efficiency improves as the scale of machinery increases from bench to pilot to full-scale; (b) The bench and pilot scale tests were run without the benefit of the primary mix-aeration tank and the benefits derived from that part of the treatment apparatus, that is to say, uniformity of the flow and better dispersion of the constituents of the wastewater stream, prior to chemical treatment; (c) The pilot DAF unit used exclusively recycled wastewater to undergo pressurization for the creation of the air bubbles. In the course of the hearing it was established that approximately 50 gallons per minute of clean tap water could be brought in to the treatment process resulting in the formation of more bubbles and the facilitation of up to 10 percent greater treatment efficiency based upon that change. The other contribution made by the use of clean tap water was the possibility of as much as a 20 percent dilution of the wastewater stream, in terms of concentration of constituents within the wastewater stream; (d) In a full-scale operation, the opportunity is presented to routinely adjust the chemical dosages as well as select among a range of chemicals in order to achieve the greatest treatment efficiency; (e) In employing routine sanitization of the DAF unit by use of a mild chlorine compound, the tendency to accumulate coliform bacteria can be overcome. Removal of this adverse influence improves the water quality. In traveling through the pipeline, the transit time is in the range of two to three hours. At a normal rate of 250 gallons per minute of discharge, the transit time in the pipeline is 2.25 hours. Given the constituents of the wastewater, bacterial populations can be expected and could conceivably consume sufficient amounts of oxygen to affect the dissolved oxygen levels within the wastewater as it exits the pipe at the diffuser ports. In addition, there is some possibility of ammonia build up within the pipeline. To avoid the build up of bacteria at harmful levels, sanitation of the DAF unit must be accomplished. In addition, the pipeline itself should be flushed with clean water at the close of operations each day and treated with small amounts of chlorine to address bacteria which may form within the pipeline. This avoids the increasing concentrations of ammonia and protects against lowered dissolved oxygen concentrations and the possibility of increased levels of toxic substances in the effluent which might be attributable to the proliferation of bacteria and the build-up of ammonia during the transport through the pipeline. Taking into the account the nature of this wastewater and the velocity associated with the transport and the sanitization of the pipeline, sedimentation associated with organic solids or other materials will not present a problem. The pollution parameters associated with the treated effluent at the point of discharge from the pipeline can be expected to meet Class III orders, excepting unionized ammonia, specific conductance, copper, cadmium, pH and zinc. In order to achieve satisfactory compliance with regulatory requirements related to those parameters, the Applicant has requested a two-meter mixing zone. The purpose of that mixing zone would be to afford an opportunity for dispersion and mixing in the ambient water before imposition of water quality standards. The implications of that mixing zone are discussed in a subsequent section to the fact finding within the Recommended Order. In effect use of the mixing zone will promote compliance with standards pertaining to the subject parameters. Petitioners point out the fact that the Applicant has based its assumptions on the results of treatment on the availability of four sets of data which were obtained from DAF effluent--two sets of data coming from the bench tests and two sets of data from the pilot plant. Further, there is an indication of the variation in quality of the effluent from one test to the next and the need to employ different dosage rates of chemicals in the face of those variations. The full-scale system utilizes a number of techniques to gain some uniformity in the quality of the effluent prior to chemical treatment and thereby some uniformity in the amount of chemicals necessary to treat the effluent. This overall system can then be expected to produce treated wastewater that is basically uniform in its constituents. Petitioners point out the limited amount of data in the testing related to BOD. There were, in fact, only two data points: one related to the bench system and one related to the pilot system pertaining to BOD, both of these the product of different chemical dosages for treatment. Again, the system that is at issue in this proceeding can be expected to arrive at a more consistent level of BOD than is depicted in the results pertaining to bench scale and pilot scale testing. In fact, those results were not remarkably disparate in that the bench sale test produced 560 mg/L and the pilot scale test produced 510 mg/L. While the data related to BOD is limited, it still gives sufficient insight as to the probability of successful full-scale treatment and the test data is found to be a reliable indication of success in achieving the goal of 510 mg/L BOD. Contrary to the Petitioners' perceptions, the treatment efficiency is improved with the system that is under review. Petitioners believe that the bench and pilot scale testing not only is unrepresentative of the full-size DAF system, they also believe that the full-size system represents a lesser quality of treatment. In this regard reference is made to features which would adversely affect the treatment efficiencies. The first of those pertains to leachate which drains from beneath the sludge drying beds and is recirculated to the existing sump pit and added to the waste stream. Sludge which sits in the drying bed does decompose and causes biochemical reactions to occur, as Petitioners suggest. Moreover, no specific testing has been done of the leachate to ascertain the ammonia concentrations, pH or other chemical characteristics. Nonetheless, given the intention to clean out the residual matter within the sump pit frequently, and the flexibility to make that cleanup more routinely, and the fact that this amount of leachate is comparatively small in its ratio to wastewater which is being sent through the system for treatment, the leachate is not found to be an unmanageable problem. Nor is the sludge a problem. Likewise, the amounts of heavy metals within the leachate can be accommodated. Concerns expressed by the Petitioners related to the organic materials in the primary mix-aeration tank that is being returned to the sump pit can also be dealt with by the evacuation of the materials in the bottom of the sump pit. This can be achieved more frequently than on a weekly basis if that becomes necessary, and in doing so avoid problems with concentrations of ammonia, bacteria, amines, sulfides and general organic decomposition products. These materials which are returned to the treatment process as wastewater reintroduced into the primary mix-aeration tank can be adequately addressed in the subsequent treatment that occurs by reaeration, the use of the chemicals and DAF flotation. The retention inherent in the sump pit, primary mix-aeration tank and sludge drying bed has a potential to cause problems with ammonia build-up; however, the problems can be satisfactorily addressed, as well as potential problems with other toxic substances in the effluent, by routinely taking the residual material in the sump pit and sludge drying bed out of the treatment system. While the specific chemicals and precise dosage rates to be used with a full-size DAF system remain open, the basic concept of chemical treatment has been identified sufficiently. The precaution that is necessary is to make certain that close monitoring is made of the results of changes in the chemicals and dosage rates. Likewise, special attention should be paid to the implications of adjustments in the pH of the effluent to make certain that compliance is achieved with the Class III water criterion related to changes in pH above background. Adjustments can be made without violating Class III water standards related to pH. In testing that was done pertaining to the electroflotation effluent, a number of other chemicals were observed, to include trimethylamine, dimethyl sulfide, chloroform and other hydrocarbons. There is some indication of the presence of dichleoroethane, ethylbenezene and other aromatics. The possibility exists that these substances may also be products within the DAF effluent. In that event, the critical question would be whether they have any adverse effect in the sense of influences on the ability of the effluent to pass bioassays and the ability of the effluent to comply with standards related to other parameters such as dissolved oxygen, BOD, and TSS. The routine testing which is called for by the draft permit, which is deemed to be appropriate, would create a satisfactory impression of the materials set forth in the paragraph in the sense of the implications of their presence and allow any necessary adjustments in treatment. While the effluent produced in the testing on the part of the Applicant is different, it is representative, and the treated effluent which will be produced in the full-scale system will be of a better quality and present less adverse impacts than shown in the past testing. Petitioners question whether the Applicant has given a conservative portrayal in analyzing the effluent. In particular, it is urged that the Applicant claimed to be vying for use of the bench scale testing as a conservative depiction of the results of treatment. In this connection, the impression given in the hearing was that of ascendancy in treatment efficiency beyond the use of bench scale, pilot scale and ending in full-scale treatment. As pointed out by Petitioners, in making his case the Applicant has used results of bench and pilot scale testing. As example, use was made of the results of testing in the pilot scale in describing the removal effioiencies related to cadmium, whereas in the measurements of nitrogen concentrations the bench scale result was better than that of the pilot testing and was utilized. The real question is whether the overall testing has given some reasonable indication of success in full-scale treatment. To that end, use of results from either the bench scale or pilot scale testing is appropriate, and those results point to success in the full-scale operation. The system that is proposed is designed to address fluctuations in flow and concentrations in the effluent, given the primary mix-aeration tank contribution and the ability to recycle flow within the DAF unit, with the use of clean tap water. This will allow the Applicant to deal with the remarkable differences in BOD that were seen in the test period, ranging from 900 to 3000 mg/L. COD data as well as BOD data is limited but is found to be an ample depiction of potential treatment efficiencies related to that former parameter. In addition to the aforementioned references to changes in chemicals in the treatment process, Petitioners characterize the use of clean tap water in the recycle flow as being "unsubstantiated speculation." While the use of tap water was discussed in a theoretical vein, that discussion is found to be an accurate assessment of the value of the contribution of clean tap water to the treatment system. Impacts on St. Johns River Ambient Water Quality and Conditions The St. Johns River and the area of the proposed discharge is a riverine estuary. It has a freshwater source flowing from the south and a tidal ocean boundary to the north. The confluence of freshwater flow and tidal influences causes the water movement within this area to be oscillatory. That is to say that at different times the water will flow downstream, to the north, and upstream, to the south. There are occasions in which the net flow over a given tidal cycle will be zero; however, the water is always moving. Conductivity and chloride data indicate that the freshwater flow is the dominant flow compared to tidal influences. The extrapolation of available flow data indicates that there is a net downstream flow of fresh water averaging approximately 6,000 CFS. The St. Johns River at the point of discharge is over one and a half miles wide and relatively shallow with maximum depth in the range of 3 to 3.5 meters. Given the fact of the width and depth in this segment of the river, and the imposition of wind conditions and tidal influence, the water is well mixed and flushed. There is no stratification in this portion of the river. The Applicant looked into the question of current bearing and velocity in depths between two to fourteen feet in the water column. Eleven sampling stations were utilized in arriving at information about current bearing. This observation was over an eleven-nautical-mile stretch of the main channel of the St. Johns River. These stations are depicted on Applicant's Exhibit 38. In this portion of the river the current at all measured depth was flowing up and down the main channel. Within