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HomeMy WebLinkAboutWQ0009064_Final Permit_19940627State of North Carolina Department of Environment, Health and Natural Resources Division of Environmental Management James B. Hunt, Jr., Governor Jonathan B. Howes, Secretary A. Preston Howard, Jr., P.E., Director June 27, 1994 Mr. Thomas H. Naylor R R 1, Box 1272A, Mt. Philo Road Charlotte, Vermont 05445 Dear Mr. Naylor: IN �5VA use A ID FE F10 Subject: Permit No. WQ0009064 Thomas H. Naylor Residence Single Family Wastewater Spray Irrigation Facility Orange County In accordance with your application received March 1, 1994, we are forwarding herewith Permit No. WQ0009064 dated June 27, 1994, to Mr. Thomas H. Naylor for the construction and operation of the subject single family wastewater treatment and spray irrigation facilities. This permit shall be effective from the date of issuance until May 31, 1999, and shall be subject to the conditions and limitations as specified therein. Please pay particular attention to the monitoring requirements 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 the 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. One set of approved plans and specifications is being forwarded to you. If you need additional information concerning this matter, please con ��&Jghn :Seymour at (919) 733-5083. Sincerely, A. Pres Howard, Jr.. P.'. cc: Orange County Health Department Raleigh Regional Office, Water Quality Central Office Groundwater Section Facilities Assessment Unit Craig B. Morgan & Associates, P.A. Consulting Engineers P.O. Box 29535, Raleigh, North Carolina 27626-0535 Telephone 919-733-5083 FAX 919-733-9919 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 SINGLE FAMILY SPRAY IRRIGATION 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 Mr. Thomas H. Naylor Orange County FOR THE construction and operation of a 480 GPD wastewater spray irrigation wastewater treatment and disposal system consisting of an existing 1,200 gallon baffled septic tank, an existing 1,200 gallon sand filter pump tank with a 20 to 25 gpm capacity pump, a minimum total of 420 ft2 dual subsurface sand filters, a tablet chlorinator, two 1,500 gallon storage/pump tanks (piped in series) with a 20 GPM irrigation pump, and a 13,500 ft2 spray irrigation area with eleven 2.2 gpm spray heads, and all associated piping, valves, controls, alarms, and appurtenances to serve the Naylor Residence, with no discharge of wastes to the surface waters, pursuant to the application received March 1, 1994, 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, 1999, and shall be subject to the following specified conditions and limitations: I. PERFORMANCE STANDARDS 1. Upon completion of construction and prior to operation of this permitted facility, a certification must be received from a professional engineer certifying that the permitted facility has been installed in accordance with this permit, the approved plans and specifications, and other supporting materials. Mail the Certification to the Water Quality Permits and Engineering Unit, P.O. Box 29535, Raleigh, NC 27626-0535. 2. The Raleigh Regional Office, telephone number 919/ 571-4700 shall be notified at least forty-eight (48) hours in advance of operation of the installed facilities so that an in -place inspection can be made. 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. 3. The spray irrigation facilities shall be effectively maintained and operated at all times so that there is no discharge to the surface waters, nor any contamination of ground waters which will render them unsatisfactory for normal use. In the event that the facilities fail to perform satisfactorily, including the creation of nuisance conditions or failure of the irrigation area to adequately assimilate the wastewater, the Permittee shall take immediate corrective actions including those actions that may be required by the Division of Environmental Management, such as the construction of additional or replacement wastewater treatment and disposal facilities. 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 facility. 5. The sand media of the subsurface sand filter(s) must comply with the Division's sand specifications. The engineer's certification will serve as evidence that these specifications have been met. 6. A leakage test shall be performed on the septic tank and dosing tank to insure that any exfiltration occurs at a rate which does not exceed twenty (20) gallons per twenty-four (24) hours per 1,000 gallons of tank capacity. The engineer's certification will serve as proof of compliance with this condition. 7. If excavation into bedrock is required for the installation of the septic tank or sand filter, the pit shall be lined with a 10 mil synthetic liner. 8. The residuals generated from these treatment facilities must be disposed in accordance with General Statute 143-215.1 and in a manner approved by the North Carolina Division of Environmental Management. 9. Diversion or bypassing of the untreated wastewater from the treatment facilities is prohibited. 10. The following buffers shall be maintained, with the only buffer variances being as agreed to in the Adjacent Landowner Agreements, that are stated as part of this permit: a)*400 feet between wetted area and any residence or places of public assembly under separate ownership*, b)* 150 feet between wetted area and property lines*, c) 100 feet between wetted area and wells, d) 100 feet between wetted area and drainageways or surface water bodies, e) 50 feet between wetted area and public right of ways, f) 100 feet between treatment/storage units and any wells, and g) 50 feet between treatment units and property lines. * Due to hardship circumstances, specific buffer variances are granted as long as existing and/or planted vegetation buffers are maintained between the sprayfield and adjoining homes and property lines. Three existing houses will be within 400 feet of the subject sprayfield. These houses will be at distances of 258, 265, and 275 feet. The subject sprayfield is to be 10 feet from the Duke Forest property line. Waivers have been signed by the effected property owners and are considered part of this permit. H. OPERATION AND MAINTENANCE REQUIREMENTS 1. The facilities shall be properly maintained and operated at all times. 