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HomeMy WebLinkAboutNCG140518_Application_20230117RECEIVED FOR AGENCY USE ONLY NCG14____ Assigned to: ARO FRO MRO RRO WARO WIRO WSRO JAN 17 2023 Division of Energy, Mineral, and Land Resources Land Quality Section National Pollutant Discharge Elimination System NCG140000 Notice of Intent This General Permit covers STORMWATER AND/OR WASTEWATER DISCHARGES associated with activities under SIC (Standard Industrial Classification) Code 3273 [Ready Mix Concrete] and like activities. You can find information on the DEMLR Stormwater Program at deq.nc.gov/SW. Directions: Print or type all entries on this application. Send the original, signed application with all required items listed in Item (8) below to: NCDEMLR Stormwater Program, 1612 MSC, Raleigh, NC 27699-1612. The submission of this application does not guarantee coverage under the General Permit. Prior to coverage under this General Permit a site inspection will be conducted. 1. Owner/Operator (to whom all permit correspondence will be mailed): Name of legal organizational entity: Legally responsible person as signed in Item (9) below: The Lane Construction Corporation David Cha arro Street address: City: State: Zip Code: 6125 T ola Centre Drive Charlotte NC 28217 Telephone number: Email address: 336-518-4671 dmcha arro laneconstruct.com Type of Ownership: Government ❑ County ❑ Federal ❑ Municipal ❑ State Non -government ® Business (If ownership is business, a copy of NCSOS report must be included with this application) ❑ Individual 2. Industrial Facility (facility being permitted): Facility name: Facility environmental contact: Lane Temporary Concrete Batch Plant - Chapel Hill Roberto Morales Street address: City: State: Zip Code: 7201-UT NC 86 S Chapel Hill NC 27514 Parcel Identification Number (PIN): County: 9880096500 Orange County Telephone number: Email address: 704-712-1879 rmorales@laneconstruct.com 4-digit SIC code: Facility is: 1 Date operation is to begin or began: 3273 M New ❑ Proposed ❑ Existing June 1, 2023 Latitude of entrance: Longitude of entrance: 35058'28"N I 79003'53"W Brief description of the Vpes of industrial activities and products manufactured at this facility This is a temporary portable ce ral mix concrete batch plant which will be used to produce concrete for the 140 Widening From 1-85 IN Orange County to The If the Stormwater discharges to a municipal separate storm sewer system (MS4), name the operator of the MS4: ® N/A Page 1 of 7 This facility uses: ❑ Phosphorus -containing detergents ❑ Non -Phosphorus -containing detergents ❑ Brighteners ❑ Other Cleaning Agents This facility has a closed -loop recycle system that meets design requirements in 15A NCAC 02T. 1000 and hold the facilities working volume ❑ Yes —stop completion of this N01. Contact DWR Non -Discharge Permitting Program for permitting requirements ® No 3. Consultant (if applicable): Name of consultant: Consulting firm: Street address: City: State: Zip code: Telephone number: Email address: 4. Outfall(s) (at least one outfall is required to be eligible for coverage): 3-4 digit identifier: Name of receiving water: Classification: ❑ This water is impaired. 001 1 Old Field Creek WS-V; NSW ❑ This watershed has a TMDL. Discharge from this outfall is from: ❑ Stormwater Only ❑ Wastewater Only ® Wastewater Comingled with Stormwater 7Q10 Flow of receiving waterbody (if discharging Wastewater Only or Wastewater Comingled with Stormwater to waters classified as HQW ORW, Tr, WS-I, WS-II, WS-III, SA, or PNA): Discharge occurs from this outfall: ❑ Only during a rainfall event ® Intermittent 4indicate how often El Continuously (indicate flow in CFS) Depends on deman o productions but d could once week. Latitude of outfall: Longitude of outfall: 35058'24"N I 79°03'57"W Brief description of the industrial activities that drain to this outfall: The industrial activities that drain to this out fall are as follows, truck washout, spray down or actively wet aggregate piles, and mixer drum clean -out. Do Vehicle Maintenance Activities occur in the drainage are of this outfall? ❑ Yes ® No If yes, how many gallons of new motor oil are used each month when averaged over the calendar year? 3-4 digit identifier: Name of receiving water: Classification: ❑ This water is impaired. ❑ This watershed has a TMDL. Discharge from this outfall Is from: ❑ Stormwater Only ❑ Wastewater Only ❑ Wastewater Comingled with Stormwater 7Q10 Flow of receiving waterbody (if discharging Wastewater Only or Wastewater Comingled with Stormwater to waters classified as HQW, ORW, Tr, WS-I, WS-II, WS-III, SA, or PNA): Discharge occurs from this outfall: ❑ Only during