these sections there is no indication of a pronounced subsurface water movement toward the east and west banks of the river. Current velocities within the three stations closest to the POD averaged in the range of 0.5 feet per second and velocities in the other stations found within the main channel were within that range of movement. By contrast current velocities within the embayment areas along the east bank of the river were substantially weaker. DER conducted two studies using tracing dyes poured into the St. Johns River at the approximate point of discharge and monitored the course of dispersement of that dye. During this observation the dye was constantly replenished while being carried on the currents. While the dye remained within the area of the main channel, it stayed on the east side of the river as it moved down river on the outgoing tide in the direction of Smith's Point and the Shands Bridge. As the tide was slowing before the change of tide, the dye drifted for approximately two hours in the immediate vicinity of the point of discharge. The DER dye study was a fairly gross measurement of the direction of water movement within the river beyond the point of discharge. It tended to confirm that the water flow was basically up and down river, depending on whether the tide is incoming or outgoing. The studies were not sufficiently refined to speak with any certainty on the possibility that some part of the flow regime would move toward the east or west bank of the river. Nonetheless, in examining the nature of the shallow embayment areas along the banks of the St. Johns River, they are not seen to be subject to the basic flow regime that is occurring in the main channel during tide events. The bathymetry in this area is such that if the main flow regime was having some influence on the embayment areas, the depths within those embayments would be more similar to the depths found in the main channel of the river. Petitioners have employed a number of dye and drogue measurements to try to give a more accurate depiction of the influence of flow within the main channel upon the dispersion of effluent upon discharge and the possibility of those pollutants reaching the embayment areas. While there is no dispute over the fact that Trout Creek is a tributary to the St. Johns River with some tidal influences being shown in that Creek and there is no dispute that water from the St. Johns River flows in and out of Palmo Cove and Trout Creek, there does not appear to be a significant flow of water from the St. John River into the cove and creek from the main channel, in particular from the area of the point of discharge. One of the witnesses of the Petitioners, Sandy Young, did a dye procedure in which a plume was allowed to develop over a distance of approximately 1,000 feet. Although some slight lateral variation was shown in the dye plume, it did not identify a basic flow pattern toward the embayment areas on the east side of the river. The DER dye study was over a distance of some eight thousand feet and also showed some minor lateral variation. Both of these dye studies tend to show a basic flow pattern within the main channel. The dye study run by the Petitioners' witness White gave the same basic depiction as seen in the studies by DER and Young and did not identify a flow pattern out of the main channel toward the embayment areas. In the drogue studies run by Young three Chlorox bottles were filled to 95 percent of volume with water and released at the point of discharge. They were followed for a period of five hours. They moved initially with the outgoing tide toward Jack Wright Island and then when the tide slowed, the drogues slowed. When the tide changed with the incoming tide, the drogues moved toward the center of Palmo Cove. The drogue studies by Young do tend to indicate that some water was exchanged from the main channel at the point of discharge and the embayment areas. It is not a very exact measurement as it only deals with the surface area of the water column, given the wind and wave conditions existing on that occasion. It is in no way representative of the flow direction of the rest of the water column. Therefore, although it may tend to identify that some of the pollutants leaving the point of discharge may find their way to Palmo Cove, it does not establish that quantity of that pollution dispersion and the significance of that dispersion. Based upon this evidence it cannot be seen to be so revealing that the assumptions made by the applicant in trying to identify the dispersion characteristics of the effluent at point of discharge are negated based upon the results of the drogue study. The drogue study which Young did and the observation of the movement from Smith's Point to Little Florence Cove are no more compelling than the dye studies done at the point of discharge. When the Petitioners suggest that there is some influence by centrifugal force pushing the water to the outside of the curve toward the eastern bank, they are correct. However, the contention by the Petitioners that the incoming and outgoing tides sweep to the eastern shoreline of the St. Johns River moving toward Pacetti Point, Palmo Cove, Florence Cove and Smith Point is not accepted. Again, the general flow regime is up and down the main channel of the river and not primarily to the eastern bank. Finally, the fact that the Tetratech data produced for the benefit of the Applicant showing the flow pattern within the overall water column, which indicated that the general direction is the same at the top or bottom of the water column, did not tend to identify the fact that pollutants throughout the water column will be dispersed into the embayment areas from the point of discharge. The data collected in the main channel seem to establish that the water was flowing up and down the channel at depths below the surface. The question becomes whether the amount of pollutants that are being brought into the embayment areas is in such concentrations that they tend to cause problems along the shoreline, especially as it pertains to dissolved oxygen levels. From the facts presented, this outcome is not expected. Levels of dissolved oxygen in the St. Johns River can vary in the natural condition as much as 2 to 3 mg daily. These variations are influenced by algal activity and are not uncommon in Florida waters. Dissolved oxygen is essential to aquatic life. Optimum levels of dissolved oxygen for the fish population of the river are in the neighborhood of 6 to 8 mg/L. DER has established a minimum DO standard of 5 mg/L for Class III waters such as Trout Creek, Palmo Cove and the St. Johns River. This standard is designed to achieve uniform compliance throughout water column at whatever time the measurement may be made. DER, by the employment of this rule, is attempting to deal with those instances in which, in view of the dissolved oxygen level, aquatic organisms are placed under greater stress. The lowest DO concentration expected is normally seen in the summer in July, August and September. DO concentrations in the water column are expected to be highest at the surface area and lowest near the bottom. Measurements near the bottom are significant in this instance because the discharge will occur approximately one foot off the bottom of the river. The Applicant took DO measurements of the area in question during the spring of 1984 over a period of three days. These measurements were taken at a time when a better quality of dissolved oxygen might be expected as contrasted with circumstances in the summer. With the amount of wind involved impressive levels of reaeration were also occurring. These measurements showed that in all stations DO levels were at least 5.0 mg/L at all depths. A study by Applicant's consultant Environmental Science Engineering related to a diurnal event for dissolved oxygen was taken approximately one kilometer downstream from the point of discharge in August 1985 and did not reveal any measurements below 5.0 mg/L. The river was choppy on that day and this would improve the quality of dissolved oxygen. Historical data by DER related to water quality at Picolata, which is south of the POD in the St. Johns River, reveals average DO levels of approximately 6 mg/L. Historical water quality data collected by the Florida Game and Freshwater Fish Commission near Green Cove Springs, which is several kilometers north of the point of discharge, indicated average DO levels in compliance with water quality standards. Diurnal data from near Green Cove Springs did not show any history of DO values below the state standards. There is other historical data, however, which indicates that DO concentrations in the general vicinity of the point of discharge do go below 5.0 mg/L. Game and Freshwater Fish Commission data indicate that the readings below 5.0 mg/L could occur as much as 10 percent of the time. This relates to the study done at Green Cove Springs. There does not appear to be any particular pattern to these events of low DO violations other than the expectation of their occurring in the summer months, occurring more frequently in the lower depths of the water column and in areas which are shallow with limited flow. The summer circumstance is one in which there is a possibility of very heavy rainfall followed by hot weather with overcast skies and no wind, and the DO values go down in that set of conditions. The DO values are, in addition to being lower near the bottom of the water column, likely to be lowest in the evening or early morning hours and persist in length of time from eight to ten hours. Some of the Florida Game and Freshwater Fish Commission data from Green Cove Springs depicted some DO concentrations as low as 1.8 mg/L at the bottom and 2.1 mg/L at the surface. The low readings that were taken at Green Cove Springs occurred in September 1979 after Hurricane David had created unusual conditions in the upper St. Johns River as to effects on DO. The same report indicated DO concentrations at eleven stations in the lower St. Johns River in July and September 1982 were in the range to 4.0 to 4.5 mg/L respectively. This particular data is not particularly valuable in view of the location of those stations. There are occasions when the DO concentration at the point of discharge could go below 5 mg/L and could be as low as 2 mg/L on the bottom, but this is not a routine occurrence and would not persist. The Petitioners' consultant Young had taken certain dissolved oxygen readings at the point of discharge in April 1985 and found compliance with the 5 mg/L standard. At other times he and the consultant white measured substandard dissolved oxygen concentrations at the point of discharge. On July 20, 1985, white collected water samples at the surface and at two feet above the bottom and determined that the readings were 4 mg at the surface and 3 mg near the bottom. On August 10, 1985, Young measured DO concentrations of 4 mg/L near the bottom. On August 30, 1985, Young measured DO values of 4 mg/L at the point of discharge. Young had also measured DO concentrations at Green Cove Springs on August 10, 1985, and discovered readings as low as .5 mg/L and ranging up to 3.8 mg/L. A downstream measurement away from the point of discharge in the main channel made on August 10, 1985, by Young showed a dissolved oxygen reading of 4 mg/L. In these August measurements Young had discovered a number of readings that were in compliance with the 5 mg/L requirement. Again on September 5, 1985, Young made a measurement of dissolved oxygen near the bottom of the water column at the point of discharge which was 5.3 mg/L. Young's measurements of dissolved oxygen at the surface and in the intermediate depth, typically were above 5 mg/L. Bottom readings taken by Young in the main channel of the river and to some extent in the embayment areas were extracted from the soft detrital materials, the place of intersection of the river bottom and the water column. DO levels in these anoxic materials would tend to give lower dissolved oxygen readings and, to the extent that this anoxic material remains in the test probe while taking measurements toward the surface, would have an influence on the readings, making them appear lower than would be the case if the anoxic sediments were not present in the test device. These effects were not so dramatic as to cause the rejection of the data collected by this witness. Some explanation for lower DO readings at the point of discharge can be attributable to the fact that the anoxic material associated with high benthic oxygen demand on the bottom reduces the dissolved oxygen in the water column. Although Rangia clams were present at the point of discharge and they are capable of living in an environment of low salinity and low DO, they are likewise able to live in higher ranges of DO and their presence cannot be regarded as meaning that the dissolved oxygen levels are consistently below 5 mg/L. Petitioners' consultant White opined that there would be a very frequent violation of DO standards at the point of discharge, approaching 25 percent of the time. Considering the facts on the subject