2. A suitable vegetative cover of the spray field shall be maintained. 3. Irrigation shall not be performed during inclement weather or when the ground is in a condition that will cause runoff. 4. Adequate measures shall be taken to prevent wastewater runoff from the spray field. 5. The application rate shall not exceed 0.40 inches per week at an instantaneous application rate not to exceed 0.20 inches per hour. 6. The facilities shall be effectively maintained and operated as a non -discharge system to prevent the discharge of any wastewater resulting from the operation of this facility. 7. No type of wastewater other than that from the Naylor Residence shall be sprayed onto the irrigation area. 2 8. In the event that the sprinkler heads fail to achieve the design diameter of 45 feet due to obstructions, the obstructions shall be removed or the sprinkler heads shall be raised and supported to such height that the design diameter is achieved. 9. No traffic or equipment shall be allowed on the disposal area except while installation occurs or while normal maintenance is being performed. 10. The Permittee is responsible for the operation and maintenance of the entire treatment and disposal system including, but not limited to, the following items: a. The septic tank shall be checked annually and pumped out as needed. b. The tablet chlorinator shall be checked every week. Tablets shall be added so as to provide proper chlorination. c. The storage, pump, and alarm systems shall be inspected weekly. The scum layer shall be removed at the same interval as the septic tank is cleaned out. d. The spray system shall be inspected weekly to make certain of the sprayers proper operation, that the vegetative growth allows a proper spray pattern, that the soil is assimilating the disposed treated wastewater with no surface runoff, and that no objectionable odors are being generated. III. MONITORING AND REPORTIN,C REQUIREMENTS 1. Any monitoring deemed necessary by the Division of Environmental Management to insure surface and ground water protection will be established and an acceptable sampling reporting schedule shall be followed. 2. The Permittee shall maintain records of all maintenance performed on the system and irrigation area, as required in Condition II.10 for a minimum of five years. This information shall be provided to the Division of Environmental Management upon request. 3. Noncompliance Notification: The Permittee shall report by telephone to the Raleigh Regional Office, telephone number 919/ 571-4700 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 process unit failure, due to known or unknown reasons, that renders the facility incapable of adequate wastewater treatment, such as mechanical or electrical failures of pumps, spray heads, etc.; or b. Any failure of a pumping station or treatment facility resulting in a by-pass directly to receiving waters without treatment of all or any portion of the influent to such station or facility. Persons reporting such occurrences by telephone shall also file a written report in letter form within 15 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. INSPECTIONS 1. Adequate inspection, maintenance, and cleaning shall be provided by the Permittee to insure proper operation of the subject facilities. 3 2. Any duly authorized officer, employee, or representative of the Division of Environmental Management may, upon presentation of credentials, enter and inspect any property, premises or place on or related to the disposal 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 maintained under the terms and conditions of this permit, and may obtain samples of groundwater, surface water, or leachate. V . GENERAL CONDITIONS 1. This permit shall become voidable unless the facilities are constructed in accordance with the conditions of this permit, the approved plans and specifications, and other supporting data. 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 transferable. In the event there is a desire for the facilities to change ownership, or there is a name change of the Permittee, a formal permit request must be submitted to the Division of Environmental Management 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. Upon the availability of a municipal or regional sewerage collection system, the subject wastewater treatment facilities shall be abandoned and all wastewater discharged into the municipal or regional sewerage system. 5. The spray irrigation field shall be fenced with at least a two strand wire fence. 6. Failure to abide by the conditions and limitations contained in this permit may subject the Permittee to an enforcement action by the Division of Environmental Management in accordance with North Carolina General Statute 143-215.6(a) to 143-215.6(c). 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. 8. This permit may be revoked if the Permittee fails to abide by the conditions of the "Operation and Maintenance Agreement" previously signed by the Permittee. 9. A set of approved plans and specifications for the subject project must be retained by the Penmittee for the life of the project. 10. 