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HomeMy WebLinkAboutNC0079227_Approval_20180613WaterResources ENVIRONMENTAL QUALITY June 13, 2018 Russell E. Eiler, Director, Global EIIS Compliance Schlage Lock Company LLC 11819 N.Pennsylvania Street Carmel, Indiana 46032 Subject: Dear Mr. Eiler: ROY COOPER Gom". MICHAEL S. REGAN Semlary LINDA CULPEPPER ham., Director NPDES Permit NCO079227 Review of Application to Modify Permit for the Former Schlage Lock Plant GW-REM — Class PC-1 213 Red Iron Road, Rocky Mount 27804 Nash County The Division of Water Resources (the Division or DWR) has reviewed your application (received April 3, 2018) to modify the subject permit. We do not believe the permit needs to be modified for you to proceed. We understand you propose to vaporize liquid -phase organic compounds to facilitate contaminant removal in the subsurface, then condense the vapor back to liquid for treatment prior to discharge. We have considered the potential impacts to the receiving stream of changes in process temperature, and have also reconsidered the list of parameters of concern (POCs). The Division concludes that a permit modification is not required if the condensate effluent is treated, as is the extracted groundwater, such that all discharges meet existing permit limits and conditions. Lastly, please note that we have updated your site -vicinity map (see attached). If you have questions, or if we can further assist you, please contact Joe R. Corporon L.G. at fioe.comoron0mcdenngovl or call his direct line (919) 807-6394. Linda Culpepper Enclosure: Site -Vicinity Map hc: Central Files NPDES Program Files DWR/RRO Supervisor, Danny Smith ec: ATU, Susan Meadows OCU, Maureen Kinney DWR/RRO Supervisor, Danny Smith 1 y c _ u 1 0 \ 1 r Approximate Property ` �s`=` PP P rh' ,00 `�B Boundary /00 LJ Q= J(D J zo /100' N UT to Beach //'�\ ' ,l ,� " • Branch mar• _ A Outfa11001 •----- (Flows north) r e. NORTH CAROLING .. ....� (� EBLSYGN COLLEG .J s e p• rj CS 0- 131 i O � \ � � f ..1 ` •1 ``_� `o J NC Hwy 301 301 r✓ j �- �1 — - /� 1100 1 � , Iq0 j 1403 _ 1400 Schlage Lock Company LLC Facility Former Schlage Lock Plant - GW-REM Location not to Scale Receiving Stream: UT of Beach Branch Drainage Basin: Tar -Pamlico Latitude: 36' 01' 28" N Longitude: 770 46' 04" W Sub -Basin: 03-03-02 Permitted Flow: 0.124 MGD NPDES Pernut NC0079227 State Grid / USGS Ouad: C 27 SE / Drake, NC Stream Class: C-NSW North Nash County Corporon, Joe: MOD review LOG / Fact 79227 - Schlage LockAant - GW-REM; system MOD 20Apr2018 -- assigned to Joe. 01May2018 -- Jeff Ahrens P.E., Principal Engineer, Geosyntec [704-227-0850] called to ask about progress on MOD. Joe has yet to review the MOD request. 08May2018 -- Rob Mcdaniel (DEMLR/HWM; Hydrogeologist, PJM; 919-707-8215) called to offer his assistance with MOD; said Schlage does are on Lazerfiche, EPA ID# = NCD065300519; will email CAP to Joe. Permittee applying electrodes to plume; vapor -phase to be collected and treated. Active in the next month or two. Joe to copy Rob on the MOD response letter. Updated BIMs Events/initiated MOD review. 09Mav2018 Notes: Permittee proposes to add "thermo-treatment" to vaporize parameters of concern (POCs); new processes will add —2.1 gpm [0.0030 MGD] to the flow currently averaging 0.02722 MGD [about 22% of permitted flow], but the Permittee will simultaneously abandon 3 recovery wells, resulting in —no net gain in flow. The remediation target, PCE (99% reduction), enters treatment @ — 1,000 ug/L will be treated to 9 ug/L; temperature is expected to resolve to ambient through the system long before discharge, and is therefore is not a POC. Julie Grzyb discussed needs with the Permittee prior to application (021762018) saying that, beyond temperature (effluent, U&D), no modifications (limits or flow rate) are anticipated. Facts considered during MOD request review: 1. POCs monitoring frequency - continuous flow Ave 0.027 MGD / 190k gallons/week (27,142 gpd). 