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HomeMy WebLinkAboutWQ0002146_Final Permit_19970623State of North Carolina Department of Environment, Health and Natural Resources Division of Water Quality James B. Hunt, Jr., Governor Jonathan B. Howes, Secretary A. Preston Howard, Jr., P.E., Director June 23, 1997 Mr. Lawrence D. Lively, V.P. Environmental Affairs Gwaltney of Smithfield, Ltd. 900 Dominion Tower 999 Waterside Drive Norfolk, Virginia 23510 Dear Mr. Lively: "4 �j� �EHN1=1 Subject: Permit No. WQ0002146 Gwaltney of Smithfield, Ltd. Land Application of Wastewater Residuals Sampson County In accordance with your application received on March 3, 1997, we are forwarding herewith Permit No. WQ0002146, dated June 23, 1997, to Gwaltney of Smithfield, Ltd. for the operation of a wastewater residuals land application program. This permit shall be effective from the date of issuance until May 31, 2002, shall void Permit No. WQ0002146, issued September 16, 1992, and shall be subject to the conditions and limitations as specified therein. Please pay particular attention to the monitoring and reporting requirements contained in this permit. Failure to establish an adequate system for collecting and maintaining the required operational information will result in future compliance problems. If any parts, requirements, or limitations contained in this permit are unacceptable, you have the right to request an adjudicatory hearing upon written request within thirty (30) days following receipt of this permit. This request must be in the form of a written petition, conforming to Chapter 150B of North Carolina General Statutes, and filed with the Office of Administrative Hearings, P.O. Drawer 27447, Raleigh, NC 27611-7447. Unless such demands are made this permit shall be final and binding. If you need additional information concerning this matter, please conta6FRic1 1V 66te at (919) 733- 5083 extension 527. Sincere , �-A. Preston Howard, Jr., P.E. cc: Sampson County Health Department Gwaltney of Smithfield, Ltd.; Mr. Charles Fiero Fayetteville Regional Office, Water Quality Section Fayetteville Regional Office, Groundwater Section Bob Cheek, Groundwater Section, Central Office Training and Certification Unit Facilities Assessment Unit P.O. Box 29535, Raleigh, North Carolina 27626-0535 Telephone (919) 733-5083 FAX (919) 733-0719 An Equal Opportunity Affirmative Action Employer 50% recycled/ 10% post -consumer paper NORTH CAROLINA ENVIRONMENTAL MANAGEMENT COMMISSION DEPARTMENT OF ENVIRONMENT, HEALTH AND NATURAL RESOURCES RALEIGH RESIDUALS LAND APPLICATION PERMIT In accordance with the provisions of ,Article 21 of Chapter 143, General Statutes of North Carolina as amended, and other applicable Laws, Rules, and Regulations PERMISSION IS HEREBY GRANTED TO Gwaltney of Smithfield, Ltd. Sampson County operation of a wastewater residuals land application program consisting of the application of 1,000 GPD of residuals from sources listed in Condition II 5, to approximately 61 acres of land in Sampson County with no discharge of wastes to the surface waters, pursuant to the application received on March 3, 1997, and in conformity with the project plan, specifications, and other supporting data subsequently filed and approved by the Department of Environment, Health and Natural Resources and considered a part of this permit. This permit shall be effective from the date of issuance until May 31, 2002, shall void Permit No. WQ0002146, issued September 16, 1992, and shall be subject to the following specified conditions and limitations: I. PERFORMANCE STANDARDS 1. The Fayetteville Regional Office, telephone number (910) 486-1541, and the appropriate local governmental official (county manager/city manager) shall be notified at least twenty- four (24) hours prior to the initial application of the residuals to a site so that an inspection can be made of the application sites and application method. Such notification to the regional supervisor shall be made during the normal office hours from 8:00 a.m. until 5:00 p.m. on Monday through Friday, excluding State Holidays. In addition, the Sampson County Manager's office must be notified prior to the initial application so that they will be aware that the operation has commenced. 2. This permit shall become voidable if the soils fail to adequately assimilate the wastes and may be rescinded unless the sites are maintained and operated in a manner which will protect the assigned water quality standards of the surface waters and ground waters. 3. The land application program shall be effectively maintained and operated as a non - discharge system to prevent the discharge of any wastes resulting from the operation of this program. 4. The issuance of this permit shall not relieve the Permittee of the responsibility for damages to surface or groundwaters resulting from the operation of this program. 5. In the event that the land application program is not operated satisfactorily, including the creation of nuisance conditions, the Permittee shall cease applying residuals to the sites and take any immediate corrective actions as maybe required by the Division. 6. Some of the buffers specified below may not have been included in previous permits for this land application operation. However, any sites or fields that are included in this permit, but were approved with different applicable buffers shall be reflagged to comply with the below buffers. The following buffer zones shall be maintained: a) 400 feet from residences or places of public assembly under separate ownership for surface application method; however, the buffer zone requirement may be reduced to a minimum of 100 feet upon written consent of the owner and approval from the appropriate DWQ regional office, b) 200 feet from residences or places of public assembly under separate ownership for subsurface residual injection method; however, the buffer zone requirement may be reduced to a minimum of 100 feet upon written consent of the owner and the appropriate DWQ regional office, c) 100 feet from any public or private water supply source, waters classified as SA or SB, and any Class I or Class II impounded reservoir used as a source of drinking water for both methods, d) 100 feet from any streams classified as WS or B, any other stream, canal, marsh or coastal waters and any other lake or impoundment for surface application, e) 50 feet from any streams classified as WS or B, any other stream, canal, marsh or coastal waters and any other lake or impoundment for subsurface application, f) 50 feet from property lines for both surface and subsurface application methods; g) 50 feet from public right of ways for both application methods, h) 10 feet from upslope interceptor drains and surface water diversions for both application methods, i) 25 feet from downslope interceptor drains, surface water diversions, groundwater drainage systems and surface drainage ditches for both application methods. 7. A copy of this permit shall be maintained at the land application site when residuals are being applied during the life of this permit. A spill prevention and control plan shall be maintained in all residuals transport and application vehicles. 