of dissolved oxygen in that area, this opinion is rejected, as is the opinion that DO concentrations will go below DER standards most of the time in July, August, and September. Young believes that a more involved study of worst case conditions would reveal DO violations throughout the column in the center of the river. The data that was presented was ample to demonstrate that violations would not be that widespread. Nor is the opinion of the consultant Parks on the subject of DO violations, to the effect that they will occur on many occasions accepted. In the Palmo Cove area it is not unusual to see some DO readings below the 5 mg/L standards. The E.S.E. group found substandard DO conditions in Palmo Cove at sampling Station 1 in September and October 1984 and some instances in April and May 1985. DO concentrations were found in the range of .4 and .6 mg/L in August 15 and 30, 1984, respectively, with DO concentrations of 1.8 and 2.1 mg/L reported on October 4 and October 29, 1984, respectively. DO violations in four out of eight checking periods between April 25 and May 24, 1985, were shown in the Palmo Cove area. Measurements taken by the consultant white showed 3 mg/L at the surface and 2 mg/L at the bottom on July 28, 1985. The consultant Young also made a measurement of 3.2 mg/L of dissolved oxygen on August 10, 1985, in a mid-depth reading in the Palmo Cove area. On September 5, 1985, he found a DO reading of 4.0 mg/L. At those places along the eastern shoreline of the St. Johns River and the relative vicinity of Florence Cove, Jack Wright Island, Little Florence Cove and Colee Cove, low dissolved oxygen readings were found, that is below 5 mg/L. These coves can be expected to have substandard readings frequently during the summer period, based upon measurements taken by the consultant Young. In the conduct of the drogue study related to the Chlorox bottle, the consultant Young in tracking the path of those bottles, found a couple of locations in the path of the drogue which were in the range 2.8 to 4.2 mg/L and 2.0 to 4.6 mg/L. The influences of the discharge will not reduce DO in the embayments. The ambient conditions for BOD in the area where the discharge is contemplated is relatively low and there is no thermal or saline stratification even in the summer months. Nutrient concentrations in this part of the St. Johns River are as indicated within the Applicants Exhibit A-4(B)(3) and at present are at such levels as to promote a healthy fish community. There is algae production that can be sufficient in some areas within this section to cause algae blooms. Algae blooms are not found to be a routine occurrence. Algae blooms reflect higher levels of nitrogen and phosphorus. The consultants Young and White have seen algae blooms in the St. Johns River away from the general area of concern, both upstream and downstream. Should those algae blooms occur, they would promote significant rises and falls in DO concentrations. In Palmo Cove and the St. Johns River, supersaturated DO concentrations have been detected and they are indications of high rates of primary algal productivity. The circumstance of supersaturated conditions, related to dissolved oxygen, can be the by-product of an algal bloom. The concentrations of nitrogen range from an average of 1.42 to a maximum of 2.54 mg/L. Nitrogen concentrations of 1.4 mg to 1.5 mg/L are optimally advantageous for fish production. Significant increases above those levels would cause the decline of the fish population. Total phosphorus concentrations in the ambient waters are high. Concentrations in excess of 0.1 mg/L of total phosphorus are regarded as a indication of eutrophication and the average concentration here is measured as 0.3 mg/L with a maximum ambient concentration found at 0.52 milligrams per liter. There is significant algal growth in the inshore areas and an indication of some eutrophication in the grass beds. The dominant species of algae found in that vicinity are blue-green, which are seen as being nuisance species. The grass beds along the shoreline are basically healthy. On the other hand, some of the public witnesses identified the fact that grass beds and other vegetation have died with the advent of discharge from the Applicant's plant into Trout Creek. This was under a system in which little or no treatment was afforded the effluent. One other public witness indicated that his dock in the Florence Cove area had been covered with a slimy material and algae during the past two years. Significant grass beds are found along Jack Wright Island and in other areas along the eastern shoreline of the river. These grass beds are important as fish habitat to include nursery areas, areas for various juvenile species of fish and other organisms. Some of these grass beds are showing signs of environmental stress, and nutrient loading can contribute to that stress. Some of the grass beds are covered with higher amounts of algae, duckweed and periphyton than are desirable. The duckweed had floated into these areas from other locations and can be expected to move away. The presence of algae is an indication of nutrient loading. The presence of duckweed is not a product of nutrient loading in the sense of the production of the duckweed at the site where they were found along the shoreline. The area in question between Pacetti Point and Shands Bridge serves as a nursery in a sense of providing habitat for juvenile species of fish and other organisms. The grass beds along the shoreline provide habitat for feeding and breeding related to juvenile organisms, to include such species as bass and shrimp. Juvenile catfish are found within the deeper portions of the river as well as croaker and other marine species. There is a high number of juvenile blue crabs in this area of the river and this is a commercial resource. Shrimp are taken by recreational fisherman in the area of the North Shore Pacetti Point. Clam beds are also present near the point of discharge. Juvenile and adult manatee have been seen in the St. Johns River and in the area near Jack Wright Island. Manatee have also been observed in Trout Creek at a time before the operation of the Applicant's plant and at times following the cessation of operations in June 1985. During the course of the operation of the Applicant's plant, when raw effluent was discharged into Trout Creek, fish kills were observed. Those events had not been seen prior to the operation of the plant. Indications are that fish were killed in the creek due to the use by the Applicant of fly bait, which made its way into the water. Dispersion Modeling of Water Quality Impact In order to gain some impression of the influences caused by the dispersion of the pollutants within the effluent, the Applicant through its expert employed several modeling techniques. DER was made aware of this modeling as it developed. A far-field model was used to calculate what the long-term or steady state impacts of the treated effluent would be on the ambient water quality. In trying to identify the influence of the discharge, measurement of metals were taken based upon an assessment of long term increases. BOD, which breaks down and consumes oxygen over time, was examined in the sense of the long term effects as to DO deficits. In essence these projections were superimposed over the ambient condition to gain an impression of the adjusted ambient values, taking into account the influence of the discharge. The Applicant also ran a plume model which was designed to calculate spreading and dispersion of the treated effluent within the zone of initial dilution or mixing zone at the point of discharge. This model responds to the discharge configuration. Through the use of computer calculations, it was established that a five-point diffuser with port openings of 0.75 inches in diameter angled upward at ten degrees would result in an effluent dilution ratio of 28.5:1 within two meters of the point of discharge. The calculated impacts of the plume model were superimposed upon the adjusted ambient water quality conditions set forth in the far-field model in order to determine net impact upon the receiving waters within the mixing zone. A third model was used, referred to as the lateral diffusivity model. This model is designed to calculate the six-hour or short term water quality impacts of the treated effluent when it moves from the zone of initial dilution during flood and ebb tide conditions. By estimating dispersion rate, this model predicts what dilution would occur in the path of the effluent plume. These impacts were then superimposed upon the adjusted ambient water quality conditions to determine the total impact in the path of the plume. The modeling work by the Applicant's consultant is a reasonable depiction of the predicted impacts of the pollution on the ambient conditions. The calculations used in the far-field model assumed a freshwater flow of 2,000 CFS. This assumption in the far-field model satisfactorily addresses worst case flow conditions related to seven-day, 10-year low flow. The temperature utilized in depicting ambient water was 30 degrees centigrade when employed in the far-field and lateral diffusivity models. This corresponds to warm weather conditions, which are more profound in describing effects on water quality. The far-field and lateral diffusivity models assumed that the treated effluent discharged from the pipeline would have a BOD concentration of 665 mg/L. This is contrasted with the maximum concentration allowed by the draft permit, which is 510 mg/L, which is the expected amount of BOD. This tends to depict the impacts of the discharge more conservatively. The model assumes the BOD loading of 2,720 kg per week, equating to an average discharge concentration of 665 mg/L if the plant operates five days a week on an eighteen-hour day. The reaeration rate and NBOD and CBOD decay rates used in the far field and lateral diffusivity models are acceptable. Likewise, the longitudinal dispersion coefficient that was used in the far-field model is acceptable. The standard modeling methodology in this process calls for an assumption of a 1.33 growth rate of the plume in the lateral diffusivity model. The Applicant's consultant decided to use a lower constant diffusivity growth rate. As a consequence, less lateral spreading is depicted. With less lateral spreading, less dilution is shown, and the impacts predicted by the model are exaggerated. One of the parameters of the plume model has to do with river flow which causes some turbulence and also brings about dilution. In this instance the plume model calculations assume stagnant conditions which is a more conservative assessment. As the Petitioners have suggested, the modeling to explain the impacts of dispersion of the pollutants is not designed to give precise calculations of the DO deficit at each point in the river along the eastern shoreline. It is indeed an estimate. The estimate on this occasion is reasonable. Although DER performs mathematical analysis of dispersion of proposed discharge in some cases, it did not do so on this occasion. Nonetheless DER was satisfied with the present choice for modeling the dispersion characteristics of the discharge. Although the models utilized were not subject to exact calibration by measurement of the dispersion at the site, the information gained by the Applicant prior to the imposition of the modeling techniques was sufficient to develop the models and to give a theoretical verification of the expected impacts from the discharge. The Applicant's belief that the maximum DO deficit caused by the discharge will not exceed 0.1 mg/L is accepted. The dissolved oxygen level in the effluent at the point of discharge will be above 5 mg/L. The Applicant's choice of reaeration rates, CBOD decay rates, NBOD decay rates, discharge rate from the pipeline, hours of operation, average reversing current speed, net non- tidal flow, non-tidal velocity, time lag before NBOD decay, maximum tidal velocity, and other variables and assumptions within the models were acceptable choices. Although the possibility exists of an occasional 5 1/2 day operation in which 10 additional hours of operation are added, this would not be so significant as to set aside the predictions as to the pollutant dispersion. The Applicant's consultant who modeled the dispersion rates did not conduct dye studies to verify or calibrate the actual dispersion in the river. One of the dye studies indicated a lateral spreading rate which was less than that predicted by the model. Notwithstanding this revelation, the overall techniques used by the Applicant in predicting lateral spreading rate are sound and do not present a risk of a greater DO deficit than was predicted based upon incorrect assumptions as to lateral spreading rates. The Applicant's consultant's use of 2,000 CFS as the net non-tidal low flow was a more convincing estimate than the field data collected by the United States Geological Service, given the paucity of information about the flow conditions within the St. Johns River. The Applicant's choices in describing maximum tidal velocities and average velocity are