a rainfall event ❑ Intermittently (indicate how often) ❑ Continuously (indicate flow in CFS) Latitude of outfall: Longitude of outfall: Brief description of the industrial activities that drain to this outfall: Do Vehicle Maintenance Activities occur in the drainage are of this outfall? ❑ Yes ❑ No If yes, how many gallons of new motor oil are used each month when averaged over the calendar year? Page 2 of 7 3-4 digit identifier: Name of receiving water: Classification: ❑ This water is impaired. ❑ This watershed has a TMDL. Discharge from this outfall is from: ❑ Stormwater Only ❑ Wastewater Only ❑ Wastewater Comingled with Stormwater 7Q10 Flow of receiving waterbody (if discharging Wastewater Only or Wastewater Comingled with Stormwater to waters classified as HOW, ORW, Tr, WS-1, WS-11, WS-III, SA, or PNA): Discharge occurs from this outfall: ❑ Only during a rainfall event ❑ Intermittently (indicate how often) ❑ Continuously (indicate flow in CFS) Latitude of outfall: Longitude of outfall: Brief description of the Industrial activities that drain to this outfall: Do Vehicle Maintenance Activities occur in the drainage are of this outfall? ❑ Yes ❑ No If yes, how many gallons of new motor oil are used each month when averaged over the calendar year? 3-4 digit identifier: Name of receiving water: Classification: ❑ This water is impaired. ❑ This watershed has a TMDL. Discharge from this outfall is from: ❑ Stormwater Only ❑ Wastewater Only ❑ Wastewater Comingled with Stormwater 70.10 Flow of receiving waterbody (if discharging Wastewater Only or Wastewater Comingled with Stormwater to waters classified as HOW, ORW, Tr, WS-1, WS-11, WS-111, SA, or PNA): Discharge occurs from this outfall: ❑ Only during a rainfall event ❑ Intermittently (indicate how often) ❑ Continuously (indicate flow in CFS) Latitude of outfall: Longitude of outfall: Brief description of the industrial activities that drain to this outfall: Do Vehicle Maintenance Activities occur in the drainage are of this outfall? ❑ Yes ❑ No If yes, how many gallons of new motor oil are used each month when averaged over the calendar year? All outfalls must be listed and at least one outfall is required. Additional outfalls may be added in the section "Additional Outfalls" found on the last page of this NO]. 5. Wastewater Types of Wastewater facility will generate or discharge Vehicle & equipment cleaning (VE) ® Generate ® Discharge ® Sent to WW Treatment System Wetting of raw material stockpiles (RIM) ® Generate ® Discharge ® Sent to WW Treatment System Mixing drum cleaning (MD) 171 Generate x❑ Discharge ® Sent to WW Treatment System Facility will spray -down or actively wet aggregate piles © Yes ❑ No Page 3 of 7 6. Wastewater treatment alternatives What wastewaters were considered for this alternatives review: ® VE ® RM ® MD Are there existing sewer lines with a one mile radius: ® Yes ❑ No If Yes: ❑ The wastewater treatment plant will accept the wastewater. It is feasible to connect. Explain: ❑ The wastewater treatment plant will accept the wastewater. It is not feasible to connect. Explain: ® The wastewater treatment plant will not accept the wastewater (attach a letter documenting) ® Surface or subsurface disposal is technologically feasible ❑ Surface or subsurface disposal is not technologically feasible Explain: Surface discharge of treated wastewater is technologically feasible. ❑ Surface or subsurface disposal system is feasible to implement ® Surface or subsurface disposal system is not feasible to implement Explain: There is no available area within the facility for a potential surface disposal system. The volume of discharge will require a large system installed in a large area that is not available. In addition, the temporary nature of this facility makes the installation of such system not feasible. What is the feasibility of employing a subsurface or surface discharge as compared to a direct discharge to surface waters? Explain: Due to the temporary nature of this facility, direct surface water discharge of treated waste water is significantly more economically and environmentally feasible. Discharge to surface waters is the most environmentally sound alternative of all reasonably cost-effective options of the wastewaters being considered: 0 Yes ❑ No— contact DEMLR's Land Application Unit to determine permitting requirements If this review included all wastewater discharge types, would excluding some types make of the above non - discharge options feasible? ❑ Yes ® No 7. Other Facility Conditions (check all that apply and explain accordingly): ® This facility has a DMLR Erosion & Sedimentation Control Permit. If checked, list the permit numbers