8. Specific residual application area boundaries shall be clearly marked on each site prior to and during application. 9. No residuals at any time shall be stored at any application site, unless approval has been requested and obtained from the Division of Water Quality. 10. Maximum slope for residual application shall be 10% for surface application and 18% for subsurface applications. 11. When residuals from an animal processing facility are being land applied, one of the following stabilization methods shall be completed to control possible nuisance conditions: a. The residuals are subsurfacely injected, or b. The residuals are incorporated into the soil within 24 hours, or c. Sufficient lime is added to the residuals to create a uniform mixture and achieve a pH of 10 for thirty minutes prior to being surface land applied. 2 11. OPERATION AND MAINTENANCE REQUIREMENTS I . The facilities and application sites shall be properly maintained and operated at all times. 2. A suitable vegetative cover, as listed in condition II 4, shall be maintained in accordance with the crop management plan outlined by the local Extension Office of the Department of Agriculture, the Natural Resources Conservation Service, or other agronomist, and approved by this Division. 3. An acceptable pH must be maintained in the soil, residual and lime mixture, greater than 6.0, on all land application sites to insure optimum yield for the crop(s) specified below. The agronomist shall provide information on the pH best suited for the specified crop and the soil type. 4. The application rates shall not exceed the following for the specified crops: Crop PAN lb./acrel yr. 5. go Alfalfa 200 Bermuda Grass (Hay, Pasture) 220 BIue Grass 120 Corn (Grain) 160 Corn (Silage) 200 Cotton 70 Fescue 250 Forest (Hardwood & Softwood) 75 Milo 100 Small Grain (Wheat, barley, oats) 100 Sorghum, Sudex (Pasture) 180 Sorghum, Sudex (Silage) 220 Soybeans 200 Timothy, Orchard, & Rye Grass 200 No residuals other than the following are hereby approved for land application in accordance with this permit: Source County Volume Gwaltney of Smithfield, Ltd. Sampson 1,000 GPD The metal Ioading rates shall not exceed the following Curn alative Pollutant loading rates: Kilograms Pounds Parameters jer Hectare per Acre Arsenic 41 36 Cadmium 39 34 Copper 1,500 1,338 Lead 300 267 Mercury 17 15 Molybdenum ---- ---- Nickel 420 374 Selenium 100 89 Zinc 2,800 2,498 3 7. The pollutant concentrations in the residuals which will be applied to the land shall not exceed the following Ceiling Concentrations (Dry Weight Basis): Parameters mg/ka Arsenic 75 Cadmium 85 Copper 4,300 Lead 840 Mercury 57 Molybdenum 75 Nickel 420 Selenium 100 Zinc 7,500 Upon classification of the facility by the Certification Commission, the Permittee shall employ a certified land application/residuals operator to be in responsible charge (ORC) of the land application program. The operator must hold a certificate of the type classification assigned to the land application program, by the Certification Commission. The Permittee must also employ a certified back-up operator of the appropriate type to comply with the conditions of Title 15A NCAC 8A, .0202. 9. Adequate procedures shall be provided to prevent surface runoff from carrying any disposed or stored residuals into any surface waters. 10. Surface applied residuals will be plowed or disced within twenty-four (24) hours after application on lands with no cover crop established. 11. For areas that are prone to flooding or within the 100-year flood elevation, residuals may be applied only during periods of dry weather. The residuals must be incorporated into the soil within twenty-four (24) hours after application. 12. Appropriate measures must be taken to control public access to the land application sites during active site use and for the 12-month period following the last residual application event. Such controls may include the posting of signs indicating the activities being conducted at each site. 13. Adequate provisions shall be taken to prevent wind erosion and surface runoff from conveying pollutants from the residuals application area onto the adjacent property or into any surface waters. 14. Residuals shall not be applied in inclement weather or until 24 hours following a rainfall event of 1/2-inch or greater in 24 hours. Any emergency residuals disposal measures must first be approved by the Division of Water Quality. 15. Residuals shall not be applied to any land application site that is flooded, frozen or snow- covered. lb. Residuals shall not be applied at rates greater than agronomic rates, unless authorized by the Division. 17. Animals shall not be grazed on an application site for 30 days after residuals application. Application sites that are to be used for grazing shall have fencing that will be used to prevent access after each application. II 18. Food crops, feed crops and fiber crops that do not come in contact with the residuals shall not be harvested for 30 days after residuals application. 19. Food crops with harvested parts that touch the residual/soil mixture and are totally above the land surface (ex. tobacco, melons, cucumbers, squash, etc.) shall not be harvested for 14 months after residuals application. 20. Food crops with harvested parts below the surface of the land (root crops such as potatoes, carrots, radishes, etc.) shall not be harvested for 20 months after application of residuals when the residuals remain on the land surface for four (4) months or longer prior to incorporation into the soil. 21. Food crops with harvested parts below the surface of the land shall not be harvested for 38 months after application of residuals when the residuals remain on the land surface for less than four (4) months prior to incorporation into the soil. 22. Turf shall not be harvested for 1 year after residuals application if the turf is to be placed on land with a high potential for public exposure. MONITORING AND REPORTING REQUIREMENTS 1. Any monitoring (including groundwater, surface water, residuals, soil, or plant tissue analyses) deemed necessary by the Division of Water Quality to insure protection of the environment will be established and an acceptable sampling and reporting schedule shall be followed. 