accepted. The critique of the modeling efforts done by the Applicant that was made by Petitioners' consultant, Dr. Parks, in which he concludes that the DO deficit is considerably greater than 0.1 mg/L is not accepted. Comparison of Predicted Impacts of Discharge with Statutory and Regulatory Criteria Inside the Mixing Zone Applicant's assumptions about the increase in nutrient concentrations in the St. Johns caused by the discharge are accepted. This is based on the assumption of a nitrogen value of 52 mg/L which was achieved in bench scale testing of the effluent and which can be achieved in the full scale operation. As the effluent is discharged from the diffuser within the mixing zone, there will be some turbidity problems in that the bottom near the point of discharge. The soft silt there is easily resuspended. When the discharge is concluded, the material will settle back to the bottom. There will be further resuspension when the operation commences again and there is a discharge. The transport of these suspended materials is limited in that the water velocity associated with the discharge is quickly dissipated. This phenomenon will not cause adverse environmental impacts. The mixing zone does not include an area approved by the State of Florida, Department of Natural Resources for shellfish harvesting; it does not exceed the presumptive maximum size set forth in Rule 17-4.244, Florida Administrative Code. Nor does it include an existing drinking water supply intake or any other existing supply intake that would be significantly impaired by the proposed mixing zone. The water in this area is of sufficient depth that it will not support grass beds that are associated with a principal nursery area, such as pond weed, midgeon grass, manatee grass, turtle grass or eel grass which are used to support nursery activities. These grasses are normally found inshore. Although juvenile fish are found throughout this reach of the St. Johns River, and for that matter in the entire lower eighty miles of the St. Johns River, the mixing zone is not of such dimensions that it will preempt the health of juvenile fish. Most of the freshwater fish in this system use the littoral areas for reproduction. Marine and estuarine species do not reproduce in the St. Johns River. There is some reproduction that is occurring with some species, such as catfish. Given the size of the mixing zone, no significant adverse effects will occur with the established community of organisms in this portion of the river. The mixing zone will not otherwise impair designated uses of the St. Johns River. The treated effluent will not create a nuisance condition or violate any other DER standards that apply within the mixing zone. With the advent of the full scale facility, maximum, average and chronic toxicity criteria can be reasonably expected to be met at the point of discharge, within the mixing zone and at the boundary of the mixing zone. As described before, the effects of sediment transport upon discharge are localized. The proposal for a mixing zone takes into account Rule 17-4.244, Florida Administrative Code, in the sense of addressing present and future sources of pollutants and the combined effects with other pollutants or substances which may be present in the ambient waters. One of the concerns which DER has about wastewater is the effect which that pollutant has on organisms within the environment. To gain an impression of that influence, testing is required to establish whether the wastewater is acutely toxic. The testing is known as bioassay assessment. While this assessment is normally done after the grant of a construction permit, when confronted with uncertainty about the quality of the effluent, some testing is beneficial prior to the grant of a construction permit. This is especially true given DER's experiences in dealing with raw effluent of several of the scallop processors, to include Homer Smith, which showed that the raw effluent was acutely toxic. This acute toxicity testing is done by placing test organisms into aquaria containing the effluent and measuring survival of those species over time. Results are described in terms of a measurement of the concentration of the effluent at which 50 percent of the organisms are killed during a prescribed test period. In static testing the organisms are simply exposed to the effluent for the requisite period of time. By contrast, a static renewal test calls for the effluent to be replaced with another sample of the effluent at various intervals within the test period. Finally, a flow through bioassay test calls for a continuous stream of fresh effluent to be introduced in prescribed concentrations over the duration of the test. A bioassay assessment in the static condition was performed related to DAF pilot scale effluent that was collected on April 19, 1985. In this instance Daphnia magna were used as test organisms and demonstrated a survival rate of greater than 50 percent in a 100 percent concentration of effluent over a period of 96 hours in the setting of static and static renewal tests. That survival rate was also shown in lesser concentrations of effluent as well. The April 19, 1985, sample was also used in testing the response of Pimephales promelas. These test organisms did not survive either in the static or static renewal tests. While an hypothesis has been made that acute toxicity was experienced in this test organism attributable to build-ups of ammonia, which is greater with this type of organism than with the Daphnia, due to larger biomass which allows for a greater number of ammonia generating bacteria to be presented in the test aquaria and the fact that the Pimethales excrete more ammonia, these differences do not definitely explain why the Daphnia survived and the Pimephales did not. In the series of static renewal bioassays performed on the wastewater that was collected at the plant on April 29, 1985, and shipped to Lenox, Massachusetts, for bench scale treatment, the test organisms of both types failed to survive for 96 hours. It was discovered that during the course of the test period, levels of ammonia rose rapidly. Trace metals in the treated effluent are principally in the form of stable species, as opposed to free ions. These constituents standing alone are not likely to have caused the mortality in the test organisms. The effect of decomposition of the organic constituents in the waste stream is the most likely explanation of why the bioassays of pilot and bench scale treated effluent did not lead to a satisfactory result. Unionized ammonia, a by-product of organic decomposition, is found to be a principle player in the explanation of why the treated effluent was acutely toxic to the test organisms. The exact cause of toxicity has not been precisely identified. Given the complex nature of the effluent, other potentially toxic substances such as sulfides, amines, and other organic compounds could have contributed to the demise of the test organisms. Moreover, toxicity can increase with combinations of chemicals acting in a synergistic fashion, making their combined effects more devastating than the effect of any single substance. Having in mind the fact that ammonia is a major problem in the survival of test organisms subjected to a bioassay, the question becomes one of what may be done to remove ammonia. The production of ammonia in wastewater would depend upon the presence of bacteria. The proposed DAF system removes substantial numbers of bacteria, thereby limiting the possibility of ammonia build-up, if bacteria are not allowed to recolonize in some part of the system prior to discharge. As discussed before, reduction of bacterial activity can be achieved within the proposed treatment system. This is unlike the experience with the bench scale and pilot scale testing that was done on the effluent in which a substantial amount of time transpired before subjecting the test organisms to the effluent and in which a substantial amount of time transpired while the test organisms were being subjected to static and static renewal procedures with the same effluent. The time intervals contributed to the build- up of toxic levels of ammonia in the effluent. The system which is proposed in this instance can avoid the problem of time as it relates to the build-up of levels of ammonia. To further reduce the influence of retention of the waste product, flow through bioassay testing would be the most appropriate measurement of the survivability of the test organism in that it would be responding to real case conditions pertaining to the quality of effluent and its potential toxicity. Under these circumstances, it is reasonable to believe that in a flow through bioassay test of the full scale treatment system, the test organisms could survive. This determination is reached given the reduction in retention time compared to the bench and pilot scale testing, which reduces ammonia, with further ability to reduce ammonia by frequent removal of residual materials from the sludge drying bed and sump pit and taking into account basic improvements in treatment efficiency associated with the full scale system. In addition, the pH of the effluent can be regulated to avoid toxicity in the ammonia which is associated with inappropriate balance within the pH. While a 96-hour LC-50 cannot be calculated with the results of bench scale and pilot scale testing, a reasonable possibility exists for the establishment of that measurement with the advent of a flow through bioassay. There is sufficient similarity between the effluent in the pilot and bench scale testing and the expected effluent in the full-size system for the bioassay testing that was done in those limited systems to give a meaningful indication of the probability that the Applicant can pass a flow through bioassay. Applicant can be reasonably expected to produce an effluent in the mixing zone which will not exceed the 96 hour LC-50 for acute toxicity. As with the circumstance of ammonia, pH can be controlled within the system to address the implications of changes in pH as it pertains to other pollutants in the wastewater. Ammonia production can be influenced by the amount of alkalinity in the effluent and the receiving waters. Alkalinity has not been measured thus far. Alkalinity could be established for the effluent and receiving waters and dealt with if it was suspected as being an explanation of problems with the build up of ammonia which might exceed DER standards. The discharge from the Applicant's plant will not cause long-term problems with low DO, high nutrients, algal imbalances, and chronic toxicity. Outside the Mixing Zone Those constituents within the waste stream, to include those for which a mixing zone was sought, will comply with applicable water quality standards at the boundary of the mixing zone. The dissolved oxygen deficit at its maximum can be expected to be in the neighborhood of 0.1 mg/L and will be exerted somewhere in the range between 1 and 2.5 km downstream of the point of discharge across the width of the plume in worst case conditions. This deficit is not of a dimension which is easily detectable. The implications of that deficit are difficult to perceive in terms of tangible environmental consequences. While a deficit in the range of 0.1 mg/L has some relevance in the DER permitting decision, that deficit as it is dispersed is not expected to cause or contribute to violations of water quality standards in the main channel of the river or in the inshore and embayment areas. While it is true that there are periodic fluctuations of dissolved oxygen below 5 mg/L, DER, as a matter of present policy and professional judgment believes that in this system which evidences characteristics of a clean well-flushed, unstratified water body occasional readings of low DO are not regarded as an indication of violation of water quality standards. This speaks to the main channel area of the river where the only quantifiable influence is expected. The facts presented in this case support the soundness of this policy choice. Petitioners presented the testimony of former officials within DER, namely Parks and Young, who stated that dissolved oxygen standards of 5 mg/L are applied at all times and at all places. They felt that the DER policy was to the effect that permits would not be granted for discharge in any circumstance where the DO concentrations are substandard in the ambient waters, regardless of the amount of decrease or deficit that would be promoted. Parks spoke of the availability of site specific alternative criteria, variances, exceptions or exemptions from the terms of the water quality rule. Having considered these remarks, the present DER policy of allowing the permit to be granted in the instance where occasional violations of ambient water quality standards related to 5 mg/L occur, in the face of the small deficit which is involved in this case, is the better choice. Further, it is a choice that is not so inconsistent with prior practices as to be arbitrary in nature. Finally, DER's position that it would be unadvisable to require a request for site specific alternative