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HomeMy WebLinkAboutNC0060755_Wasteload Allocation_19910612NPDES WASTE LOAD ALLOCATION PERMIT NO.: NC0060755 PERMITTEE NAME: Carolina Water Service, Inc. of N.C. / Facility Status: Existing 5&>0LGUXX-) F3DIUls10�'�l Pen -nit Status: Renewal Major Pipe No.: 001 Minor -q Design Capacity: 0.009 MGD Domestic (% of Flow): 100 % Industrial (% of Flow): 0 % Comments: no compliance data for 1986-1987 Refer : Basinwide / Streamline WLA File Completed By Permits & Engineering At Front Of Subbasin RECEIVING STREAM: an unnamed tributary to Crowders Creek Class: C Sub -Basin: 03-08-37 Reference USGS Quad:_G 14 NW County: Gaston (please attach) Regional Office: Mooresville Regional Office Previous Exp. Date: 9/30/91 Treatment Plant Class: H Classification changes within three mules: none Requested by: Angela Y. Griffin Date: 2/28/91 Prepared by: Date: _ f� Reviewed��y: / c LPL— Date: lG lla C 79'5 J- /ate Modeler Date Rec. # S'en,.1 3 t k t o Drainage Area (mi`') ? J.f Avg. Streamflow (cfs): 0. d 7Q10 (cfs) Winter 7Q10 (cfs) >, c. 30Q2 (cfs) o, o Toxicity Limits: IWC % Acute/Chronic Instream Monitoring: Parameters v:: -� �£ L v Upstream Location 360 r f, Y ,-t -ft Downstream Location 7u o F t Effluent � Characteristics „J,�,yw �vmnw (i�N%✓ BODS (m ) / 7 5' NH3-N (mg/1) D.O. (mg/1) f TSS (mg/1) 30 F. Col. (/100 ml) PH (SU) I U LIJ i — - Co ments: r -1- FACT SHEET FOR WASTEtOAD ALLOCATIONS I Request Facility Name :CWS-SADDLEWOOD SUBDIVISION FT IV F D NPDES No. :NC0060755 Type of Waste :100% DOMESTIC Facility Status :EXISTING Permit Status :RENEWAL Receiving Stream :UT CROWDERS CREEK Stream Classification: C Subbasin :030837 County :GASTON Regional Office :MRO Ay- Requestor :GRIFFIN Date of Request :3/4/91 Topo Quad :G14NW ,SUN 6 1991 PERMITS & ENGINEERING # 6104 , ATV"L ANP t.1A� 291991 „"p;;�zillt�E l�kNa6EMEN OIVlS10fl `�F E�` Stream Characteristics: googswJI ►' USGS #0214561625 Date 2/90 Drainage Area: 0.08 sq.mi. Summer 7Q10: 0.0 cfs Winter 7Q10: 0.0 cfs Average Flow: 0.09 cfs 30Q2: 0.0 cfs Wasteload Allocation Summary (approach taken, correspondence with region, EPA, etc.) FACILITY REQUESTING RENEWAL OF EXISTING PERMIT. LAST WLA DONE IN 3/90 AND SADDLEWOOD WILL SUBMIT ENGINEERING REPORT ON NONDISCHARGE ALTERNATIVES BY 7/91. REPORT NOT RECEIVED AS YET. TECH SUPPORT RECOMMENDS EXISTING LIMITS. BECAUSE OF 7Q10=0 AND 30Q2=0, FACILITY MUST REMOVE DISCHARGE OR HAVE 5/1 & 10/1.8 LIMITS ASSIGNED IN JUNE 1993. FACILITY SHOULD CONNECT TO REGIONAL CROWDERS CREEK WWTP AS SOON AS AVAILABLE. Special Scheduled Requirements and additional comments from Reviewers: Recommended by: Date:_5/14/91_ Reviewed by ,-., '. _, Instream Assessment: ( Cl/Ll01XJLlJ Date: Regional Supervisor: G Date• q� 1 Permits & Engineering: Date: LZ 7/ef, v RETURN TO TECHNICAL SERVICES BY: JUN 18 1991 e Existing Limits -2- CONVENTIONAL PARAMETERS Monthly Average Summer/Winter Wasteflow (MGD): 0.009 / 0.009 BOD5 (mg/1): 16 / 17 NH3N (mg/1) : 9 / 12 DO (mg/1) : 6 / 6 TSS (mg/1): 30 / 30 Fecal Coliform (/100 ml): 200 / 200 pH (SU) : 6-9 / 6-9 Oil & Grease (mg/1): TP (mg/1): TN (mg/1): Toxicity: mdn;4-or CA)ori re : After 3 Years 0.009 / 0.009 5 / 10 1 / 1.8 6 / 6 30 / 30 200 / 200 6-9 / 6-9 Recommended Limits EXISTING LIMITS 11F DISCHARGE NOT IREMOVED ON 6/93 Summer/Winter I Summer7Winter I Wasteflow (MGD):0.009 / 0.009 10.009 / 0.009 1 BOD5 (mg/1): 16 / 17 1 5 / 10 NH3N (mg/1): 9 / 12 1 1 1.8 1 DO (mg/1): 6/ 6 1 6 6 1 TSS (mg/1): 30 / 30 1 30 30 1 Fecal Coliform (/100 ml): 200 / 200 1 200 200 1 pH (SU): 6-9 / 6-9 1 6-9 6-9 1 Oil & Grease (mg/1): TP (mg/1) : TN (mg/1): Toxicity: Chlor;ne: n'lon���' 1'� I INSTREAM MONITORING REQUIREMENTS:TEMPERATURE, DO, FECAL COLIFORM,CONDUCTIVITY Upstream: Y Location: 300 FT. UPSTREAM OF DISCHARGE Donwstream: Y Location: 300 FT. DOWNSTREAM OF DISCHARGE Limits Chances Due To: Instream Data Ammonia Toxicity Chlorine Nutrient Sensitive Waters HQW New 7Q10 flow data Special Modeling Studies New facility information Other Parameter(s) Affected NH3 (explanation of any modifications to past modeling analysis including new flows, rates, field data, interacting discharges, etc.) I AJO MEMO DATE: TO: I `` SUBJECT: c cc) L In - l N,,�-FC �c�- �1'^'�.',,, � w u.u- �o,✓.t/�t1 � � %i.�Jc 'tn � � re✓�a.��J 14 �qel,103 � �-172, 283 . STATE o� North Carolina Department of Environment, ��7�;, �. Health, and Natural Resources CAROLINA WATER SERVICE. INC. of N.C. AN AFFILIATE OF U II IU M-95,1NI IC - i Corporate Offices: 2335 Sanders Road Northbrook, Illinois 60062 Telephone: (312) 498-6440 Regional Offices:,. -,?. . 5701 Westpark Dr., Suite 101 P.O. Box 240705 Charlotte, NO 28224 (704)525-7990 Fax (704) 525-8174 j l`,j June 4 101 1 . , Mr. George T. Everett, Director N.C. Department of Environment, Health, and Natural Resources Division of Environmental Management P.O. Box 27687 Raleigh, NC 2761 1 Ref Saddlewood Subdivision N 579 T 5ermit #N,Yr �i�-? 5 5 Engineering Study Alternatives to Surface Discharge Dear Mr. Everett, North Carolina: Asheville, NO (704) 252-6864 Banner Elk, NO (704) 898-5011 Charlotte, NC (704) 525-7990 Morehead City, NO (919) 247-2309 New Bern, NC (919) 633-0920 rt' Whispering Pines, NC (919) 949-2010 .Ff 1991 - � f.. AI jYY SE" j JON r Please find the enclosed copy .of the Engineering Study completed for the above referenced facility by Moore Engineering Associates, as required in Part III (D) of the NP rmit. Due to the current size of the Wastewater reatment ant, it would not be economically feasible to utilize any of the outlined alternatives, other than the current surface discharge at present. Therefore, the requirements of Part III (D) state that the limits will change on June 1, 1903 to 5.0 mg �i BOD 5 and 1.0 mg NH3 as N d�!ring the summer, and 10.0 mgil BOD5 and 1.8 mg/1 NH3 as N during the winter. Carolina ,Water b Service requests that the change in BOD requirements -for the summer be f1% raised to 10 mg A BOD 5, as opposed to the 5 mg A DOD 5. All other requirements are acceptable at this time. If you have any questions, or if I can be of any further assistance, please do not hesitate to contact Mr. Bruce Haas or myself. Sincerely, -7 Carl Daniel Vice President Enclosures cc : File Mr. Bruce Haas ENGINEERING l..l Srl,U L 1` FOR EFFLUENT MANAGEMENT AT S ADDLEWn OD SLR BDIVIS ION WASTEWATER TREATMENT FACILITY MAY, 19 91 CAROLINA WATER SERVICE, INC-,/'. 5 701 WEST PARK DRIVE, SUITE 201 CHARLOTTE, NORTH CAROLINA 'N(I�NI�I11lIt Ye\% = _ SEAL 7609 d 7506 EAST INDEPENDENC:E BOULEVARD, SUITE 119 CHARLOTTE, NORTH CAROLINA 282-�'27 TABLE OF CONTENTS CONCLUSIONS AND RECOMMENDATIONS ...........................1 PAGE EVALUATION................................................3 PAGES GENERAL INFORMATION.......................................I PAGE ATTACHMENT A, PUMP SEWAGE TO GASTON COUNTY UTILITIES ...... 1 PAGE ATTACHMENT B, PUMP EFFLUENT TO NEAREST STABLE CREEK ....... 1 PAGE ATTACHMENT C, SUBSURFACE RECHARGE .........................1 PAGE ATTACHMENT D, CONSTRUCT LAND APPLICATION SYSTEM ........... I PAGE ATTACHMENT E, CREATION OF WETLANDS ........................I PAGE ATTACHMENT F, MODIFY EXISTING EXTENDED AERATION PLANT ..... 