2. update O&G to reflect EPA test method — decided "no." 3. adding metals (?) — decided "no." 4. considered Temperature monitoring for "heat" process added — decided not a factor at discharge 5. reviewed parameters of concern (POCs) — no changes recommended 30May2018 -- Confirmation by NPDES Staff [Julie / John] Conclusion: No permit changes recommended; generate letter for signature by John Hennessy. Geosyntecc> consultants Geosyntec Consultants of NC. PC 2501 Blue Ridge Road, Suite 430 Raleigh, North Carolina 27607 PH 919.870.0576 w .geosyntec.com February 22, 2018 Ms. Julie A. Grzyb RECEIVED/DENR/0WR Supervisor NPDES Complex Permitting NPR - 3 2018 North Carolina DEQ/Division of Water Resources/Water Quality Permitting 1617 Mail Service Center Water Resource. Raleigh, North Carolina 27699-1617 Permitting Section Subject: Modification Request for NPDES Permit NCO079227 Former Schlage Lock Facility 213 Red Iron Rd. Rocky Mount, Nash County, NC L Dear Ms. Grzyb: Geosyntec Consultants of NC, PC (Geosyntec) is working on behalf of Schlage Lock Company LLC (Schlage) to conduct environmental remediation activities at the Former Schlage Lock Facility located at 213 Red Iron Road in Rocky Mount, North Carolina (Site). Environmental activities at the Site are being conducted in accordance with a North Carolina Department of Environmental Quality (NCDEQ) issued Administrative Order (AO) in Lieu of a Post -Closure Permit, which initially became effective in December 2011 and was updated in December 2016 (Docket Number AA2011-084). Currently, remedial activities at the Site include the operation of a groundwater extraction and treatment system, which treats chlorinated volatile organic compound (CVOC) impacted groundwater prior to discharge under an existing National Pollutant Discharge Elimination System (NPDES) Permit NCO079227 (Attachment 1). As we have discussed with you in a phone conversation on 02 February 2018, and as presented in this correspondence, Geosyntec is requesting a modification to NPDES Permit NC0079227, to implement additional remedial actions at the Site using in situ thermal remediation (ISTR), which is proposed to discharge its treated effluent into the existing groundwater extraction and treatment system prior to discharge in the existing NPDES Outfall 001. The NPDES permit modification request form (NPDES Permit Application - Short Form C — GW) is provided as Attachment 2. Purpose of Modification Request A groundwater extraction and treatment system has been in operation at the Site since 1992 to address CVOCs in groundwater. While the groundwater distribution of CVOCs has been relatively Former Schlage Lock Facility, Rocky Mount, NC engineers I scientists I innovators Ms. Julie A. Grcyb 22 February 2018 Page 2 stable in recent years, a more aggressive source zone remedial strategy has been approved by NCDEQ as part of an NCDEQ-approved Site Closure Strategy. An evaluation of targeted source zone remedial technologies led to the concurrent decision by Geosyntec, Schlage, and NCDEQ to reduce CVOC mass via ISTR, as documented in an Interim Measures Work Plan (June 2017). The proposed ISTR system will utilize Electrical Resistive Heating (ERH) to heat up the subsurface beyond the boiling point of the CVOCs and remove contaminants with vapor recovery wells. The extracted steam and vapors will be separated into liquid and vapor streams, cooled, and treated above -grade in a modular treatment system operated at the Site by the ISTR contractor. After pre- treatment by the