2. Proper records shall be maintained by the Permittee tracking all application activities. These records shall include, but are not necessarily limited to the following information: a. source of residuals b . date of residual application c. location of residual application (site, field, or zone #) d . method of application e. weather conditions (sunny, cloudy, raining, etc.) f . soiI conditions g . type of crop or crops to be grown on field h . volume of residuals applied in gallons/acre, dry tons/acre or kilograms/hectare i. annual and cumulative totals of dry tons/acre of residuals, annual and cumulative pounds/acre of each heavy metal (which shall include, but not be limited to arsenic, cadmium, copper, lead, mercury, molybdenum, nickel, selenium and zinc), annual pounds/acre of plant available nitrogen (PAN), and annual pounds/acre of phosphorus applied to each field. A representative annual soils analysis (Standard Soil Fertility Analysis) shall be conducted on each site receiving residuals in the respective calendar year and the results maintained on file by the Permittee for a minimum of five years. The Standard Soil Fertility Analysis shall include, but is not necessarily limited to, the following parameters: Acidity Calcium Copper Magnesium Base Saturation (by calculation) Cation Exchange Capacity Manganese Potassium Percent Humic Matter Sodium pH Zinc Phosphorus 5 The Standard Soil Fertility Analysis (see above) and an analysis for the following pollutants shall be conducted once prior to permit renewal on soils from each site which has received residuals during the permit cycle. Arsenic Mercury Nickel Cadmium Molybdenum Selenium Lead 4. A residuals analysis will be conducted annually from the date of permit issuance by the Permittee and the results maintained on file by the Permittee for a minimum of five years. If land application occurs at a frequency less than annually a residuals analysis will be required for each instance of land application. The residuals analysis shall include but is not necessarily limited to the following parameters: Arsenic Calcium Cadmium Nitrate -Nitrite Nitrogen Copper Magnesium Lead % Total Solids Mercury pH Molybdenum Phosphorus Nickel Plant Available Nitrogen (by calculation) Selenium Potassium Zinc Sodium Aluminum TKN Ammonia -Nitrogen 5. All residuals included in this permit must be monitored annually from the date of permit issuance, for compliance with condition I 11 of this permit. Data to verify stabilization and vector attraction reduction of the residuals must be maintained by the Permittee. The required data is specific to the stabilization process utilized, but should be sufficient to clearly demonstrate compliance the Class A pathogen requirements in 40 CFR Part 503.32(a) or with the Class B pathogen requirements and site restrictions in 40 CFR Part 503.32(b), and one of vector attraction reduction requirements in 40 CFR Part 503.33. In addition, the EPA certification statements concerning compliance with pathogen requirements, vector attraction reduction requirements and management practices must be completed annually by the proper authority or authorities if more than one is involved, either the person who prepares the residuals, the person who derives the material, or the person who applies the residuals. 6. Three copies of all required monitoring and reporting requirements as specified in conditions III 1, III 2,1113, III 4, III 5 shall be submitted annually on or before March 1 of the following year to the following address: NC Division of Water Quality Water Quality Section Facility Assessment Unit PO Box 29535 Raleigh, NC 27626-0535 31 7. Noncompliance Notification: The Permittee shall report by telephone to the Fayetteville Regional Office, telephone number (910) 485-1541 as soon as possible, but in no case more than 24 hours or on the next working day following the occurrence or first knowledge of the occurrence of any of the following: a. Any occurrence with the land application program which results in the land application of significant amounts of wastes which are abnormal in quantity or characteristic. b . Any failure of the land application program resulting in a release of material to receiving waters. c. Any time that self -monitoring information indicates that the facility has gone out of compliance with the conditions and limitations of this permit or the parameters on which the system was designed. d . Any process unit failure, due to known or unknown reasons, that render the facility incapable of adequate residual treatment. e. Any spillage or discharge from a vehicle or piping system transporting residuals to the application site. Persons reporting such occurrences by telephone shall also file a written report in letter form within five (5) days following first knowledge of the occurrence. This report must outline the actions taken or proposed to be taken to ensure that the problem does not recur. IV. GROUNDWATER REQUIREMENTS 1. The COMPLIANCE BOUNDARY for the disposal system is specified by regulations in 15A NCAC 2L, Groundwater Classifications and Standards. An exceedance of Groundwater Quality Standards at or beyond the Compliance Boundary is subject to immediate remediation action in addition to the penalty provisions applicable under General Statute 143-215.6A(a)(1). The sale of property' by the Permittee, which is within or contiguous to the disposal system site, may alter location of the compliance boundary. For facilities permitted on or after December 30, 1983, the Compliance Boundary is established at the lesser of 250 feet from the application field or 50 feet within the property boundary. If the title for any property which may affect the location of the Compliance Boundary" is changed, the Permittee shall notify the Division Director within 14 days. The Director shall then establish a modified Compliance Boundary which will be done as a modification to the permit. 2. Any groundwater quality monitoring, as deemed necessary by the Division, shall be provided. 7 V. 1A-1 INSPECTIONS The Permittee or his designee shall inspect the residuals storage, transport, and application facilities to prevent malfunctions and deterioration, operator errors and discharges which may cause or lead to the release of wastes to the environment, a threat to human health, or a nuisance. The Permittee shall maintain an inspection log or summary including at least the date and time of inspection, observations made, and any maintenance, repairs, or corrective actions taken by the Permittee. This log of inspections shall be maintained by the Permittee for a period of five years from the date of the inspection and shall be made available to the Division of Water Quality or other permitting authority, upon request. 2. Any duly authorized officer, employee, or representative of the Division of Water Quality may, upon presentation of credentials, enter and inspect any property, premises or place on or related to the application site or facility at any reasonable time for the purpose of determining compliance with this permit; may inspect or copy any records that must be kept under the terms and conditions of this permit; and may obtain samples of groundwater, surface water, or leachate. GENERAL CONDITIONS This permit shall become voidable unless the land application activities are carried out in accordance with the conditions of this permit, the supporting materials, and in the manner approved by this Division. 2. This permit is effective only with respect to the nature and volume of wastes described in the application and other supporting data. 3. This permit is not automatically transferable. In the event that there is a desire for the facilities to change ownership or a name change of the Permittee, a formal permit request must be submitted to the Division of Water Quality accompanied by an application fee, documentation from the parties involved, and other supporting materials as may be appropriate. The approval of this request will be considered on its merits and may -or may not be approved. 