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. Permit issued this the 27th day of June, 1994 NORTH CAROLINA ENVIRONMENTAL MANAGEMENT COMMISSION 62—�L, �,n 0 z"- /I - A. Preston ward, Jr., P. ., Director Division of Efivironmental Management By Authority of the Environmental Management Commission Permit Number WQ0009064 4 Permit No. WQ0009064 June 27, 1994 ENGINEER'S CERTIFICATION I, , as a duly registered Professional Engineer in the State of North Carolina, having been authorized to observe (periodically, weekly, full titre) the construction of the project, Project Name Location for the Permittee hereby state that, to the best of my abilities, due care and diligence was used in the observation of the construction such that the construction was observed to be built within substantial compliance and intent of this permit, the approved plans and specifications, and other supporting materials. Signature Registration No. Date 5 OPERATION AND MAINTENANCE AGREEMENT FOR THE DIVISION OF ENVIRONMENTAL MANAGEMENT Name: T# ol-fAf // AlA xe vR Address: 3 0 0 A-V /VC - State: /VC ZIP: Single Family Residence Wastewater Treatment System Final Disposal by Spray Irrigation Permit No. (TO BE COMPLETED BY DEM) , D AA'clCounty I agree to operate and maintain the wastewater treatment system as follows: I . The Permittee is responsible for the operation and maintenance of the entire treatment and disposal system including, but not limited to, the following items: a. The septic tank shall be checked every six (6) months and pumped out as required. b. The tablet chlorinator shall be checked every week until the actual usage rate is established and thence on a monthly basis. Tablets shall be added so as to provide proper chlorination. C. The storage system, pump system, and alarm system shall be inspected monthly. The scum layer shall be removed at the same interval as the septic tank is cleaned out. d. The spray system shall be inspected monthly to make certain of the sprayers proper operation, that the vegetative growth allows proper spray patterns, that the soil is absorbing the disposed treated wastewater with no surface runoff, and that no objectionable odors are being generated. 2. Failure of the Permittee to properly operate this system is subject to a penalty up to $10,000 per day. 3. Failure to meet permit conditions or violation of the State's surface or groundwater reg�,,la ions will require cessation of occupancy of the residence. I understand that failure to comply with these conditions along with the permit conditions may result in voiding the permit. Signature: Date: l3, r �� Notary Seal Notary Signature: <: 32`'.Q Date:-%J.,=.9'7 U5G5 MAP y'' S� CHAPEL HILL QUADRANGLE NORTH CAROLINA 7.5 MINUTE SERIES (TOPOGRAPHIC). 679 6&0 79 ° 00' _� - 36 ° 00' 3985 3983 610 000 FEET THOMAS H. NAYLOR PROPERTY 300 MIMOSA DRIVE, CHAPEL HILL, NC EXHIBIT C RATING SCALE FOR CLASSIFICATION OF pWATER POLLUTION CONTROL SYSTEMS Name 'of Facility: I ►7avka5 Not L, le., ReS-; de iCe 1 r,1-51C fl^ly Owner or Contact Person: 7 x 4W sz /arr Mailing Address: •_ -� far 1 ?�72 . �� iA. . l>' d .. �`h�r to `��Vt 05'tf#5 County: Telephone: Present Classification: New Facility z Existing Facility NPI)ES Per. No. NCOO Nondisc. Per. No.*R!RE p64Health Dept. Per. Na - Rated by: _ 7gAw r-t0zmP&t,, Telephone: Date; 9(" Reviewed by: Health Dept. Telephone: flegional Office Telephone: Central Office Telephone: ORC: Grade; Telephone: Check Classification's): Subsurface Spray Irrigation LandApplication Wastewater Classification: (Circle One)61, ll ill. IV Total Points:— — - -• r • •• -• • • �-0 • \� / �1� ti i •:il � : lu ►1 ��i 1� ia� • :S . IEl � . :►► � u. mil. 7 J�. SU8SURFACE CLASSIFICATK)N (check all units that apply) I. —septic tanks 2. pump tanks 3. siphon or pump -dosing systems 4. sand fillers 5, grease lraphnlercepior 6. oil/water separators 7. subsurface treatment and disposal aravily rsressure SPRAY IRRIGATION CLASSIFICATION • . (check all units that apply) 1. - preliminary treatment {definition no. 32 ) 2. lagoons 3._V septic tanks 4.�,- pump tanks 5. pumps 6.),,_sand fillers 7, grease trapAnterceptor 8. ^_oillwa€er separators 9. V disinfection 10. chemical addition for nutrient/algae control 11­L1 _spray irrigation of wastewater Pretreatment of wastewater in excess of these components shall be rated using the point rating system and will require an operator with an appropriate dual certification, LAND APPLICATION/RESIDUALS CLASSIFICATION (Applies only to permit holder) 1. Land application of biosofids, residuals or contaminated soils on a designated site. WASTEWATER TREATMENT FACILITY CLASSIFICATION The following systems shall be assigned a Class I classification, unless the flow is 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 Oillwaier Separator Systems consisting only of physical separation, pumps and disposal; 2. Septic Tank/Sand Filter Systems consisting only of septic tanks, dosing apparatus, pumps,sand fillers, 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 Remedialion Systems consisting only of pumps, air -stripping, carbon adsorption, disinfection and disposal; 6. Fish farms 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-lamily discharging systems with the. exception of Aerobic Treatment Units, will be classified it permilled after July,1,.1993 or if upon inspection by the Division, It is, found that the system is not being adequately operated or maintained.,' Such systems will be notified of the:classilicalion or reclassilication by the Commission. -in writing, The following scale is used for rating wastewater treatment facilities: (circle appropriate points) (2) (3) (4) (5) (6) REM POINTS Industrial Pretreatment Units or Industrlai Pretreatment Program (sea definition No. 33)...................................................4' DF iGN PLOW OF PLANT IN gpd (Trot applicable to non-oonlamlnated cooling waters, sludge handling faciiities for water purification plants, totally closed cycle systen's(sae delinhlon No. 11), and facilities consisting only of Item (4)(d) or Items (4)(d) and (11)(d)] 0 •.20,000........................................................................................ ........................._............................. 20,001 - 50,0w... ..................... :..........................................................:...::...........................:.................2 50.001 - .100.000 ........................ :........................................................... ................................................ .3 100,001 250,000 ................................:......................................I................-..........................................4 250,001 - 500,000. ....................................................................