1 PAGE ATTACHMENT G, SOILS MAP...................................1 PAGE ATTACHMENT H, SOILS DESCRIPTION ...........................1 PAGE ATTACHMENT J, SCALED LOCATION MAP.........................1 PAGE ATTACHMENT K, PROCESS SCHEMATIC ............................I PAGE ATTACHMENT L, GENERAL LOCATION MAP........................1 PAGE. E N G= N E E R= N G S T U D Y SADDLEWOOD SLJBD=V= S =O1\1 WA S T E WA T E R T R E A T M E N T P LAN T Conclusions Surface discharge of treated effluent from an improved wastewater treatment plant at the Saddlewood Subdivision is the most cost effective alternative for meeting effluent discharge require- ments. Discharge limits set for June 1, 1993 for BOD5 and NH3 as N are not unrealistic for an extended aeration treatment plant. With process and operational modifications the Saddlewood waste- water treatment plant could reach both its winter and summer effluent limits. Recommendations Modify the treatment plant and it's operation in order to meet the effluent requirements that take effect June 1,1993. Alternatives Considered Wastewater treatment disposal methods considered included the following: 1) PUMP TO EXISTING UTILITIES (GASTON COUNTY) 2) PUMP TO A LARGER MORE STABLE STREAM 3) LAND APPLICATION (IRRIGATION) 4) CREATION OF A WETLANDS AREA 5) GROUNDWATER RECHARGE (SUBSURFACE DRAINFIELDS) 6) MODIFYING EXISTING FACILITY TO MEET DISCHARGE REQUIREMENTS BOTH CAPITAL AND OPERATIONAL COSTS WERE EVALUATED. EVALUATION PUMP TO EXISTING UTILITIES (GASTON COUNTY) Sewerage systems within a 5 mile radius include the Gaston County Utility System (see Attachment J). Sewerage systems outside this radius were not considered due to the high cost of connection to such a facility. Connection to the Gaston County Utility System would seem to be an acceptable choice. This would put the burden of treatment on a larger system with more available financial means. Such action on the other hand has not always led to an environ- mentally sound solution. During an upset, a larger system will put an enormous stress on a sometimes already fragile environment. A cost estimate for this alternative is attached (Attachment A). PUMP TO A LARGER MORE STABLE STREAM Transport.of the effluent to a larger stream is also an alternative that was considered. This would seem acceptable if the stream was within a short distance. Crowders Creek was the next closest source for discharge of the effluent that was considered. This alternative meets with some protest in that you are only transferring your problem by piping it from one location to another. The travel time along a natural water course provides some additional treatment and safety factor. The effluent will be in an improved state having traversed the natural channel rather than being piped directly to a point downstream. The stream itself becomes a source of treatment. Treatment of the problem on site seems the more logical solution rather than transporting it to another environment that may not be able to handle the added stress. A cost estimate for this alternative is attached (Attachment B). GROUNDWATER RECHARGE A soils map of the treatment plant location (Attachments G and H) indicates patchy areas of generally suitable soils for groundwater recharge, specifically subsurface drainfields. Over time a drainfield of this size with the surrounding soil may tend to blind. There may also come a time when the drainfield will not satisfy the water disposal requirements of the entire subdivision. The amount of land and utilities required for a central drain field for a subdivision of this size would cause this alternative to be economically burdensome. A cost estimate for this alternative is attached (Attachment C) LAND