4. The following are approved sites for residuals application (see attached map[s]). Application Area [acres] Site No. Owner/Lessee (excluding buffers) Sampson County I Gwaltney of Smithfield, Ltd. 3 II Ralph Bass 8 III Ralph Bass 50 TOTAL ACRES IN COUNTY 61 TOTAL AVAILABLE ACRES 61 5. Failure to abide by the conditions and limitations contained in this permit may subject the Permittee to an enforcement action by the Division of Water Quality in accordance with North Carolina General Statute 143-215.6(a) to 143-215.6(c). M. 6. The annual administering and compliance fee must be paid by the Permittee within thirty (30) days after being billed by the Division. Failure to pay the fee accordingly may cause the Division to initiate action to revoke this permit as specified by 15 NCAC 2H .0205 (c)(4)• 7. The issuance of this permit does not preclude the Permittee from complying with any and all statutes, rules, regulations, or ordinances which may be imposed by other government agencies (local, state, and federal) which have jurisdiction. S. The Permittee, at least six (6) months prior to the expiration of this permit, shall request its extension. Upon receipt of the request, the Commission will review the adequacy of the facilities described therein, and if warranted, will extend the permit for such period of time and under such conditions and limitations as it may deem appropriate. 9. This permit may be modified, or revoked and reissued to incorporate any conditions, limitations and monitoring requirements the Division of Water Quality deems necessary in order to adequately protect the environment and public health. 10. This permit shall become voidable unless the agreements between the Permittee and the I andowners/les sees are in full force and effect. The land owner agreements are considered expired concurrent with the expiration date of the permit and must be renewed at the same time the permit is renewed. Permit issued this the twenty-third day of June, 1997. NORTH CAROLINA ENVIRONMENTAL MANAGEMENT COMMISSION A. Preston Howard, Jr., P.E., Director Division of Water Quality By Authority of the Environmental Management Commission Permit Number WQ0002146 9 y � e000 AF / 0.0 � yt �t �� / Mom.` •'� � , t ' � �/ E .�f , ' � / ����'" •i ��•''a. � �i�'' ��. � '-�T�����..-•yam � % {� T • `.-- ,�: ti, .,. i •� ��' •oF / 9 �.� D � it (COHAR/E r sx sool � ur 6J31JN •�i 1 ': u1.•.+,d.'..'1 .+r m .r�::.+'.: �r. HATING SCALE FOR CLASSIFICATION OF WATER POLLUTION CONTROL SYSTEMS Name of Facility: ccJa/ *." Of' Srri Z%; / a 4fc3% Owner or Contact -Person: ` — Mailing Address: PO_ 4',17 _647LC= /le-4/V ,. County: S a..Ps� __Telephone: Present Classification: New Facility Existing Facility NPDES Per. No. NC00 Nondisc. Per. No.WO-4192241,z6 Health Dept.Per No. Rated by: Telephone: Date: Reviewed by: Health Dept. Telephone: Regional Office Telephone: Central Office Telephone: ORC: -6-ca < Grade: Teleph e: Check Classification(s): Subsurface Spray Irrigation I Land Application Wastewater Classification: (Circle One) 1 11 111 IV Total Points: -Ieli L__ SUBSURFACE CL SSiFICr4TION (check all units that apply) 1. septic tanks 2. pump tanks 3. siphon or pump -dosing systems 4, sand filters 5. grease trapfinterceptor 6. oil/water separators 7, gravity subsurface treatment and disposal: S. pressure subsurface treatment and disposal: SPRAY IRRIGATION Ct ASStFiCATION (check all units that apply) 1. preliminary treatment (definition no. 32 } 2. lagoons 3. septic tanks 4. pump tanks 5, pumps 6. sand filters 7. ,_grease trapinterceptor 8. oil/water separators 9 _____ldisinfection 10. chemlral addition for nutrientlalgae control 11. spray irrigation of wastewater In addition to the above classifications, pretreatment of wastewater In excess of these components shall be rated using the point rating system and wilt require an operator with an appropriate dual certification. LAND APPLICATION/RESIDUALS CLASSIFICATION (Applies only to permit holder) I. Land application of bicsolids, residuals or contaminated soils on a designated site. WASTEWATER TREATMENT FACILITY CLASSIF)CATION The following systems shall be assigned a Class I clasalcation, unless the flow €s of a significant quantity or the technology is unusually complex, to require consideration by the Commission on a case -by -case basis: (Check if Appropriate) 1. O!Vwater Separator Systems consisting only of physical separation, pumps and disposal; 2. Septic TanklSand F€fter Systems consisting only of septic tanks, dosing apparatus, pumps,sand fitters, disinfection and direct discharge; 3. Lagoon Systems consisting only of preliminary treatment, lagoons, pumps, disinfection, necessary chemical treatment for algae or nutrient control, and direct discharge; 4. Closed -loop Recycle Systems; 5- Groundwater Remediation Systems consisting only of oil/water separators, pumps, air -stripping, carbon adsorption, disinfection and dispo ,J; 6. Aquacufture operations with discharge to surface waters; 7� _ Water Plant sludge handling and back -wash water treatment; 8. Seafood processing consisting of screening and disposal. 9. single-family discharging systems, with the exception of Aerobic Treatment Units, will be classified if permitted after .July 1, 1993 or If upon inspection by the Division, it is found that the system is not being adequately operated of maintained. Such systems will be notified of the classification or reclassification by the Commission, in writing. The following scale is used for rating wastewater treatment facilities, (circle appropriate points) ITEM POINTS (1) Industrial Pretreatment Units or Industrial Pretreatment Program (see definition No. 33)...................................................4 (2) DESIGN FLOW OF PLANT IN gpd [not applicable to non -contaminated cooling waters, sludge handling facilities for water purification plants, totally closed cycle systems(sae definition No. 11), and facilities consisting only of ham (4)(d) or items (4)(d) and (11)(d)] 0 - 20.000...............................................................................................................................1 20,001 - 50,000......................................................................................................................................2 50,001 - 100.000....................................................................................................................................3 100.001 - 250,000...................................................................................................................................4 250,001 - 500,000..........................................................................................................__......................5 500,001 - 1,000,900 ..................................................................................._..............................._............a 1.000,001 - 2,006,000.............................................. .............................................................................10 2.000,001 (and up} rate 1 point additional for each 200.000 gpd capacity up to a maximum of .................30 Design Flow (gpd) (3) PRELIMINARY UNITSIPROCESSES (see definition No.321 (a) BarScraens.................................................................................. ...t or (b) Mechanical Screens, Static Screens or Comminuting Devices..........................................................................2 (c) Grit Removal..........................................................................................................................................1 or (d) Mechanical or Aerated Grit Removal ........................ ........ ............................................................................. 2 (e) Flow Measuring Device................................................................................................................................1 or (f) Instrumented Flow Measurement ................................................................ .........................2 (g) Praaeratlon............................_.........._.................................................__..2 (h) Influent Flow Equalization ................................... (1) Grease or Oil Separators - Gravity................................................................................................ .......2 Mechanical.................................................................................................................................................3 Dissolved Alr Flotation............................................•.•..•..•....................--.....................................................a (1) Prechlorination......................... ....................................................... .......................................................... 5 (4) PRIMARYTREATMENTLNrFVPROCESSES (a) Septic Tank (sea definition No. 43)........................................................................................................2 (b) Imhoff Tank............................................................................................................................................5 (c) Primary Clariflers..-»................................ (d) Settling Ponds or Settling Tanks for lrwrgallo Ncrrloxk Materials (sludge handling facilities for water pur'rf€cation plants, sand, gravel, stone, and other mining operations except recreational activities such as gem orgold mining)...........................................--•--..............._........--............................._........2 (5) SEC�TREATMENT tNITS+PROCESSES (a) Carbonaceous Stage {i) Aeration-Mgh Purity Oxygen System..............................................................................20 DiffusedAir System.........................................................................•...._.._._...................10 Mechanical Air System (fixed, floating or rotor) ....................................................... Separate Sludge Reaeratlon............................................................................................ 3 (li} Trickling Filter HighRate........................................................................_......._.._..........7 StandardRate............................................................................................................... PackedTower......................................................................................--..................5 (fit) Biological Aerated Filter or Aerated Biological Filter 0 (Iv) Aerated Lagoons..............---......................................................__......--..........10 (v) Rotating Biological Conta=rs.................................................................................... .10 (vi) Sand Filters -Intermittent biological......................._..........•......___....._.._...........................2 Recirculatingbiological....................................................................................................3 (vii) Stabilization Lagoons........................................•-•--........................................................5 (vii€) Clarifier.........................................................................••--......-_.....................................5 (fx) S€ngla stage system for combined carbonaceous removal of BOD and nitrogenous removal by nitrification (sae definition No. 12){Points for this hem have to be in addition to items (5)(a)(1) through (5)(a)(v€€i), utlllzing the extended aeration process (see definition No.3a)..........................................2 utilizing other than the extended aaradon process ..................................................... ... a (x) Nutrient additions to enhance BOD removal......................................................................5 (x1) Biological Culture (-Super Bugs')additlon........................................................................5 (b) Nitrogenous Stage (1) Aeration - High Purity Oxygen System...................................._...._....----._.....................20 DiffusedAir System.......................................................................................................1 0 Mechanical Air System (fixed, floating or rotor) .......... _..... ............................... ............. Separate Sludge Roasmtfon............................................................................................2 (11) Trickling Flier -High Rate .................................................................. ................................7 Standard Rat* .................. _........................................................................................... 4 PackedTower............................................................. ................................................... .5 (if[) Biological Aerated Filter or Aerated Biological 0 (IV) Rotating Biological Confactors......................................................................................1 0 (v) Sand Filter - Intermittent bloiogical...................................................................................2 Recirculating biological...................................................................._......._.......3 5 (6) TERTWRYORADVANCEDTRFATME T[NrFS1PROCESSF� (a) Activated Carbon Beds - without carbon regeneratfon....................._..__............................,..................................5 withcarbon regeneration................•.•.....--•--._....................................-------•----......•.................15 (b) Powdered or Granular Activated Carbon Food - without carbon regeneration.................................................................................................5 xhh carbon regeneration............................................ .........................................................1 5 (c) Air stripping..........................................................__........_...5 (d) Danhrificatlon Process..................................................................----............_.........................10 (a) Elactrodfalysis......................................................._.......__._..............._...............................................5 (f) Foam Separatlon.............................._•......_.................................---........_.......5 (g) Ion Exchange ................................ ...............................•....................---............__..............................5 (h) Land Application of Treated Etfluert (see definition No. 22b) (not applicable for sand, gravel, stone and other similar mining operations) by high rate Infiltration. .-.....-.-_...__..._..._..................--..._..-- _.......... 4 (1) Microscraens...................................................................................,....__.............__...........5 (1) Phosphorous Removal by Blclogicaf Processes (Soo dogri4lon No, 26)........................................................20 (k) Polishing Ponds - without aeration ............... _........................................................................ __.............. 2 withaeration .... _............. ........................................ ................................................. .5 (1) Past Aeration - cascade .......... ..................................... ..................................... .......................................... a diffusedor mechanical ................................................... ..................................................... 2 (m) Reverse Osmosis...................................................................................•--•-..........................._.............._.....5 (n) Sand or Mixed -Media Filters - low rate ....................... ................................................................................. 2 highrate......................................................................5 (o) Treatment processes for removal of metal or cyanide.................................................................__..............1 5 (p) treatment processes for removal of toxic materials other than metal or cyanide............................................1 5 (7) SLUCGETREATMENT (a) Sludge Digestion Tank - Heated (anaerobic)...............................................................................................1 0 Aerobic 5 Unheated(anaerobic).................................................................................... .. (b) Sludge Stabilization (chemical or thenTW)...................................................................................................5 (c) Sludge Drying Beds - Gravity......................................................................................................................2 VacuumAssisted......................................................................................................................................5 (d) Sludge Elutriation.....................................................................................................................................5 (a) Sludge Conditioner (chemical or thermal) ........ _..........................................................................................5 (f) Sludge Thickener (gravity).........................................................................................................................5 (g) Dissolved Air Flotation Unit [not applicable to a unit rated as(3)(i)].............................................................8 (h) Sludge Gas Utilization (including gas storage) .................. (I) Sludge Holding Tank - Aerated...................................................................................................................5 Non -aerated ................................................ 2 (J) Sludge Incinerator (not Including activated carbon regeneration)................................................................10 (k) Vacuum Filter, Centrifuge, or Filter Press or other similar dewatering devices ..... ... .........................................10 (8) RESIDUALS UTiL¢ATIOWDISPOSAL (indudfng incinerated ash) (a) Lagoons .............................. .........................•....••....•................................................................_...............2 (b) Land Application (surface and subsurface) (see definition 22a) by contracting to a land application operator or landfill operator who holds the land application permit orlandfill permit............................•................................................................--...._......................._............2 (a) Dedicated Lancifill(burial) by the permittee of the wastewater treatmentfacility..._.................... „................ ..S 9 ( ) (a) Chlorination.............................................................................................................................................. (b) Dechlorinalion....••••••••.......................................................................................• 5 (c) Ozone.......................•-•........................_.•.._.•.._.................•---.............».............-•.•-.••-...--•._..............._...._..5 (d) Radiation..................................................................................................................................................5 (10) CHEMICAL ADDITION SYSTEM(S) ( see definition No. 9) [not applicable to chemical additions rated as item (3)(1). (5)(a)(xi), (6)(a), (6)(b), (7)(b), (7)(e), (9a), (9)(b) or (9)(c) 5 points each., List......................................................................................................................................5 .---•.................................................•-•..................................................._.......................5 ....................................................................................................................................5 (1 1) ....................... ..........................•---••------._--•.. ._.................................................. —........... M SCELLANEOUS UNrfSrPi70CESSES (a) Holding Ponds, Holding Tanks or Settling Ponds for Organic or Toxic Materials Including wastes from mining operations containing nitrogen or phosphorus compounds in amounts significantly greater than Is common fordomestic wastewater............................................................................................................................4 (b) Effluent Flow Equalization (not applicable to storage basins which are inherent in land application symems).....2 (c) Stage Discharge (not applicable to storage basins Inherent In land application (d) Pumps .............. .:......................................... ••......3 (e) Stand -By Power Supply ...................... ........................ (f) .....3 Thermal Pollution Control Device................................................................................................................3 TOTALPOINTS.......................................................................... CLASSiFiCATICN Class.....................................................................................................5-25 Points ClassIl........................................................................................................26.50 Points Classill........................................................................................................51.65 Points ClassN.................................... ........................................................ .......... 66-Up Points ------------- Facilities having a rating of one through four points, inclusive, do not require a certified operator. Facilities having an activated &fudge process will be assigned a minimum classification of Class II. Facilities having treatment processes for the removal of metal or cyanide will be assigned a minimum classification of Class II. Facilities having treatment processes for the biological removal of phosphorus will be assigned a minimum classification of Class ill. ------------------------------------------------------------- DC01 DEFINrrK)NS The following definitions shall apply throughout this Subchapter. (1) Activated Carbon Beds. A physlcallchemicaf method for reducing soluble organic material from wastewater effluent; The column -type beds used in this method will have a flow rate varying from two to eight gallons per minute per square foot and may be either upflow or downflow carbon beds. Carbon may or may not be regenerated on the wastewater treatment plant she; (2) Aerated Lagoons. A basin In which all solids are maintained In suspension and by which biological oxidation or organic matter is reduced through artificially accelerated transfer of oxygen on a flow -through basis; (3) Aeration. A process of bringing about Intimate contact betwean air or high purity oxygen In a liquid by spraying, agitation or d1ffuslon;(3a) Extended Aeration. An activated sludge process utilizing a minimum hydraulic detention time of is hours. (4) Agriculturally managed site. Any site on which a crop is produced, managed. and harvested (Crop Includes grasses, grains, trees, etc.); (5) Air Stripping. A process by which the ammonium Ion Is first converted to dissolved ammonia (pH adjustment) with the ammonia then released to the atmosphere by physical means; or other similar processes which remove petroleum products such as benzene, toluene, and xyfene; (6) Carbon RageneratlorL The reger*ra0on of exhausted carbon by the use of a furnace to provide extremely high temperatures which volatilize and oxidize the absorbed Impurities; (7) Carbonaceous Stage. A stage of wastewater treatment designed to achieve `secondary' effluent limits; (8) Centrifuge. A mechanical device In which centrifugal force is used to separate solids from liquids or to separate liquids of different dens"r.!as; (9) Chemical Addition Systems- The addition of chemicals) to wastewater at an application point for purposes of improving solids removal, pH adjustment, alkalinity control, etc.; the capability to experiment with different chemicals and different application points to achleve a specific result will be ccnsrdered one system; the capability to add chamical(s) to dual units will be rated as one system; capability to add a chemical at a different application points for different purposes will result In the systems being rated as separate systems; (10) Chemical Sludge Conditioning. The addhlon of a chemical compound such as lime, ferric chloride, or a polymer to wet sludge to coalesce the mass prior to its application to a dewatering device; (11) C;osed Cycle Systems_ Use of holding ponds or holding tanks for containment of wastewater conta;ning Inorganic, non -toxic materials from sand, gravel, crushed stone or other similar operallons. Such systems shall carry a maximum of two points regardless of pumping facilhiss or any other appurtenances; (12) Combined Removal of Carbonaceous BOD and Nitrogenous Removal by Nitrification- A single stage system requlmd to achieve permit effluent limits on BOD and ammonia nitrogen within the same biological reactor, (13) DechlorinatlorL The partial or complete reduction of residual chlorine In a liquid by any chemical or physical process; (14) Denftrtficatlon Process_ The conversion of nitrate -nitrogen to nitrogen gas; (15) Electrodatysis. Process for removing Ionized salts tram water through the use of ion -selective Lon -exchange membranes; (16) Filler Press. A process operated mechanically for parifally dewalering sludge; (17) Foam Separation. The planned frothing of wastewater or wastewater effluent as a means of removing excessive amounts of detergent materials through the Introduction of air In the form of fine bubbles; also called loam fractionation; (18) Grit Rsmovai. The process of removing grit and other heavy mineral matter from wastewater; (18) Imhoff Tank. A deep two story wastewater tank consisting of an upper sedimentation chamber and a sower sludge digestion chamber. (20) Instrumented Flow Measurement. A device wh;ch indicates and records rate of liow; (21) Ion Exchange. A chemical process In which kits from two different molecules are exchanged-, (22) land appfication: (a) Sludge D+sposal. A Mal sludge disposal method by which wet sludge may be applied to land either by spraying on the surface or by subsurface injecti (I.e., chisel plow); [not applicable for types of sludge described In (11) of this Rulej; (b) Treated Effluent. The process of spraying treated wastewater onto a land area or other methods of application of wastewater onto a land area as a means of final disposal or treatment; (23) Microscreen A low speed, continuously back -washed, rotating drum filtor operating under gravity conditions as a polishing method for removing suspended solids from effluent; (24) Nitrification Process. The biochemical conversion of unoxidized nitrogen (ammonia and organic nitrogen) to oxidized nitrogen (usually nitrate); (25) Nitrogenous Stage. A separate stage of wastewater treatment designed for the specific purpose of converting ammonia nitrogen to nitrate nitrogen; (26) Phosphate Removal, Biological. The removal of phosphorus from wastewater by an oxWanoxic process designed to enhance luxury uptake of phosphorus by the microorganisms; (27) Polishing Pond. A holding pond following secondary treatment with sufficient deterdion time to allow settling of finely suspended scllds; (28) Post Aeration Aeration following corrvontionaf secondary treatment units to Increase effluent D.O. or for any other purpose; (29) Post Aeration. (Cascade) A polishing method by which dissolved oxygen Is added to the effluent by a nonmechanical, gravity means of flowing down a sends of steps or worry; The flow occurring across the steps or weirs moves in a fairly thin layer and the operation of the cascade requires no operator adjustment; thus, zero points are assigned even though this Is an essential stop to meeting the limits of the discharge permit,- (30) Powdered to Granular Activated Carbon Feed. A biophysical carbon process that utlifzes biological activity and organic absorption by using powdered or granular activated carbon; Virgin or regenerated carbon is feed control;ad Into the system; (31) PreaeraOon A tank constructed to provide aeration prior to primary treatment; (32) Preliminary Units, Unh operatlons in the treatment process, such as screening and comminution, that prepare the liquor for subsequent major operas#ors; (33) Industrial Pretreatment. (a) Pre-treatment Unit, Industrial. The conditioning of a waste at its source before discharge, to remove or to neutralize substances Injurious to sewers and treatment processes