•.:........,.....,................................:..........5 500,001 - 1.000,000.......... :............:...:..............-...............-...................,.........•.......................................a 1,000,001 - 2,000,000.................. .......................................... ................................................................ 10 2.000,001 (and up) rate 1 point additional for each 200,000 gpd capacity up to a rnaxlmumof........................................................................3 Design Flow (gpd) 0 PRELiMVARY UNITS/PROCESSES (see dertndion No.32) (a) Bar Screens.•...................................:.................................:..................-....................................................1 or (b) Mech'anical-screens, Static Screens or Comminuting Devices..........................................................................2 (c) Grit Removal......................................................... :..................... ............ or (d) MechanicalorAeraledGrit Removal ............................................................ ........................ ....... .............. .....2 (e) . Flow Measuring Device ......................... :......................................................................................................1 or (f) Instrumented Flow Measurement.............................................................................:..............•...................2 {g) Preaerallon............... ........ ..... .......... ............. ........ ........... .......................... .............................................. .2 {h] Inlluare Row Equalization ............. .... ................ ................. .............. ........ :....................... I.......................... (1) Grease or Oil Separators - Gravity. ........................... ..................................................................................... 2 Mechanical........................................................................................ ...............:............I.... I.......................3 DissolvedAir Flotation ........................................... .................... ................................................................. 8 I)} Prechlorination................................................................:.........................................................................5 PRIMARY TREATMENT UNITS'PROCESSES (a) Septic Tank (see definition No. 43)........... ...................................................... ............................... .......... :� (b} Imhoff Tank ............ ...................................................................................................................................5 (c) Primary Clarifiers ............................................ ................. •................. ........ ................................ I .................... 5 (d) Settling Ponds or Settling Tanks for Inorganic Nan -toxic Materials (sludge haridling lacMlles for water purification plants, sand, gravel, stone, and other mining operations except recreational activities such as gem or gold! mining).......................................................................................... ............... SECONDARY TREATMENTLNU&PROCESSES (a) Carbonaceous Stage (1) Aarailon-High Purity Oxygen System ....................... ........................................................20 DlHusadAir System...............................................................................................:.......1 0. Mechanical Air System (fixed, floating or rotor)..................................................................8 Separate Sludge Raaerrallon.............................................................................................3 (II) TdckJng Filler HighRate....................•..................................................................................................7 StandardRate ............. ......................... .......................................................................... 5 PackedTower... ........ .................. ........... ................................ ............................... 5 . (iii) Biological Aerated Filler or Aerated BioloBoat Filler ................................... ............... :........•............................ ,.................... 10 (Iv) Aerated Lagoons ................ .................................................................................... ....... 10 (v) Rotating biological Contactors ...... .......... .................. ................. ,-...----...........................19, (VI) Sand -Filters -intermittent biological............................................................................... 10 ' Recirculating blologIcal..................................................................................................... 3 (vii) Slabilization Lagoons ....... ....... ............ ..... ...:............... ....:....... ............................ ......... ....5 (viii) Gardiar................................................. ............................................... ........................... 5 (ix), Single slags system for combined carbonaceous removal of BOD and nitrogenous removal by nitrification (see dellnitian No. 12)(Poinls for this item have 10 be In addition to Items (5)(a)(i) through (5)(a)(vlil), utilizing the extended aeration process (see definition N0.3a)...........................................2 utilizing other than the extended aeration process ........... .......................... ........................ 8 (x) Nutrient additions to enhance BOO removal .................................. .......:............................ 5 (xi) Biological Culture (".Super Bugs")addiUon............. ................... ....................... I—— ............. 5 (b) - Nitrogenous Stage I1) Aeralion : High Purity Oxygen System.............................................................................20 DiffusedAir Sys[em............................... ..:.......... ......