APPLICATION The cost of spray irrigation will exceed the cost of "secondary" treatment at least by the cost for pumping and delivery systems, monitoring, crop maintenance, land agreements, legal fees and public relations (the latter have been a justifiable concern on every effluent irrigation system presently known to the preparer, and should be included in spray irrigation and other land application system considerations). A cost estimate for this alternative is attached (Attachment D) CREATION OF A WETLANDS AREA The creation of a wetlands around the wastewater treatment facility would seem to be an environmentally sound alternative. Providing a wetland area at discharge will prevent the treated water from going directly into the stream. This natural buffer would allow more time for BOD5 and NH3 removal in an environment designed for this purpose. The problem with this alternative is the potential of flooding the wetlands. If a flood were to inundate the wetlands however., the flood waters themselves would most likely be carrying higher levels of BODS and NH3 than the effluent levels of the wastewater treatment plant. A cost estimate for this alternative is attached (Attachment E). MODIFYING EXISTING FACILITY TO MEET DISCHARGE REQUIREMENTS The existing plant nearly meets the June 1, 1993 limits required in the NPDES Permit with existing equipment and operation. By addition of other equipment, including fine bubble aeration, process controllers, an effluent filter and biological selector modifications to the aeration tank, the plant can be expected to perform consistently within the limits prescribed in the NPDES Permit for June 1, 1993. Fine bubble aeration should be added to insure adequate oxygen for oxidation of both carbonaceous BOD5 and ammonia nitrogen. Shallow packaged plants are often fitted with coarse bubble diffusers and the air supply is sized for tank agitation. Oxygen transfer is around 2% and as such is seldom sufficient to meet carbonaceous and ammonia demands with the air supplied. The installation of fine bubble aeration provides better oxygen transfer (around 10%) and improved mixing. In addition, the diffusers will be installed to encourage plug flow in the reactor vessel. Utilization of a selector chamber encourages the growth of desirable organisms and thus assists in bulking control (by not favoring filamentous organisms) and can, under controlled conditions, encourage and accomplish nutrient (phosphorus and nitrogen) removal. In this instance it will be used to provide a more stable, settleable activated sludge mixed liquor. A process controller will allow reduction in return streams from return sludge and skimmers. This will remove a significant amount of stress on the final clarifier, thus promoting greater removal of suspended solids, and consequently BOD5. In addition, a higher quality effluent will reduce filter upset problems and possibly obviate the need to operate the filters at all. Effluent filter(s) may be required to meet State approval for the new final effluent quality. In any case, installation should be planned to insure the ability of the plant to meet the imposed standards. A myth concerning filters has been that when the plant is upset, the filter can allow continued compliance with effluent permit limits by removing excess suspended solids. Actually, a filter can only provide polishing of a good effluent. If effluent quality deteriorates to any significant degree, the filter will rapidly plug and will be helplessly bound in backwash cycles. Rapid fouling of the filter will also create frequent filter cleaning requirements, and