or to effect a partial reduction In load on the treatment process which is operated by the same governing body as the wastewater treatment plant being rated', b) Pre-treatment Program, Industrial - mast be a State or EPA required program to receive points on the rating sheet; (34) Primary Clarfliers. The first satlArsg tanks through which wastewater is passed In a treatment works for the purpose of removing settleable and suspended solids and BOO which Is associated with the solids; (25) Pumps. A11 Influent, effluent and In -plant pumps; (36) Radiation Disinfection or sterilization process utilizing devices emitting ultraviolet or gamma rays; (37) Reverse Osmosis. A treatment process In which a heavy contamlrtated liquid Is pressurized through a membrane forming nearly pure liquid free from suspended solids; (38) Rotating Biological Contactors. A fixed biclogical growth process In which wastewater flows through tanks In winch a series of partially submerged circular Surfaces are rotated; (39) Sand Filters: (a) Intermittent Blologlca3. Filtration of effluent following septic tanks, lagoons, or some other treatment process In which further biodecomposltlon is expected to produce desired effluents; Hydraulic loading rates on these flitors are computed In gpolac and have a resulting taw gprrVsl (less than one); b) Recirculating biolcgical - the same type of sand fitter as defined in Subparagraph (39) (a) Of this Rule with the added capability to recycle effluent back through the sand filter, (40) Sand or Mixed -Media Fillers. A polishng process by which effluent f its are achieved through a further reduction of suspended solids; (a) low rate — gravity, hydrauflcally loaded liltor with loading rates In the one to three gpmrsf range; (b) high rate — a pressure, hydraulically kaded fitter with loading rates In the five gpmisf range; At any rate, the loading rate will exceed three gprrVsf; (41) Secondary Clariliers. A tank which follows the biological unit of treatment plant and which has the purpose of removing sludges associated with the biological treatment units; (42) Separate Sludge Reaeretlon. A part of the contact stabilization process where the activated sludge is transferred to a tank and aerated before resuming it to the contact basin; (49) Septic Tank A single -story settling tank in which settled sludge Is In contact with the wastewater flowing through the tank; shall not be applicable for septic tank systems serving single family ros+dences having capacity of 2,000 gallons or 4ess which dscharge to a nitrification field; (44) Sludge Digestion. The process by which organic or volatile matter and sludge is gaff ad, liquefied mineralized or converted into more stable organic matter through the activity of living organisms, which includes aerated holding tanks; (45) Sludge Drying Beds. An area comprising natural or artfficial sayers of porous materta4s upon whlrh digested sewage sludge Is dried by drainage and evaporation; (4-6) Sludge Eiutriation. A process of sludge conditioning in which certain constituents are removed by successive washings cosh fresh water or plant effluent; (47) Sludge Gas Utlfization The process of using sewage gas for the purpose of heating buildings, driving engines, etc-; (45) Sludge Holding Tank (Aerated and Nonaerated). A tank utilized for small wastewater treatment plants not conlalning a digester In which sludge may be kept fresh, and supernatant withdrawn prior to a drying method (i.e. sludge drying beds); This may be done by adding a small amount of air slmpiy to keep the sludge fresh, but not necessarily an amount that would be required to achieve stabitlzaticn of organic matter. A nonaarated tank would simply be used to decant sludge prior to dowatering and would not allow long periods (several days of detention) without resulting odor problems; (49) Sludge Incinerators. A furnace designed to bum sludge and to remove all moisture and combustible materials and reduce the sludge to a sterile ash; (50) Sludge Stabilization (Chemical or Thermal}. A process to make treated sludge less odorous and putrescible, and to reduce the pathogenic organism content; This may be done by pH adjustment, chlorine dosing. or by heat treatment; (51) Sludge Thickener. A type of sedimentation tank in which the sludge Is permitted to settle and thicken through agitation and gravity; (52) Stabilization lagoon A type of oxidation lagoon In which biological oxidation of organic matter Is ofiected by natural transfer of oxygen to the water from air (not a polishing pond); (53) Sland-By Power Supply. On site or portable electrical generating oqulpment, (54) Static Screens. A stationary screen designed to remove solids, including non -biodegradable particulate (ffoalable solids, suspended solids and BOO reduction) from municipai and industrial wastewater treatment systems; (55) Tertiary Treatment. A stage of treatment following secondary wflich Is primarily for the purpose of effluent polishing; A settling lagoon or sand or coal fitter might be employed for this purpose; (56) Thermal Pollution Control Device. A device providing for the transfer of heat from a fluid flowing in tubes to another fluid outside the tubes, Or vice versa; or other means of regulating liquid temperatures; (57) Thermal Sludge Conditloner. A conditioning process by which heat is added for a protracted period of time to Improve the dewaterablifty of sludge by the sclubilizing and hydraullzing of the smaller and more highly hydrated sludge particles; (58) Toxic Matanals. Those wastes or cornWnatlors of wastes, including dlsease-causing agerts which after discharge and upon exposure, Ingastlon. Inhalatlon or assimilation Into any Organism, ofther directly from the environment or indirectly by Ingestlon through food chains, will cause death, dicaasa, behavloral abnormalities, rancor, genellc mutations, physlological malfunctlons (including malfunctions In reproduction) or physical deformations. In such organisms or their offspring; Toxic materials Include, by way of illustration and not limitation: lead, cadrrium, chromium, mercury, vanadium, arsenic, zinc, ortho-nflracNorobenzene (ONCE), poiychlorinatud blphenyls (PCBs) and dichbrodiphen)t trichioroethane (DDT); and any other materials that have or may hereafter be determined to have toxic properties-, (59) Trickling Filter. A biological treatment unit consisting of a material such as broken stone or rock over which wastewater Is distributed; A high rate trickling filter Is one which operated al between 10 and 30 mgd par acre. A low rate trickling filter is one which is designed to operate at one to lour mgd per acre' (60) Trickling Filter (Packed Tower). A plug flow type of operation In which wastewater flows down through successive layers of medla or tiftrate maleriat; Organic material Is removed continually by the active biological fixed y owth In each successive layer. This method may produce 'secondary' quality effluent, or may be adapted to produce a nitrified effluent; (61) Vacuum Ffter, Centrifuges, or Filter Presses. Devices which are designed to remove excess water from either dlgasled or undigested sludge prior to disposal or further treatment.