ISTR contractor, the liquid -phase effluent is proposed to be discharged to the existing on -Site groundwater extraction treatment system, where it will combine with extracted groundwater from operating recovery wells. The groundwater extraction and treatment system will serve as secondary treatment and the combined treated groundwater will discharge to the existing Outfall 001. The ISTR system construction and operation process is anticipated to take approximately one year to complete (we anticipate construction to begin in Spring 2018), and the modular equipment will be removed following ISTR operations, at which point the groundwater extraction and treatment system operations are anticipated to continue. Please note that the groundwater extraction and treatment system will continue to operate during ISTR construction and operation; however, some pumping wells located within the footprint of the ISTR treatment zone will be abandoned. Description of Existing Groundwater Extraction and Treatment System and Permitted Discharge The existing groundwater extraction and treatment system currently consists of sixteen recovery wells (nine in the Middle Aquifer and seven in the Lower Aquifer). Prior to implementation of the ISTR system, three Middle Aquifer recovery wells (RW-2, RW-3 and RW-7, which have a combined average extraction rate of approximately 2 gallons per minute [gpm]), will be abandoned. Extracted groundwater is piped to the treatment building where it passes through an equalization tank, an air stripper, and bag filers prior to discharge via permitted Outfall 001 to an Unnamed Tributary of Beech Branch. A USGS map showing the location of the permitted Outfall 001 is provided as within the existing NPDES permit, included as Attachment 1. Between 2003 and 2017, the average pumping rate of the system was 18.9 gpm (equivalent to 0.027 million gallons per day [MGD]). The effluent from the treatment system is monitored in Fortner Schlage Lock Facility, Rocky Mount, NC engineers I scientists I innovators Ms. Julie A. Grzyb 22 February 2018 Page 3 accordance with NPDES permit NC0079227 (effective June 1, 2015 through October 31, 2019) (Attachment 1). The system's average flow rate (monitored continuously) between 2003 and 2017 was less than 22 percent of the 0.124 MGD permit limit. Pursuant to the existing NPDES permit, groundwater extraction and treatment system effluent samples are analyzed twice per month for Oil and Grease, Total Suspended Solids, pH, and temperature; and quarterly for select VOCs and chronic toxicity. Oil and Grease, Total Suspended Solids, and pH in the effluent are consistently within permit limits. VOC concentrations in the effluent have remained consistently below laboratory detection limits (i.e. less than 1 µg/L). In the treatment system influent, the average concentration of the primary VOC of concern, tetrachloroethylene (PCE), was 4,035 micrograms per liter (µg/L) between 2003 and 2017. The reduction in tetrachloroethylene concentration demonstrates that the removal efficiency of the treatment system is greater than 99.9%. The most recent monthly and quarterly sampling results are provided as Attachment 3. Proposed In Situ Thermal Remediation System The proposed ISTR system will achieve a significant removal of CVOCs (estimates of source area CVOC mass removal of approximately 12,000 Ibs) through heating of the subsurface and subsequent recovery of volatilized CVOCs and steam. Vapor recovery (VR) wells will convey the extracted steam and vapors to modular treatment components, including a process to separate liquids and vapors, a steam condenser system, a vapor treatment system, and a condensate treatment system. The condensate treatment system includes both a cooling