thereby excessive maintenance costs. A cost estimate for this alternative is attached (Attachment F). Background Information The Saddlewood Wastewater Treatment Plant is an existing 0.009 MGD extended aeration steel factory prefabricated package plant located in and serving part of the Saddlewood Subdivision off of North Carolina State Road 2416. The treatment works currently discharges into an unnamed tributary to Crowders Creek which is classified as Class C waters in the Catawba River Basin. The plant is owned and operated by Carolina Water Service, Inc. Wastewater received by the existing facility comes directly from residences in part of the Saddlewood Subdivision by way of gravity sewer. The existing process is schematically represented in Attachment K and consists of coarse screening, extended aeration activated sludge with final sedimentation and tablet chlorination for dis- infection. Existing air diffusers in the aeration tank are coarse bubble type. The return sludge and scum are moved by air lift pumps. The aeration compartment has a capacity of 24 hours detention based on the average daily design flow. The final settling basin is a hopper -bottomed type structure, the bottom of which is formed into an inverted pyramidal hopper. All side walls have a slope of at least 60 degrees. The sludge which settles to the bottom of the hopper is returned to the aeration tank by means of an air lift placed in each hopper. Disinfection follows final settling (clarification) by tablet chlorination. Effluent flowing past the solid tablets is designed to dissolve hypochlorite in sufficient amount for effective eff- luent disinfection. A general locution map is attached showing the position of the facility in relation to local roads, streams and other landmarks (Attachment L). The above"location map is scaled, in Attachment J, (from USGS Topographic sources) and shows the existing location of the treatment works and the discharge point. ***END OF REPORT*** PUMP SEWAGE TO GASTON COUNTY UTILITIES Attachment A Item Description Oty. Units Cost/unit 1 Grinder Pump Equip. & Well 1 LS $6,500.00 2 Concrete 3 CY $350.00 3 Building 1 LS $1,500.00 4 Fittings & valves 1 LS $750.00 5 Misc. metals & equip. 1 LS $750.00 6 Force line, 2 in. dia. 4,500 LF $8.00 7 Electrical work 1 LS $1,000.00 8 Site work, fencing, etc. 1 LS $2,500.00 9 Easements 1.4 Ac $10,000.00 10 Utility Connection Fee 1 LS $10,000.00 11 Contingencies 15.0% $64,050.00 Construction Cost Subtotal Engineering, surveying & testing 14.0% Legal 3.0% Admin 3. 0 % Total Capital Cost Admin & Maint. Power Estimated annual operating cost $22,462 $161 Present worth, operating cost @ 15.0% 10 years TOTAL PRESENT WORTH COST Cost $6,500 $1,050 $1,500 $750 $750 $36, 000 $1, 000 $2,500 $14,000 $1 O , 000 $9,608 $83,658 $11,712 $2, 510 $2,510 $100,389 $94,103 $472,283 $572,672 L PUMP EFFLUENT TO NEAREST STABLE CREEK Attachment B Item Description oty. Units Cost/unit Cost 1 Pumping equipment & well 1 LS $5,000.00 $5,000 2 Concrete 3 Cy $350.00 $1,050 3 Building I LS $1,500.00 $1,500 4- Fittings & 'valves 1 LS $750.00 $750 5 Misc. metals & equip. 1 LS $750.00 $750 6 Force line, 2 in. dia. 5,000 LF $8.00 $40,000 7 Electrical work I LS $1,000.00 $1,000 8 Site work, fencing., etc. 1 LS $1,500.00 $2...500 9 Easements 1.5 AC, $101000.00 $15,000 10 Contingencies 20.0% $66,550.00 Construction Cost Subtotal $79,860 Engineering, surveying & testing 24. 0(t $11.130 Legal 5.0% $3, 993 Admin 3. 