criteria, variances, exceptions or exemptions in circumstances such as this case is accepted, when taking into account the problems which would be presented to the agency in administering the permit program, should each Applicant who is confronted with occasional violations below standards for dissolved oxygen have to seek extraordinary relief. While the facts do identify that some pollutants can reach the embayment areas on the eastern shore, the facts do not depict a circumstance in which the amount and quality of that effluent will be such that it will cause or contribute to dissolved oxygen violations in those areas. The water quality in the embayment areas is lower than that in the main area of the river due to inadequate flushing. The areas inshore do not interact with the main channel in a way that would take advantage of the faster moving currents found in the main channel as this interaction might promote a better quality of water. In view of the situation in the embayment areas, the Applicant, on advice of his consultants, moved the proposed location of the discharge into the main channel away from the areas which were under greater stress in terms of dissolved oxygen values and in doing so avoided damage to these areas. The current velocities in the area east of the main channel are weak. There is a substantial distance from the point of discharge to the inshore areas. As the effluent moves toward the inshore or nearshore areas it will become so diluted it will not have an adverse influence on dissolved oxygen. Not only the distances involved, but also the fact that water flowing near the surface is well aerated contributes to the dilution of the effluent as it approaches the shore. Although it has been shown that some stress in the grasses along the eastern shoreline has occurred and the existence of blue-green algae has been shown, together with indications of undesirable algal production, the nutrients which are part of the effluent at the point of discharge are not expected to cause an imbalance in the natural populations of flora and fauna or create nuisance conditions or violations of transparency standards. The nitrogen increase could cause an increase in algal production in the order of one percent, which is inconsequential. The treated effluent will not adversely effect biological integrity of the St. Johns River. The benthic microinvertebrate community in this part of the river is fairly low density due to the fluctuations in salinity levels and predation by fish and blue crabs and given the nature of this substrate which is unstable with low levels of dissolved oxygen. The organisms that are predominant have a tolerance to siltation and fluctuations in dissolved oxygen. The treated effluent will not adversely effect the microinvertebrate community. Petitioners point out the fact that when DO concentrations decrease below optimum levels, fish and other organisms suffer. The fish reduce their movement, feeding and reproduction and they are less disease resistant. They are placed in a position of having to leave the area or risk death if the impacts of the decrease in dissolved oxygen are severe. The influence of the effluent at the point of discharge in this project is not expected to have significant impact on fish and other organisms within these topics of concern expressed in the paragraph. Even though the dissolved oxygen deficit extends in amounts below 0.1 mg/L as far as 2.1 km upstream and 4.5 km downstream and within a wide breadth of the center portion of the river, those deficits will not be significant to the water quality. The BOD associated with the discharge, allowing for mixing will not depress dissolved oxygen levels below DER standards of 5 mg/L. The combination of BOD and nutrient discharge will not cause an imbalance of algal production in the river, nor will it contribute to the dominance of nuisance algal species. The BOD nutrient loading associated with the discharge into the St. Johns will not promote significant ecological impacts on the St. Johns River, to include the possibility of more frequent and severe algae blooms, increase in benthic oxygen demand, risk of increase eutrophication, destruction of grass beds or decline in the fishery. With the advent of discharge in the St. Johns DO fluctuations in the river will not be greater nor will there be an occurrence of a swing from substandard dissolved oxygen levels to supersaturated dissolved oxygen. While the discharge from the Applicant's plant contains pollutants such as cadmium, zinc, arsenic, copper and organic decomposition products, the treatment provided the wastewater is expected to overcome any acute toxicity associated with these materials individually or in combination. Chronic toxicity is not expected related to these materials. The effects of these materials are not expected to cause physiological and behavioral responses which are abnormal in organisms such as reduced locomotion and reproduction or increase susceptibility to diseases to include ulceration and increased mortality. Treatment contemplated and provision of a mixing zone will allow compliance with the standards related to cadmium. Reference has been made to a development known as St. Johns Harbor which is in the vicinity of the proposed discharge and can be expected to promote some pollution in Palmo Cove and the St. Johns River. Although St. Johns Harbor development is proceeding through stages of permit review, it does not appear that it has reached a place in which exact information about its implications as a pollution source can be set out. In discussing the St. Johns Harbor Development, Petitioners emphasized that this eventuality and other matters which deal with cumulative impact have not been satisfactorily addressed. There is no indication than any other substantial development or activity other that St. Johns Harbor is contemplated in this area associated with the permit review at hand. St. Johns Harbor eventually hopes to develop 3000 residential units. It has received the approval of the Northeast Florida Regional Planning Council for the initial phase of development. It has been reviewed by the Florida Fresh Water Game and Fish Commission. The developers are proceeding with the project to include the sale of lots. Nonetheless, that development has not reached the phase where its implications would form the basis of a denial of this project based upon the theory of cumulative impact. While Petitioners contend that stormwater runoff from the St. Johns Harbor project will be a problem, assuming an inadequacy in the design which that developer employs to deal with that matter, this eventuality is not expected based on a review on the facts presented. Reference is made to the Ulcer Disease Syndrome which fish in the St. Johns have suffered from. The principal area in which this event has occurred is north of the area expected to be influenced by this discharge. Nonetheless, diseased fish have been found in Palmo Cove. This Ulcer Disease Syndrome is caused by heavy metals and hydrocarbons, and these materials act in league. The advent of additional heavy metals and other pollutants, such as those being discharged from the Applicant's plant could cause further deterioration in the condition of fish suffering from Ulcer Disease Syndrome. Having considered the facts, this outcome is not expected. Ambient levels of 18 other pertinent pollution constituents in the vicinity of the point of discharge were ascertained by the Applicant's consultants on the basis of field observations and historical United States Geological Survey and Florida Game and Fresh Water Fish Commission data. This formed a basis of an assessment of average and worst case values. This information indicates compliance with those parameters for purposes of water quality standards at the point of discharge. Implementation of Construction Permit Permit Conditions Applicant's Exhibit A-10 is a copy of the DER intent to issue the construction permit. It sets forth seventeen specific permit conditions, and these conditions should be imposed in the permit. The following are additional conditions that should be set forth in the construction permit: The operation and maintenance manual required by original Condition 10 shall provide that the DAF treatment system be cleaned regularly with a mild chlorine solution and that the wastewater from this maintenance be placed in a vehicle and carried off the premises for disposal at an appropriate location. This wastewater from the cleanup shall not be discharged from the plant into state waters. The operation and maintenance manual shall provide that a dosage level of chlorine to clean the pipeline that will result in comp- liance with all water quality standards at the end of the pipeline be added to a fraction of fresh water used to flush the system at the cessation of discharges each day. DER must approve this dosage amount before it becomes part of the operation and maintenance manual. The operation and maintenance manual shall set forth a regular schedule for pumping the accumulated sludge or solid materials from the sump pit. The operation and maintenance manual shall provide that as much as 50 gallons per minute of fresh tapwater may be added to recycled wastewater for pressurization. Any discharge created with this addition may not exceed 250 gallons per minute. Any discharge created above 200 gallons per minute shall be consti- tuted only of tap water. Two machine scallop processing operations at the plant will be limited to an average of 18 hours per day and no more than 90 hours in a week. Monitoring in Trout Creek shall continue as specified in paragraph 17(E) of the Consent Order as long as discharges into Trout Creek continue. On each occasion when the DAF treatment system is in operation, the Applicant shall have a fully trained operator on site. The terms of the construction permit shall expire on December 31, 1986. The constructed pipeline shall be leak tested once a month from June to September and every other month during other months of the year. If a leak in the pipeline is detected it shall be repaired within 20 days and retested for leaks within 15 days thereafter. The carrying out of any leak testing and repairs shall hereunder shall be certified by a professional engineer. Pre-pipeline Operations Petitioners have pointed out the fact that when two or more pollutants are present, as in the instance of the effluent discharged by the Applicant's plant, those pollutants tend to act in a synergistio manner. That can exacerbate the circumstance where you find low dissolved oxygen. This is particularly a matter of concern when discussing Trout Creek. This is unlike the impacts of the discharge into the St. Johns River which are not expected to exceed standards or promote adverse effects. The implications of operation within Trout Creek to allow necessary permit review by DER and the State of Florida, Department of Natural Resources can be overcome once the discharge is withdrawn from Trout Creek and may be addressed by DER more immediately if the dissolved air flotation unit, after a reasonable period of adjustment, does not perform in the fashion that it appears to be capable of. In the instance of discharge into Trout Creek, the material discharged tends to remain in that area for a relatively long period in that the creek is small and has very little flow and poor flushing characteristics. DO levels will be depressed, the presence of a deficit in dissolved oxygen caused by the discharge from the DAF unit would increase the probability of fish kills when contrasted with a circumstance where there is no further deficit of dissolved oxygen. Given the explanation of why a fish kill occurred based upon the past use of fly bait by the Applicant and the fact that there is no indication of fly bait in the present plans, a fish kill in Trout Creek in the time of interim discharged does not seem probable. With the advent of discharge into Trout Creek, the possibility is enhanced for algae blooms and increased eutrophication. There would also be some accumulation of toxic substances. Additionally, there would be some influence on juvenile fish which are more sensitive to pollutants and the possibility exists that it could reach levels that are lethal to bass larvae and juvenile sports fish. The creek would lose some of its viability as a nursery and some fish would leave the creek. These events are not irreversible and can be reasonably remedied with the cessation of discharge into the creek. Moreover, as in the instance with the problem with fish kills, if some set of circumstances attributable to the discharge were to occur in such dimensions as to cause long term impacts in Trout Creek, DER could take action against the construction permit. Dissolved oxygen in Trout Creek can be below the 5 mg/L standard. Data of the E.S.E. group showed that at Highway 13 bridge, approximately fifty yards from the plant in December 1984 and January 1985, values were as low as 0.1 and 0.2 mg/L, and readings could be frequently below 2 mg/L at Highway 13. In April through June 1985, periodic surface dissolved oxygen concentrations