for all current E&SC permits for this facility: NcooT holds the permit ❑ This facility has a Division of Waste Management permit. If checked, list the permit numbers for all current DWM permits for this facility: ® This facility has other NPDES permits. If checked, list the permit numbers for all current NPDES permits: NCDOT Individual permit ❑ This facility has Non -Discharge permits (e.g. recycle permit). If checked, list the permit numbers for all current Non -Discharge permits: ® This facility uses best management practices or structural stormwater control measures. If checked, briefly describe the practices/measures and show on site diagram: ❑ This facility has a Stormwater Pollution Prevention Plan (SW PPP). If checked, please list the date the SWPPP was implemented: Page 4 of 7 ❑ This facility is subject to Phase If Post -Construction Area If checked, please list the permitting authority: ❑ This facility is located in one of the 20 Coastal Counties If checked, please indicate if the facility is adding more than 10,000 ft2 of built -upon area or is a CAMA Major Permit ❑ Will add more than 10,0000 ft of built -upon area ❑ Is a CMA Major Permit ❑ Yes to both ❑ No to both ❑ This facility is discharging wastewater to a stormwater BMP If checked, please indicate the permitting authority, and attach letter approval to do so: ❑ This facility has wastewater treatment facilities in the 100-year floodplain ❑ This facility stores hazardous waste in the 100-year floodplain. If checked, describe how the area is protected from flooding: ❑ This facility is a (mark all that apply) ❑ Hazardous Waste Generation Facility ❑ Hazardous Waste Treatment Facility ❑ Hazardous Waste Storage Facility ❑ Hazardous Waste Disposal Facility If checked, indicate: Kilograms of waste generated each month: Type(s) of waste: How material is stored: Where material is stored: Number of waste shipments per year: Name of transport/disposal vendor: Transport/disposal vendor EPA ID: Vendor address: ❑ This facility is located on a Brownfield or Superfund site If checked, briefly describe the site conditions S. Required Items (Application will be returned unless all of the following items have been included): ❑ Check for $100 made payable to NCDEQ ❑ Copy of most recent Annual Report to the INC Secretary of State ❑ This completed application and any supporting documentation ❑ A line drawing of the water flow through the facility. ❑ Copy of county map or USGS quad sheet with the location of the facility clearly marked ❑ Letter documenting that WWTP will not accept wastewater (if applicable) ❑ Approval from permitting authority to discharge wastewater to a stormwater BMP (if applicable) Page 5 of 7 ❑ Two (2) 24" x 36" site diagrams showing, at a minimum, existing and proposed: a) outline of drainage areas b) Stormwater/wastewater treatment structures c) Location of numbered stormwater/wastewater outfalis (corresponding to which drainage areas) d) Delineation of drainage areas to each discharge point e) Runoff conveyance structures f) Areas and acreage where materials are stored g) Impervious area acreages h) Locations(s) of streams and/or wetlands the site is draining to, and applicable buffers i) Site property lines, North Arrow, and bar scale j) If applicable, the 100-yearfloodplain line k) Acreage of each Stormwater and wastewater topographical area 1) Each of the facilities' wastewater or stormwater source and discharge structures and each of its hazardous waste treatment, storage, or disposal facilities m) Notation of the water quality classification of the receiving water that site waters eventually discharge to n) Site location (insert) 9. Applicant Certification: North Carolina General Statute 143-215.6E (i) provides that: Any person who knowingly makes any false statement, representation, or certification in any application, record, report, plan, or other document filed or required to be maintained under this Article or a rule implementing this Article ... shall be guilty of a Class 2 misdemeanor which may include a fine not to exceed ten thousand dollars ($10,000). Under penalty of law, I certify that: A I am the person responsible for the permitted industrial activity, for satisfying the requirements of this permit, and for any civil or criminal penalties incurred due to violations of this permit. 