•....... ..... ........ ..... ................. ........... 1 0 Mechanical Air System (fixed, dioaling or rotor).. ....................... ............... I I ........ I .............. 8 Separate Sludge Reaeralion.............................................................................................3 ...(ii) Trickling Filler -High Rate .......................... ............................ ................ ................... .......... 7 StandardRate...........:......................................................,...............................:.............6 PackedTower...................................................................._..........................................5 (iii) - Biological Aerated Filter or Aerated Biological Filler.............................................................10 (IV) Rotating Etiological Conlactors..............:....:.............................................:....................1 0 (v) Sand Filter - intermittent biological .................................... .......... ................. ............... .....2 Recirculatingbiological.............................................................. ,...................................... 3 (vi) Clarfler.:...............................'.......................:...:::.............................................................5 TERTIARY OR ADVANCED TAEATM ENT LNUSrPrOCESSES (a) Activated Carbon Beds without carbon regeneration ......................... ............................................5 with carbon regeneration ............... :...:.:............................ ............... '....:........... I .......................... 15. (b]` Powdered or GranularAcWaiad Carbon Feed - without 'carbonregeneration.............. :...:....................... ....:................ ........... ..................... .5 with carbon regeneralion................... :.......:..•........-.................. ..-....................... ................ 15 (c) .' Air -stripping .... ..-. ..roces....................:...........:.:..,......-.........................................:.......................:.....:..:............5 - (d):: Daniiriiicit€on Ps...........:;.......:................:..........................-.............................. ......... 10 (a) Eleclrodialysis.........................................................................................................::. ............ :............... ..S (f) Foam Separation.......................................................................................................................................5 (0) Ion Exchanga................ :............................. .............................. .................................... ....................... ....,.5 (h) Land Application of Treated Effluent (see definition No. 22b) (not applicable for sand, gravel, stone and other similar mining operations) by high rate Inlillralion........ ......... ...................... :.:.....:.....4 (I) Mlcroscreens.......................................... .:.......................... ....................................................................... .5 O) Phosphorous Removal by Biological Processes (See definition No. 26).........................................................20 (k) Polishing Ponds - without aeraflon......................... ....... ............. .............................................. ............... :....... With aeration .............. ............................................................... -........... E..;....:.5. --, (I) Post Aeration - cascade ...................:..........................-........:......................-........................:................:.....0 diffused or machanlcM............................................--..........:................................2 (m) Reverse Osmosis. ................. .............................................................................................................. I ....... 5 (n) Sand or Mixed -Media Fllters - low rate .................. ............................................................. :........... ...............2 high rate' ................. (o) Treatment processes for removal o1 metal or cyanide ............... :................................................................... 1 5 N. treatment processes for removal of toxic materials other than metal or cyanide..............................................1 5 .. (7) SfJJOGETREATMENT (a) Sludge Digestion 'Tank - Healed ...................................................... ..... .......... ........................................... 10' Aerobic 5 Unhealed 3 (b) Sludge Stabilization (chemical or.thermal).......................:..:..........................................:..........................:..5' (c) Sludge Drying Bads - Gravity ................. ......................... ......................... .................... ..:......... ......... ..:......:.. 2 . Vacuum Assisted................................................................................................:.......................................5 (d) Sludge Elutriallon.....................................................................................................................................5 (a) Sludge Conditioner (chemical or thermal).....................................................................................................6 (1) Sludge Thickener(gravily)..........................................................................................................................5 ( g) Dissolved Air Flotation Unit (not applicable to a unit raked as(3)(I)1......................................................:......8 (h) Sludge. Gas Utilization (Including gas storage)......::.....:.........................•....................................,.........:......2 (f) Sludge Holding Tank - Aerated ..................... ....................................... :....... ................................................. 5 Nori aeraled... ........................ ... .......................... ............ ........... ............................... .................................. 2 O) Sludge Incinerator (not Including activated carbon regeneration) ............................................. ......... ......... 10 {kJ Vacuum Titer, Cenl61ugo, or Fllior Press or other similar dewatering devices...................................................10 (8) RESIDUALS UTILIZATIOWDISPOSAL (induding 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 or landfill permit...............................................................................................................2 c Dedicated Landlili burial by the parmlitse of the wastewater treatment facility { s) Dtsrir=ECT�ty � . (a) Chlorination..............................................................:......................I............ ..... S (b) Dechlorinalion..........................................................................................................................................5 (c) Ozone.......................................................................................................................................................5 (d) Radiation ............ :................... ..............,........................................-..................-...:............-..-...........I.......5 (10) CHEMICAL ADWTION SYSTEM(S) ( see definition No.9) {not applicable to chemical additions rated as item - (3)(j), (5)(a)(A), (6)(a), (6)(b), (7)(b), (7)(e), (9a), (9)(b) or (9)(c) 5 points each: List......................................................................................................................................5 ....................................................................... I .............. ..-................. ............... ......................................................:.................................................... ....... I ....... is .............................:.......................:............................................. ........... .......5 (t 1) MiSCEL(ANEOUS UNITSIPROCESSES (a) Holding Ponds, bolding 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 for domestic wastewater.............................................................. :.......................... 4 (b) Effluent Flow Equalization (not applicable to storage basins which are Inherent in land application systems) ...................................... ......................................................... ............. ................... I., ............. ...2 (C) Stage Discharge (not applicable to storage basins inherent in land application systems)..................................5 - (d) Pumps ............................... ..................................................................................................................... a (a) Stand -By Power Supply.............................................................................................................................3 (I) Thermal Pollution Control Device ............................ :................................... .............. ........ :............... -.... ..3 TOTAL POINTS............................................................. .............. � Class...................... ............. .......... .... ....... ......... .............. ............................ 5-25 Points Class 11.........................................:..........-.............-.......... ...26-50 Points ......................... CtassIII.......... ......... ......... ............................................................................ 51-65 Points CIassIV.......................................... .................. .......... : .................. :.............66-Up Points Facilities having a rating of one through lour points, Inclusive, do not require a certified operator. Facilities having an activated sludge process will be assigned a minimum classilicalion of Class 11. Facflilies having Iroalmant processes for the removal of metal or cyanide will be assigned a minimum cfassificalfon of Class 11. Facitilies having treatment processes for the biological removal of phosphorus wN be assigned a minimum ciassilication of Class Ill ,0004 0CFINITIOHS - - The following defiry Gans shall apply tirougtwut this Subchapter, - - (1) Activaled Carbon Bads. A physicatrchemical method for reducing solubleorganicmalarial from waslewaler Wr enl; The column -type beds used in Lets method will have a flow rate varying from Iwo to 0ght gallons per minors per square look and be oit hex vp4ow or dosrnfiow carbon bads._. Carbon may or may not be regenerated on the wastewater lrealmGak plant site; - - - 12) Aerated 4agoons. A basin In which all solids are maintained in suspension and by which biological oxida Bon or organic matter Is'jeduced through arlilicially accelerated _ transfer of oxygen on a Ilow-%trough basis; - 13) Aeration. A process of btinging-about Intimate contact between air or high purify oxygen in a liquid by spraying, aghation or dillusion;t3a) Eslended Aeration.. An - activated sludge process utilizing a rNH=m hydratAfc attention time of 18 hours- - - - - - - (4) Agriculturally managed site. My site orh which a crop Ts produced, -managed, and harvested (Crop Includes grasses, grains, trees, sic.); , (5) Air Stripping..A process by which the ammontun ion is first converted to dssolved ammonia {pH a6,uwtment) with no arnenorla then roleased to. the ahnosphera by physical means; or other slmlar processes which rairwvo petrdeurn'ptoducts such as benzene, toluene, and xylehe; - - - (6) Carbon Hegeneratron. The regenwa0an of exhausted carbon by the rise of a furnace to provide extremely high tmper alsaes which vdatiezo and oxidize the absorbed . impts'ities: - .. _ - (7) Carbonaceous Stage,, A stage of wastewater treatment designed to achieve -secondary' efeuent limits' - - - - "(8) Ceneilvge. A mechinical device in which centrilugal lace is used to separate solids from liquids O' Cto separste liquids ol-dillorom donxsioas;,�- - (e) Chemical Addlion Sysloms- Tito addlion of chemlcai(a) to waslawaler