were in the range of 3 mg/L and as low as 2.4 mg/L. DO concentrations generally found at the bottom of Trout Creek could be as little or lower than 1 mg/L at times. In July 24, 1985, at the time when the plant had not been operating for approximately a month, the DO concentrations were 2.9 mg/L at mid-depth and 0.8 mg at the bottom. Within Trout Creek in the area of the Pacetti marina, Consultant White measured DO concentrations in the range 1-3 mg/L. On August 10, 1985, six weeks after operations had stopped at the Smith facility, DO concentrations were found to be 3 mg at the surface, less at mid-depth and 0 near the bottom. Computer modeling was not done to ascertain the impacts of a discharge directly into Trout Creek from the DAF unit. The modeling done by the Petitioner's consultant, Parks, using some of the concepts considered in the Applicant's modeling for the St. Johns River is inapplicable to the circumstances in Trout Creek. Trout Creek has also served as a nursing ground for reproduction and habitat for young fish. During the course of the operations by the Applicant in the discharge of essentially untreated effluent, the beds of bass and sun fish have not been seen within the creek. Water quality improves with the DAF unit and sediment loading by heavy metals decreases. Trout Creek is a stressed system at present. It has low levels of dissolved oxygen, high nutrient concentrations and the presence of heavy metals in undesirable amounts. The low numbers of pytoplankton species give some indication of a highly stressed ecosystem. The present officials of DER, Palmer, Owen and Fox, expressed their concerns about dissolved oxygen in those instances where there would be a decrease in ambient DO concentrations. This has particular importance in discussing the problems associated with the discharge into Trout Creek, as opposed to the point of discharge contemplated in the St. Johns River, which risk is minimized given the characteristics of that area and the higher readings of ambient dissolved oxygen in that water, as contrasted with low readings within Trout Creek. A literal interpretation of the position of the agency officials would lead to the conclusion suggested by the Petitioners that no discharge should be allowed into Trout Creek, even on an interim basis. However, such a position would be inherently unfair considering the fact that some discharge would occur into the creek before the installation of the pipeline, whether based upon simultaneous permit review by DER and the State of Florida, Department of Natural Resources in the easement case or sequential review as is contemplated in this instance. Admittedly, the amount of time involved in the discharge into Trout Creek increases in view of the severance of the easement case from the present proceedings. This circumstance occurred in view of the desire on the part of the DNR to see the actual treatment efficiencies involved with the dissolved air flotation unit as opposed to the theoretical possibilities of that equipment. In the present situation, it would be a reasonable policy choice for DER to allow an interim discharge into Trout Creek pending the opportunity for DNR to monitor the quality of the effluent produced by the DAF unit and make a decision about the easement, thus allowing installation of the pipeline if the easement is granted. This arrangement contemplates that DER should closely monitor the quality of the effluent produced by the DAF unit, to make certain, after the Applicant has been given the opportunity to make necessary adjustments to that unit, that the Applicant is not allowed to continue to discharge into Trout Creek following this period of adjustment, when it is shown that the Applicant's equipment is not performing as expected. In any event, the discharge of effluent into Trout Creek will continue over a limited period of time and the system can be expected to quickly return to its healthier state after the removal of the discharge from Trout Creek. This has occurred in the past when the operations of the plant ceased and occurred at a time when the wastewater was of a more damaging quality than contemplated by that associated with the DAF unit. In summary, it would be a reasonable policy choice to allow the interim discharge into Trout Creek on this occasion. Dredge and Fill Permit Characteristics of Pipeline Corridor The pipeline corridor encompasses portions of Trout Creek, Palmo Cove and the St. Johns River. The bottom sediments where the pipeline is to be installed are constituted of soft, and sometimes extremely soft, flocculent silt. Although these sediments are easily resuspended, dispersement of these sediments will only occur while the pipeline is being installed. In placing the pipeline, it is the intention of the Applicant to simply allow the pipe to sink into the sediment. The soft substrate is several feet deep in some places within the proposed corridor. Nonetheless, the pipe is expected to stabilize as it sinks into the material. There are places within the corridor where a crusty material may be found on the surface of or just beneath the substrate. These are locations where jetting or mechanical excavation may be necessary. Jetting may also be necessary along the approximately 155 foot stretch of the corridor that crosses the State of Florida, Department of Transportation right-of-way. This requirement would occur in view of the fact that the Department of Transportation mandates that the pipeline be at a minimum of 30 inches below the creek bottom. In those instances where jetting or other mechanical excavation might be utilized, silt screens would be used to control the short term turbidity. In the areas within the pipeline corridor where tree trunks and branches have been found, these obstructions can be removed without incident. Taking into account the nature of the substrate, at the location where the diffuser will be placed at the end of the pipeline, special attention will be given to that installation to avoid having the diffuser settle into the soft silty material. Given the fact that the silty material is several feet deep and the related fact that the Applicant has not done specific testing of the depth, density and compressibility of this silty material, careful attention should be given to anchoring the diffuser and making certain that the exhaust ports within that device are correctly positioned. The need for this close attention is borne out by the fact that a test pipe which was placed in the silty material settled approximately two and a half feet within several weeks. The matter of the security of the diffuser is also critical, given the fact that the diffuser will be located within one foot of the bottom. Through proper installation, the Applicant can avoid having the diffuser settle into the silty material over time. The installation techniques satisfactorily address the potential problems. Projected Impacts (1) Environmental The icthyological and macroinvertebrate communities within the pipeline corridor have been examined by the Applicant in the person of his consultants. It was found that there are a variety of freshwater fishes within Trout Creek, such as large-mouth bass and sun fish, and a moderate density of macroinvertebrates. The St. Johns River proper is dominated by estuarine and marine aquatic organisms. Infaunal macroinvertebrate densities in the area of the pipeline corridor in the St. Johns River are not high. In placing the pipeline, the effects on aquatic and benthic communities within the corridor or upon water quality do not pose a threat to those communities or to water quality. During the installation of the pipeline, some disturbance of the benthic organisms can be expected; however, those organisms will be able to recolonize quickly. The mere presence of the pipeline is not expected to cause long-term impacts on biological resources or water quality. (b) Navigation In the area of the intended placement of the pipeline related to Trout Creek, boating clubs utilize that vicinity for purposes of anchorage. Those clubs have as many as twenty to thirty boats whose size varies from twenty to fifty-five feet in length. Some of those boats carry anchors which can weigh forty-five pounds or more. Typically, in anchoring one of these craft, the anchor rope is tied down and the engines reversed to set the anchor. Although testimony was given to the effect that the anchors being set might puncture the pipeline, given the explanation about the placement of the pipeline and the nature of the pipe itself, problems with puncturing the pipeline as it might interfere with navigation or environmental concerns such as turbidity plumes due to a puncture of the pipeline are not expected. Nor are the activities associated with retrieval of the anchors via the use of electric winches or hoists seen to be a problem in the sense of snagging the pipeline and rupturing the pipeline when the anchors are brought aboard the vessels. In summary, the pipeline will not be an interference to navigation in the sense of boat anchorage or other aspects of navigation associated with boating. Moreover, the Applicant is willing to indicate the location of the pipeline on navigational charts to assist boaters in avoiding potential problems with anchorage. This is a desirable arrangement and should be done. Comparison of Projected Impacts with Statutory and Regulatory Criteria The dredge and fill activities associated with the pipeline are not expected to cause long-term or short-term adverse impact on biological resources or water quality, or are they expected to interfere with the conservation of natural resources or marine productivity or interfere with navigation to such an extent to be contrary to public interest. The placement of the pipeline will not promote unacceptable interference with fish and other natural resources or destroy clam beds or grass flats, such as would be contrary to the public interest. Permit Conditions Appropriate permit conditions are as follows: Installation of the pipeline shall be conducted within Trout Creek only during weekdays. Pipeline installation activities within Trout Creek shall not block navigation. The pipeline shall be constructed within 60 days following the receipt of all necessary approval, to include the grant of an easement by the State of Florida, Department of Natural Resources for the placement of the pipeline over submerged sovereignty lands. All conditions set forth in the DER draft permit. See Applicant's Exhibit A-57.
The Issue The issues in this case are whether International Paper Company (IP) is entitled to National Pollutant Discharge Elimination System (NPDES) Permit No. FL0002526 issued by Department of Environmental Protection (Department) and whether the Department should approve Consent Order No. 08-0358, for the operation of IP’s paper mill in Cantonment, Escambia County, Florida.
Findings Of Fact The Department is the state agency authorized under Chapter 403, Florida Statutes (2008), to regulate discharges of industrial wastewater to waters of the state. Under a delegation from the United States Environmental Protection Agency, the Department administers the NPDES permitting program in Florida. IP owns and operates the integrated bleached kraft paper mill in Cantonment. FOPB is a non-profit Alabama corporation established in 1988 whose members are interested in protecting the water quality and natural resources of Perdido Bay. FOPB has approximately 450 members. About 90 percent of the members own property adjacent to Perdido Bay. James Lane is the president of FOPB. Jacqueline Lane and James Lane live on property adjacent to Perdido Bay. The mill's wastewater effluent is discharged into Elevenmile Creek, which is a tributary of Perdido Bay. Perdido Bay is approximately 28 square miles in area. U.S. Highway 90 crosses the Bay, going east and west, and forms the boundary between what is often referred to as the "Upper Bay" and "Lower Bay." The Bay is relatively shallow, especially in the Upper Bay, ranging in depth between five and ten feet. At the north end of Perdido Bay is a large tract of land owned by IP, known as the Rainwater Tract. The northern part of the tract is primarily fresh water wetlands. The southern part is a tidally-affected marsh. The natural features and hydrology of the fresh water wetlands have been substantially altered by agriculture, silviculture, clearing, ditching, and draining. Tee Lake and Wicker Lake are small lakes (approximately 50 acres in total surface area) within the tidal marsh of the Rainwater Tract. Depending on the tides, the lakes can be as shallow as one foot, or several feet deep. A channel through the marsh allows boaters to gain access to the lakes from Perdido Bay. Florida Pulp and Paper Company first began operating the Cantonment paper mill in 1941. St. Regis Paper Company acquired the mill in 1946. In 1984, Champion International Corporation (Champion) acquired the mill. Champion changed the product mix in 1986 from unbleached packaging paper to bleached products such as printing and writing grades of paper. The mill is integrated, meaning that it brings