process and an adsorption process to remove CVOCs in the condensed liquid. The vapor treatment system will be subject to its own air permit process, which is being addressed separately with NCDEQ. TRS Group, Inc. (TRS) has been selected as the ISTR contractor. A process flow diagram and detailed process and instrumentation diagrams (P&IDs) for the liquid -phase treatment components of the ISTR system, provided by TRS, are included as Attachment 4. The average condensate production rate produced by the ISTR system is expected to be approximately 1.8 gpm and is expected to contain approximately 1,000 µg/L PCE prior to treatment. The water treatment system for the condensate will consist of tanks for sedimentation, bag filters to capture remaining suspended solids, liquid granular activated carbon (LGAC) vessels to provide 99% reduction in CVOC concentrations via adsorption, and a heat exchanger to reduce Former Schlage Lock Facility, Rocky Mount, NC engineers I scientists I innovators Ms. Julie A. Grzyb 22 February 2018 Page 4 water temperature to that of the extracted groundwater. Sampling ports are included in the influent line to each LGAC vessel and at the effluent of the heat exchanger. The heat exchanger in the steam condenser system is water-cooled by recirculating potable water within two cooling towers. The cooling water will not come into contact with the steam from the subsurface. The cooling water will periodically blowdown to control mineral buildup at an anticipated average rate of 0.3 gpm. The treated condensate stream will join the potable water blowdown stream for an expected combined flowrate of 2.1 gpm (0.0030 MGD) and an approximate PCE concentration of 9 µg/L. The treated effluent will then enter the existing on -Site treatment system where it will join extracted groundwater and pass through the settling, air stripping, and filtration processes prior to discharge via existing Outfall 001. A process flow diagram for the existing pump -and -treat system, annotated with the proposed thermal effluent insertion point, is provided as Attachment 5. In summary, the thermal system will add approximately 2.1 gpm of treated water into the existing treatment system, which is currently only processing less than 22 percent of its 0.124 MGD limit at an average flowrate of 18.9 gpm. Additionally, it is noted that the abandonment of three recovery wells will result in a reduction of approximately 2 gpm from the groundwater extraction and treatment system. The thermal effluent will be treated by LGAC adsorption, cooled to the same temperature as the extracted groundwater, and then combined with extracted groundwater for secondary treatment by air stripping. The water quality of the effluent in Outfall 001 is expected to be comparable to existing conditions and to meet permit limits. Per discussion with you by telephone on 02 February 2018, Geosyntec understands that the existing NPDES permit will need to be modified to include an explicit temperature requirement, in consideration of the new remedial process that has been proposed. No other modifications (e.g., flow rate, CVOC limits, etc.) are anticipated to be required. The thermal treatment system is scheduled to be installed between April 2018 and July 2018. Thermal operations are planned to begin in July 2018 and end in the second quarter of 2019, which is within the dates of the current NPDES permit authorization. Geosyntec greatly appreciates your attention to this requested modification in order to facilitate a timely installation of the remedy and path to closure. Former Schlage Lock Facility, Rocky Mount, NC engineers I scientists I innovators Ms. Julie A. Grzyb 22 February 2018 Page 5 Should you have any questions regarding this