0% $2,396 Total. Capital Cost $97,429 Admin & Maint. Power, Estimated annual operating cost $28,474 $811 $94- 10 Present worth, operating cost @ 15.0% 10 Years $472,283 TOTAL PRESENT WORTH COST $569,713 CREATION OF WETLANDS Attachment C. Item Description oty, Units Cost/unit Cost 1 Land Apuisition 2.75 AC $10,00.00 $27,500 2 Excay. & backfill 0,437 CY $10.00 $44,367 3 Grading and planting 2.75 Ac. $1,500.00 $4,125 4 Contingencies 25.00 $71,866.67 $17,967 Construction Cost Subtotal $93,958 Engineering, surveying & testing 20.0o $18,792 Legal 5. 0 % $". 698 Admin 3. Ora $2, 819 Total Capital Cost $120,267 Labor & Admin Power Estimated annual operating cost $25,768 $715 $94,103 Present worth, operating cost C 15.0% 1.0 years $472,2 83 TOTAL PRESENT WORTH COST $592.550 ATTACHMENT H CONSTRUCT LAND APPLICATION SYSTEM Attachment D Item Description QtY. Units Cost/unit Cost 1 Pumping eq. & well 1 LS $8,500.00 $8,500 2 Concrete 10 CY $350.00 $3,500 3 Building I LS $11500.00 $1,500 4- Fittings & valves 1 LS $3,500.00 $3, 500 5 Misc. metals & equip. I LS $5,000.00 $5,000 6 Pipe and fittings 1,500 LF $8.00 $12,000 7 Electrical work 1 LS $2,500.00 $2,500 8 Site work, fencing, etc. 1 LS $2.500.00 $2..500 9 Excay. & backfill 3100 CY $3.00 $2,400 10 Sprinkler Heads 40 EA $100.01D $4- , 000 11 Instrumentation/controls I LS $21,400.00 $2,400 12 Irrigation distribution 3,000 LF $12.50 $37,500 13 Holding Pond 0.99 Ac. $52,272.00 $51,979 14 Land Aquisition 4 a c . $ 101, 000. 00 $4.0, 001D 15 Contingencies 25.0% $137,279 $34,320 Construction,Cost Subtotal $198.098 Engineering, surveying & testing 20.0% $39,620 Legal 3.0% $5,943 Admin 3. 0 511; $S,943 Total Capital Cost 1; 24 9. b04. Labor & Admin Power Estimated annual operating cost $4,3,,093 $100,a87 $94,103 Present worth, operating cost @ 15.0% 10 Years $472,283 TOTAL PRESENT WORTH COST $721,887 SUBSURFACE RECHARGE Attachment E Item Description oty. Units Cost/unit I Pumps, contr., well, elec. I LS $8,000.00 2 Concrete 3 Cy $300.00 Building 1 LS $1,500.00 3 Fittings & valves 1 L $750.00 4 Misc. metals & equip. 1 LS $750.DO 5 Land Aquisition 4 Ac $10.000.�0 6 P i p i n �:,'j 1.500 L F $5. --10 7 Site work, fencing, etc. I LS $1,250.00 8 Excay. & backfill .1500 CY 9 Distribution Pipe 10000 LF 10 Gravel 1200 CY $16. o 11 Distribution Box 1 LS 1; 8 0 0. 0, ID 12 Contingencies 20.0% $122,650.�0 Construction Cost Subtotal Engineering, surveying & testing 15.0% Legal 3.0% Admin 3.0% Total Capital Cost Labor & Admin Power Estimated annual operating cost $23,106 $871 Present worth, operating cost @ 15.0% 10 Years TOTAL PRESENT WORTH COST Cost $.8'000 $900 $1,500 $750 $750 $ 40 , 000 $7, 500 $ 1, 2-5 0 $12,000 $30,000 $19,200 $800 $24,530 $147,180 $29,715 $519413 $5,943 $188,781 $94,103 $472,283 $661,064 MODIFY EXISTING EXTENDED AERATION PLANT Attachment F Item Description Qty. Units Cost/unit Cost 1 Fine Bubble Diffusers 5 EA $100.00 $500 2 Pipe work & fittings 1 LS $1, 500.00 $1, 500 3 Timer for Air Lift Skimmer 1 EA $200.00 $200 4. Electrical Work 1 LS $2,000.00 $2,000 5 Addition of Selector 1 LS $5,000.00 $5,000 6 Addition Of Filter 1 LS $27,000.00 $27,000 7 Contingencies 25.0% $361200.00 $9.050 Construction Cost Subtotal $4.5,250 Engineering, surveying & testing 20.0% $9,050 Legal 3.0, $1,358 Admin 3.00 $1,358 Total Capital Cost $57.015 Labor & Admi.n Power Estimated annual operating cost $40,699 $74.2 $94,103 Present worth, operating cost @ 15.0o 10 years $472,283 TOTAL PRESENT WORTH COST $529,298 Capital CostTotal PW Cost PUMP SEWAGE TO GASTON COUNTY UTILITIES $100,389 $572,672 PUMP EFFLUENT TO NEAREST STABLE CREEK $97,a29 $569,713 CREATION OF WETLANDS $120,267 $5921550 CONSTRUCT LAND APPLICATION SYSTEM $24.9,604. $721,887 SUBSURFACE RECHARGE $188,781 $661,064. 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