in logs and wood chips, makes pulp, and produces paper. The wood is chemically treated in cookers called digesters to separate the cellulose from the lignin in the wood because only the cellulose is used to make paper. Then the "brown stock" from the digesters goes through the oxygen delignification process, is mixed with water, and is pumped to paper machines that make the paper products. In 1989, the Department and Champion signed a Consent Order to address water quality violations in Elevenmile Creek. Pursuant to the Consent Order, Champion commissioned a comprehensive study of the Perdido Bay system that was undertaken by a team of scientists led by Dr. Robert Livingston, an aquatic ecologist and professor at Florida State University. The initial three-year study by Dr. Livingston's team of scientists was followed by a series of related scientific studies (“the Livingston studies"). Champion was granted variances from the water quality standards in Elevenmile Creek for iron, specific conductance, zinc, biological integrity, un-ionized ammonia, and dissolved oxygen (DO). In 2001, IP and Champion merged and Champion’s industrial wastewater permit and related authorizations were transferred to IP. In 2002, IP submitted a permit application to upgrade its wastewater treatment plant (WWTP) and relocate its discharge. The WWTP upgrades consist of converting to a modified activated sludge treatment process, increasing aeration, constructing storm surge ponds, and adding a process for pH adjustment. The new WWTP would have an average daily effluent discharge of 23.8 million gallons per day (mgd). IP proposes to convey the treated effluent by pipeline 10.7 miles to the Rainwater Tract, where the effluent would be distributed over the wetlands as it flows to lower Elevenmile Creek and upper Perdido Bay. IP's primary objective in upgrading the WWTP was to reduce the nitrogen and phosphorus in the mill's effluent discharge. The upgrades are designed to reduce un-ionized ammonia, total soluble nitrogen, and phosphorus. They are also expected to achieve a reduction of biological oxygen demand (BOD) and TSS. IP plans to obtain up to 5 mgd of treated municipal wastewater from a new treatment facility planned by the Emerald Coast Utility Authority (ECUA), which would be used in the paper production process and would reduce the need for groundwater withdrawals by IP for this purpose. The treated wastewater would enter the WWTP, along with other process wastewater and become part of the effluent conveyed through the pipeline to the wetland tract. The effluent limits required by the proposed permit include technology-based effluent limits (TBELs) that apply to the entire pulp and paper industry. TBELs are predominantly production-based, limiting the amount of pollutants that may be discharged for each ton of product that is produced. The proposed permit also imposes water quality-based effluent limits (WQBELs) that are specific to the Cantonment mill and the waters affected by its effluent discharge. The WQBELs for the mill are necessary for certain constituents of the mill's effluent because the TBELs, alone, would not be sufficient to prevent water quality criteria in the receiving waters from being violated. The Livingston studies represent perhaps the most complete scientific evaluation ever made of a coastal ecosystem. Dr. Livingston developed an extensive biological and chemical history of Perdido Bay and then evaluated the nutrient loadings from Elevenmile Creek over a 12-year period to correlate mill loadings with the biological health of the Bay. The Livingston studies confirmed that when nutrient loadings from the mill were high, they caused toxic algae blooms and reduced biological productivity in Perdido Bay. Some of the adverse effects attributable to the mill effluent were most acute in the area of the Bay near the Lanes' home on the northeastern shore of the Bay because the flow from the Perdido River tends to push the flow from Elevenmile Creek toward the northeastern shore. Because Dr. Livingston determined that the nutrient loadings from the mill that occurred in 1988 and 1989 did not adversely impact the food web of Perdido Bay, he recommended effluent limits for ammonia nitrogen, orthophosphate, and total phosphorous that were correlated with mill loadings of these nutrients in those years. The Department used Dr. Livingston’s data, and did its own analyses, to establish WQBELs for orthophosphate for drought conditions and for nitrate-nitrite. WQBELs were ultimately developed for total ammonia, orthophosphate, nitrate-nitrite, total phosphorus, BOD, color, and soluble inorganic nitrogen. The WQBELs in the proposed permit were developed to assure compliance with water quality standards under conditions of pollutant loadings at the daily limit (based on a monthly average) during low flow in the receiving waters. Petitioners did not dispute that the proposed WWTP is capable of achieving the TBELs and WQBELs. Their main complaint is that the WQBELs are not adequate to protect the receiving waters. A wetland pilot project was constructed in 1990 at the Cantonment mill into which effluent from the mill has been discharged. The flora and fauna of the pilot wetland project have been monitored to evaluate how they are affected by IP’s effluent. An effluent distribution system is proposed for the wetland tract to spread the effluent out over the full width of the wetlands. This would be accomplished by a system of berms running perpendicular to the flow of water through the wetlands, and gates and other structures in and along the berms to gather and redistribute the flow as it moves in a southerly direction toward Perdido Bay. The design incorporates four existing tram roads that were constructed on the wetland tract to serve the past and present silvicultural activities there. The tram roads, with modifications, would serve as the berms in the wetland distribution system. As the effluent is discharged from the pipeline, it would be re-aerated and distributed across Berm 1 through a series of adjustable, gated openings. Mixing with naturally occurring waters, the effluent would move by gravity to the next lower berm. The water will re-collect behind each of the vegetated berms and be distributed again through each berm. The distance between the berms varies from a quarter to a half mile. Approximately 70 percent of the effluent discharged into the wetland would flow a distance of approximately 2.3 miles to Perdido Bay. The remaining 30 percent of the effluent would flow a somewhat shorter distance to lower Elevenmile Creek. A computer simulation performed by Dr. Wade Nutter indicated that the effluent would move through the wetland tract at a velocity of approximately a quarter-of-a-foot per second and the depth of flow across the wetland tract will be 0.6 inches. It would take four or five days for the effluent to reach lower Elevenmile Creek and Perdido Bay. As the treated effluent flows through the wetland tract, there will be some removal of nutrients by plants and soil. Nitrogen and phosphorous are expected to be reduced approximately ten percent. BOD in the effluent is expected to be reduced approximately 90 percent. Construction activities associated with the effluent pipeline, berm, and control structures in the wetland tract, as originally proposed, were permitted by the Department through issuance of a Wetland Resource Permit to IP. The United States Army Corps of Engineers has also permitted this work. Petitioners did not challenge those permits. A wetland monitoring program is required by the proposed permit. The stated purpose of the monitoring program is to assure that there are no significant adverse impacts to the wetland tract, including Tee and Wicker Lakes. After the discharge to the wetland tract commences, the proposed permit requires IP to submit wetland monitoring reports annually to the Department. A monitoring program was also developed by Dr. Livingston and other IP consultants to monitor the impacts of the proposed discharge on Elevenmile Creek and Perdido Bay. It was made a part of the proposed permit. The proposed Consent Order establishes a schedule for the construction activities associated with the proposed WWTP upgrades and the effluent pipeline and for incremental relocation of the mill's discharge from Elevenmile Creek to the wetland tract. IP is given two years to complete construction activities and begin operation of the new facilities. At the end of the construction phase, least 25 percent of the effluent is to be diverted to the wetland tract. The volume of effluent diverted to the wetlands is to be increased another 25 percent every three months thereafter. Three years after issuance of the permit, 100 percent of the effluent would be discharged into the wetland tract and there would no longer be a discharge into Elevenmile Creek. The proposed Consent Order establishes interim effluent limits that would apply immediately upon the effective date of the Consent Order and continue during the two-year construction phase when the mill would continue to discharge into Elevenmile Creek. Other interim effluent limits would apply during the 12- month period following construction when the upgraded WWTP would be operating and the effluent would be incrementally diverted from Elevenmile Creek to the wetland tract. A third set of interim effluent limits would apply when 100 percent of the effluent is discharged into the wetland tract. IP is required by the Consent Order to submit quarterly reports of its progress toward compliance with the required corrective actions and deadlines. Project Changes After the issuance of the Final Order in 05-1609, IP modified its manufacturing process to eliminate the production of white paper. IP now produces brown paper for packaging material and “fluff” pulp used in such products as filters and diapers. IP’s new manufacturing processes uses substantially smaller amounts of bleach and other chemicals that must be treated and discharged. IP reduced its discharge of BOD components, salts that increase the specific conductance of the effluent, adsorbable organic halides, and ammonia. IP also reduced the odor associated with its discharge. In the findings that follow, the portion of the Rainwater Tract into which IP proposes to discharge and distribute its effluent will be referred to as the “effluent distribution system,” which is the term used by Dr. Nutter in his 2008 “White Paper” (IP Exhibit 23). The effluent distribution system includes the berms and other water control structures as well as all of the natural areas over which IP’s effluent will flow to Perdido Bay. Most of the existing ditches, sloughs, and depressions in the effluent distribution system are ephemeral, holding water only after heavy rainfall or during the wet season. Even the more frequently wetted features, other than Tee and Wicker Lakes, intermittently dry out. There is currently little connectivity among the small water bodies that would allow fish and other organisms to move across the site. Fish and other organisms within these water bodies are exposed to wide fluctuations in specific conductivity, pH, and DO. When the water bodies dry out, the minnows and other small fish die. New populations of fish enter these water bodies from Elevenmile Creek during high water conditions, or on the feet of water birds. IP's consultants conducted an extensive investigation and evaluation of animal and plant communities in the Rainwater Tract in coordination with scientists from the Department and the Florida Fish and Wildlife Conservation Commission. Among the habitats that were identified and mapped were some wet prairies, which are designated “S-2," or imperiled, in the Florida Natural Area Inventory. In these wet prairies are rare and endangered pitcher plants. IP modified the design of the proposed effluent distribution system to shorten the upper berms and remove 72.3 acres of S-2 habitat. The total area of the system was reduced from 1,484 acres to 1,381 acres. The proposed land management activities within the effluent distribution system are intended to achieve restoration of historic ecosystems, including the establishment and maintenance of tree species appropriate to the various water depths in the system, and the removal of exotic and invasive plant species. A functional assessment of the existing and projected habitats in the effluent distribution system was performed. The Department concluded that IP’s project would result in a six percent increase in overall wetland functional value within the system. That estimate accounts for the loss of some S-2 habitat, but does not include the benefits associated with IP’s conservation of S-2 habitat and other land forms outside of the effluent distribution system. IP proposes to place in protected conservation status 147 acres of wet prairie, 115 acres of seepage slope, and 72 acres of sand hill lands outside the effluent distribution system. The total area outside of the wetland distribution system that the Consent Order requires IP to perpetually protect and manage as conservation area is 1,188 acres. The Consent