submittal, please contact the undersigned at (704) 227-0850. f Ahren. Principal Engineer Attachments: 1— Existing NPDES Permit NCO079227 2 - NC Form C-GW Sincerely, Wayne Amber, Ph.D. Project Manager 3 - Recent monthly and quarterly sampling results 4 - Proposed Thermal Process Diagrams 5 - Existing System Process Diagram Copies to: Mr. Russ Eiler - Schlage Former Schlage Lock Facility, Rocky Mount, NC engineers I scientists I innovators WATER TREATMENT SYSTEM BLDG D FENCE GRIP TdFflOM A01- pDU 1100 MR PIPING FROM AOI 2 P LOOP BAG L TO*ROQm-1 TO GEOSYNTEC WATER POLY TANK VR PIPING TREPMENT SYSTEM FROMAOI-1 zoo LB LOU ID GAS VESSELS GRASS MMEUP WATE ON E ERHSYSTEMOISCHAR GET (POTABLE SOURCE) GEOSYNTEC WATER TREAMENT SYSTEM PNIOR TO NPTES p� .CHMGE (OUTFP1L 001) rig K1 OFFICE WER 11 TRNLER TACK IS�EE L14 40 HP NOTE2NOTE O GACVESSELS M1 -_ NOTES 1. STACK HEIGHT WILL BE 15 FT, UNLESS DTHERNASE ROM CONDENSER REQUIRED BY THE AIR PERMIT. BROKEN CONCRETE N 2. PIPING TO OM THE VGAC VESSELS CAN BE CPVC OR H28 FLEX HOSE. 0 H29 - 0 H301 — SIC PEX -, BDHSOPVC EQVIPMENT PIPING PLAN — 2' BCH 40 PVC TRS T SCH 40 CPVC A9NOdUMLe — SECONOARYCONTAINMENT 0 10 3U 40 ® 'umm"u _ "slc.oe —.— SECURITY FENCE BCRI — Y-4 LEGEND PEID LINE COLORS LIRE WELMO f PVRR WEMTEB"2"SZWO, OMIXtY la enen%z POR ExlcnlPiwn GATP cauEcm�IWoroxrx«s 4 Ctl MMPNREf.CMRUB BCfiFNE[YWTI94EFLEYI WI.iEI MLLV.LLVE x MYYRE INBIGRIR iAOLEY W/'TER BVFRRFLr vuY£ AN PgEBU1gE CpIIRU vuVE MR MNn rry ANT.MREMVYVE R MEBYRE BWRIf♦IIPV Mg2RAM MIX R PLCW UFNEM N M TRUEUNWMLLV.LLVE --_.__-_ BIWAUVN Ytl MM0.F KRi N RVNIXBx:/.iOR WMPR REMERPTEBCOXTRUB q %owounxim xwcnioR N ueuwLVE MggVTREUXRROY selFWiuEWY II PLbMTRN1YTlR ELECAIGLCIHLE wl' E MYYRE REMiw q %pMCUPMI1V IXpv.Tw -D6 BPpm U LtVH.p . EM LEVEL.. NiV BYXFLdI pIFYEx1EA FVtgE VEM LEVU6LMG11[dINGM 41 LEVELBNR'"U"M VPryVYgIILNEVYVE ESE LEVEE8N1FGIlPVyON %(�xR NPI1p8PFC. OCMWE UI TEMPERATURE MARYNY. TE TEYPEMNREEYE M WYP R ... TIYPEMNPEU RLM14ER 11 RYPEMTVRE xBC/.LCR 1tYPEMNRE6MRCN MIBN OqI RERANr Epee WEMWR O x cwnvuEER T i.REMTURE S. ® rPxx c uReox BTEu 6x BCNtl.CWG%tE ® MPT FFOU.YER RR xTftIA RLRMILINCER q FLgY UIxiROL V.LLVE M FETERn UMNG M PRESSURE BN HHPUR TG TEYPERANRE9NRGIxpX SUBMERSIBLE PUMP MIS* M' ALLINUMMUSEMNEWEET. IgTALL SYYBYS W.LLAPPFMON FKxBMEET POIO LINE COLORS PHOOEBB WNTM MR NRIST MIX BLOMD Procan Steam Location Air Watar Vapor Water CVOCs umparatt re I Pn ra Dssctiptlon g (lb/min) (acfm) (lb/min) (scfm) (m/min) (gpm) (lb/min) (ppm) aC °P (8 from barvmabk) Eoraded air and steam from vapor recovery system 1 65 860 16.7 356 0 0.0 0.039 73.68 69 156 2" HS Vac Discharge air from condenser after steam removal 2 65 860 LB 37 0 0 0.039 I00.08 30 86 5' Hg Vac Condensate discharge from condenser 3 0 0 0 0 IS 1.8 1.5E-05 1.03 30 86 30 psig Bleed air to rotary lobe blower 4 6 86 0 1 0 0 0 0 13 56 N/A Discharge air from rotary lobe blower 5 71 946 1.80 38 0 0 0.039 91-23 60 140 1 psi Discharge from carbon vessels 6 71 946 L90 38 0 0 3.9E-04 0.91 50 122 N/A Cooling air into cooling tower 7 2250 30,OW 16.94 360 0 0 0 0 13 56 N/A Air exhaust from cooling tower 8 2250 30AW 30 632 0 1 0 0 0 IS 65 WA Recircule0on water from condenserto coolingtower 9 0 0 0 0 4996 600 0 0 IB 65 IO prig Recirculation from cooling tower to condenser 10 0 0 0 0 4998M2.30 0 16 60 Make-up water for cooling tower from potable source 11 0 0 0 0 19 0 20 68 Driwater to electrodes(potable) 12 0 0 0 0 4 0 30 86 Blowdown 13 0 0 0 0 2 0 30 e6 :psig Condensate after LGAC 14 0 0 0 0 Is 0.01 30 86 Discharge to Geosyntec water treatment system 15 0 0 0 0 17 B.BE-03 30 86 N4r1R r.inernw ixaurzmxrxarr,usconnsaxoxoro me wunox xuuuaa rxonceo ox sxssr ry .m.e .Wm�.vo PROCESS FLOW MASS BALANCE i^�ia ""•.iccc. 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