at anapplicalion POW tar purposes of improving solids romoval, pFi adp stment, alkalinity control, etc.: the capability 16 aaporimeni with &K.aronl cherricals and.differeni application points to achievo a, specific' result wdl bo'considerod one s)-A":,tho capability to add - cjiendcaf{s) to dual urils will be rated as one system; capabliily 10 add a chemcal at a d ilwont appricalien potnui for different purposes will result In the systems being rated as separate systems; (to) C7)arrical Sludge Conditiorxrg- The addition of a chemical compound such as -lima, ferric chloride, w a polymer to wet r}udgs to coalesce the mass prior to Its applicatlon So a dewalering device; (It) Closed Cycle Systems- Use of holcFrtg ponds or holding tari%m for contalnmen; of waslahvalw Containing Inorganic, non-taxlc materials from sand, gravel; crushed Slone or other-sTmftar operations. Such systems shall carry a maximum of two points regardless ofpumpingfacilities or any other eppununance$; (;z) Combined Removal of Carbonacootus BOO and NiVogonous Removal by Ritrificalion• A single stage system regU(Od fo achieve permit ohluonl limits ex) BOO and ammoella rrlrogon within file came biological ieaclor; - - - - - (13) Dechlorination. The partiaf or complete reduction of.ras€dual chlorine In a liq.rid.by anychemicalor physical process; - (14) Deritrificatton Process, The cornorsio_n of nitralo-nitrogen to'rilrogon gas; =- - - - ' (l5) Elociiadia4yslc. Process for iemWW Iodized sails from water ;!Tough the use of forr•solpctive lon•oxchangg membranes- - - (sil) Filler Press. A`pfocesc oporaled-.mecharicany for partially dewaiaring sludga;- (17) Foam -Separation. The planned frothing of wastewater or wastewater oMoarA as a means of removing excessive amounts of detergent materials through the introduction aF airin-l}he form of fine bubbles; also called foam fractionation; (18) GrIt:R0movaL- The process -ol removing grit and oll-w heavy rrineral mantic horn wastewater; - - - (14) In-haff-Tank._ A doop two story wastewater -lank consisting of an.rppercedimentation chamber and a lower $fudge digestion chambeC, - (20) instmCrierhted now 14e0stremenL. A device which indicates and records rate of now; (21) Ion Exchange. -A chemical process In which lorrs from tiro dilw9nl mdecxies are exchanged; - (22) Land -application: ..:. :. - - (a) Sludga Disposal. A final sludge disposal method by which wet sludge may be applied to land either by spraying on lhhe surface or by subsurface. iryaclion (i.e.. ciisei plow); (not applicable for types of Sludge described in (11) of this Rttoj; (b) Treated Effluer<t The process of splaying treated wastewater onto- a land area, or other methods of application of wastewater onto a land area as a moans of final disposal ar treatment; (23) Microscreon. A low speed, continuously back•wastted, rotating drum filter operating under g-.AMty condcrions as a polishing method for removing suspended solids from eluenl;. (24) Nitrification Process. The biochemical conversion of unoxidzed nitrogen (ammonia and organic rilrogon) to oxidized r>ilrogon (vsually nitrate); {25) Nitrogenous Stage. A teparale claga of wastewater treatment designed For the spadlic ptzpose of converting ammoria ritrogon to nitrate, nitrogen; (26) Phosphate. Removal, Biological. The. 'removal of phosphorus from wastewater by an 0xlc12noxic ptocess d90"d to enhance luxrxy uptake of phosphorus by the microorg ririls ms; (27) Polishing Pond, A holding pond following secondary treatment wlth sufficient detention time to allow salding of finely suspended solids; (28) Post Aeration. AeralIon following conventional secondary treatmsnl uriLs to Increase effluent D.O, or ror any other purpose; (29) Post Aaradon. (Cascade) A polishing method by which dissolved oxygen Is added to the'effitionl by a noinhecharical, gravity means of IlovAng down a series of steps or weirs; The rrnv Dcctrring across the slops cc weirs moves In a Jsiliy li'in layer and the operation of the cascade requires no operator adjustmenl; thus, zero points are assigned even though this'€s an essential slop, to meeting the limits of the discharge permit; (30) Powdosod to Granular Activated ;Carbon Feod. A Biophysical carbon process that utlizas,biological activity and organic absorption by using powdered or granular activated carbon; Virgin or regenerated carbon is teed conlrofled Into the system; - - (31) Preaeration, A tack constructed to provide aeration prior to primary treatmeni; (32) Preliminary Urils, Unit operations in the treatment process, Such as sc'teening and comrriinutiori, that prepare the liquor for subsequant major operations: (33) Industrial Pretreatment. (a) Pre-troatmonl Uri!, lnduslrlal- The condtioring of A. waste at its source before discharge, to remove Or to neutralize subslances Injurious to sewers and veatrnent processes or to effect a partial reduction In load on the tr'eatmertl process which Is operated by rite same governing body as the wastewater treatment plant being rated; b) Pre-trealrnanl Program, industrial - must be a State or EPA required program to receive points an the rating shoot; - (34) Primary Clarifiers. The first settling tanks through which wastewater is passed in a Veatmant works for the purpose of removing seltieabla and suspended solids and BOO which is associated with the solids; (35) Pumps- All Infivanl, efituenl and In•planl punps; (36) Radiation. Disieilection or sterilization process VbIlzing devices emitting u€traviolel or gamma rays; (37) Reverse Osmosis, A leatment process In which a heavy conlarrinaled Hod is pressurized tsyothgh a membrane forming nearly. pure liquid free from suspended solids; (39) Rotating Biological _Contractors. A lixed biological growth process in which wastewater Aows Nough tanks in which a sefhes of partially submerged circular surfaces are rotated- - - - - (39) Sand Fillers: (a) InterrTitIw9 Biological, Filtration of effluent following septic tanks, lagocris, or some Other lrealmonl process in which Fu-ther biodecomposltion is expected to produce desired effluents; Hydrat4c loading rates