Order was modified to incorporate many of the wetland monitoring provisions that had previously been a part of the former experimental use of wetlands authorization. IP proposes to achieve compliance with all proposed water quality standards and permit limits by the end of the schedule established in the Consent Order, including the water quality standards for specific conductance, pH, turbidity, and DO, which IP had previously sought exceptions for pursuant to Florida Administrative Code Rule 62-660.300(1). Limitation of Factual Issues As explained in the Conclusions of Law, the doctrine of collateral estoppel bars the parties in these consolidated cases from re-litigating factual issues that were previously litigated by them in DOAH Case No. 05-1609. The Department’s Final Order of August 8, 2007, determined that IP had provided reasonable assurance that the NPDES permit, Consent Order, exception for the experimental use of wetlands, and variance were in compliance with all applicable statutes and rules, except for the following area: the evidence presented by IP was insufficient to demonstrate that IP’s wastewater effluent would not cause significant adverse impact to the biological community of the wetland tract, including Tee and Wicker Lakes. Following a number of motions and extensive argument on the subject of what factual issues raised by Petitioners are proper for litigation in this new proceeding, an Order was issued on June 2, 2009, that limited the case to two general factual issues: Whether the revised Consent Order and proposed permit are valid with respect to the effects of the proposed discharge on the wetland system, including Tee and Wicker Lakes, and with respect to any modifications to the effluent distribution and treatment functions of the wetland system following the Final Order issued in DOAH Case No. 05- 1609; and Whether the December 2007 report of the Livingston team demonstrates that the WQBELS are inadequate to prevent water quality violations in Perdido Bay. Petitioners’ Disputes Petitioners’ proposed recommended orders include arguments that are barred by collateral estoppel. For example, Jacqueline Lane restates her opinions about physical and chemical processes that would occur if IP’s effluent is discharged into the wetlands, despite the fact that some of these opinions were rejected in DOAH Case No. 05-1609. Dr. Lane believes that IP’s effluent would cause adverse impacts from high water temperatures resulting from color in IP’s effluent. There is already color in the waters of the effluent distribution system under background conditions. The increased amount of shading from the trees that IP is planting in the effluent distribution system would tend to lower water temperatures. Peak summer water temperatures would probably be lowered by the effluent. Petitioners evidence was insufficient to show that the organisms that comprise the biological community of the effluent distribution system cannot tolerate the expected range of temperatures. Dr. Lane also contends that the BOD in IP's effluent would deplete DO in the wetlands and Tee and Wicker Lakes. Her contention, however, is not based on new data about the effluent or changes in the design of the effluent distribution system. There is a natural, wide fluctuation in DO in the wetlands of the effluent distribution system because DO is affected by numerous factors, including temperature, salinity, atmospheric pressure, turbulence, and surface water aeration. There are seasonal changes in DO levels, with higher levels in colder temperatures. There is also a daily cycle of DO, with higher levels occurring during the day and lower levels at night. It is typical for DO levels in wetlands to fall below the Class III water quality standard for DO, which is five milligrams per liter (mg/l). An anaerobic zone in the water column is beneficial for wetland functions. DO levels in the water bodies of the effluent distribution system currently range from a high of 11 to 12 mg/l to a low approaching zero. The principal factor that determines DO concentrations within a wetland is sediment oxygen demand (SOD). SOD refers to the depletion of oxygen from biological responses (respiration) as well as oxidation-reduction reactions within the sediment. The naturally occurring BOD in a wetland is large because of the amount of organic material. The BOD associated with IP’s effluent would be a tiny fraction of the naturally occurring BOD in the effluent distribution system and would be masked by the effect of the SOD. It was estimated that the BOD associated with IP's effluent would represent only about .00000000001 percent of the background BOD, and would have an immeasurable effect. Dr. Pruitt’s testimony about oxygen dynamics in a wetland showed that IP’s effluent should not cause a measurable decrease in DO levels within the effluent distribution system, including Tee and Wicker Lakes. FOPB and James Lane assert that only 200 acres of the effluent distribution system would be inundated by IP’s effluent, so that the alleged assimilation or buffering of the chemical constituents of the effluent would not occur. That assertion misconstrues the record evidence. About 200 acres of the effluent distribution system would be permanently inundated behind the four berms. However, IP proposes to use the entire 1,381-acre system for effluent distribution. The modifications to the berms and the 72-acre reduction in the size of the effluent distribution system would not have a material effect on the assimilative capacity of system. The residence time and travel time of the effluent in the system, for example, would not be materially affected. Variability in topography within the effluent distribution system and in rainfall would affect water depths in the system. The variability in topography, including the creation of some deeper pools, would contribute to plant and animal diversity and overall biological productivity within the system. The pH of the effluent is not expected to change the pH in the effluent distribution system because of natural buffering in the soils. The specific conductance (saltiness) of IP’s effluent is not high enough to adversely affect the biological community in the fresh water wetlands of the effluent distribution system. IP is already close to maintaining compliance with the water quality standard for specific conductance and would be in full compliance by the end of the compliance schedule established in the proposed Consent Order. After the 2007 conversion to brown paper manufacturing, IP’s effluent has shown no toxicity. The effluent has passed the chronic toxicity test, which analyzes the potential for toxicity from the whole effluent, including any toxicity arising from additive or synergistic effects, on sensitive test organisms. Dr. Lane points out that the limits for BOD and TSS in the proposed NPDES permit exceed the limits established by Department rule for discharges of municipal wastewater into wetlands. However, paper mill BOD is more recalcitrant in the environment than municipal wastewater BOD and less “bio- available” in the processes that can lower DO. In addition, the regulatory limits for municipal wastewater are technology-based, representing “secondary treatment.” The secondary treatment technology is not applicable to IP’s wastewater. Sampling in the pilot wetland at the paper mill revealed a diversity of macroinvertebrates, including predator species, and other aquatic organisms. Macroinvertebrates are a good measure of the health of a water body because of their fundamental role in the food web and because they are generally sensitive to pollutants. Petitioners contend that the pilot wetland at the paper mill is not a good model for the effect of the IP’s effluent in the wetland distribution system, primarily because of the small amount of effluent that has been applied to the pilot wetland. Although the utility of the pilot wetland data is diminished in this respect, it is not eliminated. The health of the biological community in the pilot wetland contributes to IP’s demonstration of reasonable assurance that the biological community in the effluent distribution system would not be adversely affected. The effluent would not have a significant effect on the salinity of Tee and Wicker Lakes. Under current conditions, the lakes have a salinity of less than one part per thousand 25 percent of the time, less than 10 parts per thousand 53 percent of the time, and greater than 10 parts per thousand 22 percent of the time. In comparison, marine waters have a salinity of 2.7 parts per thousand. IP’s effluent would not affect the lower end of the salinity range for Tee and Wicker Lakes, and would cause only a minor decrease in the higher range. That minor decrease should not adversely affect the biota in Tee and Wicker Lakes or interfere with their nursery functions. The proposed hydrologic loading rate of the effluent amounts to an average of six-tenths of an inch over the area of effluent distribution system. The addition of IP’s effluent to the wetlands of the effluent distribution system and the creation of permanent pools would allow for permanent fish populations and would increase the opportunity for fish and other organisms to move across the effluent distribution system. Biological diversity and productivity is likely to be increased in the effluent distribution system. By improving fish habitat, the site would attract wading birds and other predatory birds. Although the site would not be open to public use (with the exception of Tee and Wicker Lakes), recreational opportunities could be provided by special permission for guided tours, educational programs, and university research. Even if public access were confined to Tee and Wicker Lakes, that would not be a reduction in public use as compared to the existing situation. IP’s discharge, including its discharges subject to the interim limits established in the Consent Order, would not interfere with the designated uses of the Class III receiving waters, which are the propagation and maintenance of a healthy, well-balanced population of fish and wildlife. The wetlands of the effluent distribution system are the “receiving waters” for IP’s discharge. The proposed project would not be unreasonably destructive to the receiving waters, which would involve a substantial alteration in community structure and function, including the loss of sensitive taxa and their replacement with pollution-tolerant taxa. The proposed WQBELs would maintain the productivity in Tee and Wicker Lakes. There would be no loss of the habitat values or nursery functions of the lakes which are important to recreational and commercial fish species. IP has no reasonable, alternative means of disposing of its wastewater other than by discharging it into waters of the state. IP has demonstrated a need to meet interim limits for a period of time necessary to complete the construction of its alternative waste disposal system. The interim limits and schedule for coming into full compliance with all water quality standards, established in the proposed Consent Order, are reasonable. The proposed project is important and beneficial to the public health, safety, and welfare because (1) economic benefits would accrue to the local and regional economy from the operation of IP’s paper mill, (2) Elevenmile Creek would be set on a course of recovery, (3) the wetlands of the effluent distribution system would become a site of greater biological diversity and productivity, (4) the environmental health of Perdido Bay would be improved, (5) the Department’s decades-long enforcement action against IP would be concluded, (6) substantial areas of important habitat would be set aside for permanent protection, and (7) the effluent distribution system would yield important information on a multitude of scientific topics that were debated by these parties. The proposed project would not adversely affect the conservation of fish or wildlife or their habitats. The proposed project would not adversely affect fishing or water-based recreational values or marine productivity in the vicinity of the proposed discharge. There is no Surface Water Improvement and Management Plan applicable to IP’s proposed discharge. The preponderance of the record evidence establishes reasonable assurance that IP’s proposed project would comply with all applicable laws and that the Consent Order establishes reasonable terms and conditions to resolve the Department’s enforcement action against IP for past violations.
Recommendation Based upon the foregoing Findings of Fact and Conclusions of Law, it is: RECOMMENDED that the Department enter a final order granting NPDES Permit No. FL0002526 and approving Consent Order No. 08-0358. DONE AND ENTERED this 27th day of January, 2010, in Tallahassee, Leon County, Florida. BRAM D. E. CANTER Administrative Law Judge Division of Administrative Hearings The DeSoto Building 1230 Apalachee Parkway Tallahassee, Florida 32399-3060 (850) 488-9675 Fax Filing (850) 921-6847 www.doah.state.fl.us Filed with the Clerk of the Division of Administrative Hearings this 27th day of January, 2010.