on these fillers are computed ln'gpolac and have a resulting low gpn✓sl {lass than one); - b) Recirculating biologicaE - the same type of sand filter as defined in Subparagraph (39) (a) of this Rule with duo added capability to recycle effluent back tn-vugh the sand lifter; (40) Sand or Mixed-Madia Fillers. A polishing process by which effluent Hails are achieved through a hither 7educ6en ai suspended solids•: (a) low rate -• gravity, hydraulically loaded filter with loading rates In the one to three gpmrsf rangy; (b) high rate -- a presvxo, hydcauficalty loaded filter with baring rates in Cue Five gpm/sf range; At any rate, the loading rate will exceed three, gpnvsf; (41) Secondary Clarifiers. A lank which follows the biological unit of treatment plant and wHch has the purpose of rornoving sludges associated with the biological arealmenl units- - - (42) Separate Sludge Reaeration. A pars of the contact stabilization process vhsre the activated sludge Is transferred to a Lznk and aerated before returning it to the contact basin; (43) Septic Tarn. A single -story settling tank In which settled sludge Is in contact with ;use wastewater flawing through the lank; shall no[ be applicable for septic lank systems serv€rtg Single. family residences having capacity o1,2,000 gallons or lass which discharge to a nitrification field; (44) Sludge .Digestion. The process by which organic of volatile matter and sludge is gasified, #iquefied, mineralized or converted into more stable organic matter trough ;he activity'of.living argarisms, which Includes aerated holding tanks; (45) Sludge Drying Beds. An area comprising natural or artihcfal layers of porous materials upon which digested sewage sludge is dried by drainage and evapoafioo; (46) Sludge ElutriaGon. A procass of sludge conditioning in which certain corsifuonts are removed by successive washings with fresh water or plant effluent; (47) SkKge Gas Utilization. The process of using sewage gas for the purpose of heating buildings, dying engirios, etc.; (48) 5;uege Holding Tank (Aerated and Flonaerated). A lark utilized for smali wastewater treatment plants rwl conlairing a dgeslarin which sludge may be kept fresh, and supernatant withdrawn prior to a.drying rnothod (i.e. sludge drying beds); THz may be done by adding a small amount of air sirnply to keep ttw sludge Iresh, but not necosswily an arnouil that woUd be raquired to achieve stabilization of organic rnatiar. A nonaeraled Iznk would simply be used to decant sludge prior to dewatering and would not allow long periods (several days of detention) without resulting odor problems; (49) Sludgo Incinaralws. A hrnace dosigriod to bum sludga and to fsmove all moisture and combustible materials and reduce the sludge- to a sterile asks; (50) Sludge Stabilization {Chemical a Thermal). A process to make boated sludge less odorous and putrascible, and to reduce the pathogenic organli n contonl: This may be Done by, psi adustrnonl, chhlorino dosing, oc by heat treatment; ' (51) Sludge Thickener. A type of sedimentation tank In which the sludge IS pear tad to settle and Uiickon througfx agitation and gravity; - - - (52) Stabilization Lagoon. A type of oxidation lagoon in which biological oxidation oI &garic.matter is affected by natural transfer of oxygen to Iho water from air (not a polishing pond); - - . - - - (53) Stand•By Power Supply, On.silo DC pollable electrical generating aquprr*rii:' - - (54) Static Screens. A stalionary screen designed in romove solids, including non-biodo7adablo,parliaRaie (Doalabla solids, suspended solids and'BOD reduction),from _mulicipal and indvstiial wastewater treatment systems: - (55) Tertiary Treatment. , A stage of treatment lollovAng secondary which is primarily to the puxpose of effluent pdishfng:.A settling lagoonorsand or coal filter fright be s ampfoyed for this purposo; - - - - (56) Thormat Pollution Control Device. A device pfoviding for the transfer of Nat hom,a nuid blowing In lobes to anothor Auld outside the tubes,- or vice versa; u olher rreans of 7agulaling livid. lomperahuses, (57) Thermal Sludge Conditio'hor. A_ condtioning process by which -heat is adder for .a protracted period of lime to improve the dewalerabinty of sludge by the so;vbili Ti rhg and hydkau><€Ying'ol the smaller and moo highly hydraEed -sludge ¢ariides; ..;' - - - - � '� � -" - -.' - - _- - (59) toxic Moterials. Those wastes or combinations of wastes, including diseasa-caustfg agents.which'affor discharge:and upon exposure, ingaslion, inhalaiiorl u assinitalion into any o,-garvsm, eilho! directly from the environment or indiDcGy by ingestion Csrough toed chains, will cause den{h,.disease,- beha.vlora€ abnormafilias, rancor, gonoticmutations, pheysiologcal, malhrrxlions (including. mallurxtiarhsin raproduxtion)-or-physical;deformations, In �iueh.orgarssmso ttioirol(spri7oxic.'malerials includo, by way of iltusiration and rat limitation: lead. cadmium, chromiurn;wmercury`vanadtim'--'arsenic; zinc, orCio•nitro-chittirobenzona,(QNCB), polychlorinated -(PCBs) and dichtoo'dphenyl Irichioroelhane {DDT); and any 'odhor materials Ifni havo'o. may hareafte l;be dalarrrrned to have toxic: properoos, - (59) Trickling GfboC i. blolcgical Imalmont unit consisting of a-malorial such as brokbn stone or rocY. Doer which waslewalor is. cSstribuilad; A hygh a lric kling'l, tar. is. ono' +^'Ch op oraled at bovrean Fo- and 30 mgd per acre. -•A fo>v race 4icklira Rhor is a"w wridh is do signod.4o operate al ern to lots mgd per acre; - - - 7ricklin9 Filter (Packed Tgwuf). A plug Acw typo of operation in which was or. tkovrs down liraugh _successive IayorY of media -or Gltralo malenal;`Orga c mAlarral' :.is removed coniirxrattyby lho-actiya biological Axod.growih in'oadt successw'C­i3j er............. -.,............. 71is madhod may prodako -secondary- quality alauonl, a mr,�r bo e$ap 2 to ` - 'ptouUco,i'.rilrllio.d 01lunl5l- (61} \'acu.xn F-tile;. Cczo ifugos- ix >-dlar Presses.. Devices which are,b7 s,�=o .� romavopzcuss water born oilhw rSgasea0 a und'gesiod $ludg-li'ptiorla diso .zk or lvrlhor IroaEmon:.