9 The information submitted in this NOI is, to the best of my knowledge and belief, true, accurate, and complete based on my inquiry of the person or persons who manage the system, or those persons directly responsible for gathering the information. X I will abide by all conditions of the NCG140000 permit. I understand that coverage under this permit will constitute the permit requirements for the discharge(s) and is enforceable in the same manner as an individual permit. ® I hereby request coverage under the NCG140000 General Permit. Printed Name of Applicant: David Chaparro Title: Project Manager DigWy signed by DaM M. Chapa DN: E=DMChapartoO1an�mftdmm, CN-David M. Chapa., OU=Users, David M. ChaparroDN-OoMorate,OU=NC,OU=Mid-SoNhRe&n, 12/30/22 DU= anec nsv d, DC-Ianeco Md, DC m Date' 2022,12,30 13 4937-0SOP (Signature of Applicant) (Date Signed) Mail the entire package to: DEMLR—Stormwater Program Department of Environmental Quality 1612 Mail Service Center Raleigh, NC 27699-1612 Page 6 of 7 Additional Outfalls 3-4 digit identifier: Name of receiving water: Classification: ❑ This water is impaired. ❑ This watershed has a TMDL. Discharge from this outfall is from: ❑ Stormwater Only ❑ Wastewater Only ❑ Wastewater Comingled with Stormwater 7Q10 Flow of receiving waterbody (if discharging Wastewater Only or Wastewater Comingled with Stormwater to waters classified as HOW, ORW, Tr, WS-I, WS-II, WS-III, SA, or PNA): Discharge occurs from this outfall: ❑ Only during a rainfall event ❑ Intermittently (indicate how often) ❑ Continuously (indicate flow in CFS) Latitude of outfall: Longitude of outfall: Brief description of the industrial activities that drain to this outfall: Do Vehicle Maintenance Activities occur in the drainage are of this outfall? ❑ Yes ❑ No If yes, how many gallons of new motor oil are used each month when averaged over the calendar year? 3-4 digit identifier: Name of receiving water: Classification: ❑ This water is impaired. ❑ This watershed has a TMDL. Discharge from this outfall is from: ❑ Stormwater only ❑ Wastewater Only ❑ Wastewater Comingled with Stormwater 7Q10 Flow of receiving waterbody (if discharging Wastewater Only or Wastewater Comingled with Stormwater to waters classified as HQW, ORW, Tr, WS-I, WS-II, WS-III, SA, or PNA): Discharge occurs from this outfall: ❑ Only during a rainfall event ❑ Intermittently (indicate how often) ❑ Continuously (indicate flow in CFS) Latitude of outfall: Longitude of outfall: Brief description of the industrial activities that drain to this outfall: Do Vehicle Maintenance Activities occur in the drainage are of this outfall? ❑ Yes ❑ No If yes, how many gallons of new motor oil are used each month when averaged over the calendar year? 3 4 digit identifier: Name of receiving water: Classification: ❑ This water is impaired. ❑ This watershed has a TMDL. Discharge from this outfall is from: ❑ Stormwater Only ❑ Wastewater Only ❑ Wastewater Comingled with Stormwater 7Q10 Flow of receiving waterbody (if discharging Wastewater Only or Wastewater Comingled with Stormwater to waters classified as HQW, ORW, Tr, WS-I, WS-II, WS-III, SA, or PNA): Discharge occurs from this outfall: ❑ Only during a rainfall event ❑ Intermittently (indicate how often) ❑ Continuously (indicate flow in CFS) Latitude of outfall: Longitude of outfall: Brief description of the industrial activities that drain to this outfall: Do Vehicle Maintenance Activities occur in the drainage are of this outfall? ❑ Yes ❑ No If yes, how many gallons of new motor oil are used each month when averaged over the calendar year? Page 7 of 7 •.:.LY515 r9-Y9RPB- POr Sia 29+76.:� 34-YSRPB- ST Sic. 27+41.87 b9S UTV6. LLC Y9.R6pC��g1&+7507 0 WTI K 0 I� ptv - oe wR Pc ssz M2K0��: 25 —c1 00 -_/ I I I T 1 3P BI .w w� \ >TEvrtrti� 0 R II ET AM N TaSTANDSU AH M MK a]M P03 PG0&a \ \ C W LT \ \ fc e3.oa Li. WE )a 00'LT. \ 63 35 GRAPHIC SCALE REraN 50 25 0 50 100 �"`�_ PLANS General Site Plar2022 I-40 Widening From I-85 IN Orange Co orL ales TIP PI I Lane e0o s I 0)WI + a 41 °_TA 1 = :'� '� • 400 cubic yard per hour production capabilities jor YEARS OF EXCELLENCE • Approved mix times in as few as 30 seconds • Self -erect setup as fast as 4 hours achieved using a 20 HP self-contained power unit • Open configuration allows for ease of maintenance and access to all plant components • Innovative plant and safety design features that evolve with the industry 'Estimated production based on industry standards, consult factory for details MC-11C MENEM Mobile Combo Self -Erect Central Mix Plant The ERIE MC-11C is the premier self -erect mobile central mix plant in the concrete industry. Equipped with a self-contained, self -erect hydraulic system, there is no need to erect the plant with a crane. FEATURES • 12 cubic yard highly mobile self -erect tilt mixer • 50 or 60 HP water-cooled high-speed mixer hydraulic system • Automatic central grease and mixer lubrication • Twin 75 HP crusher -duty TEFC drive motors • Heavy Duty Auburn M10B reducing units • Heavy Duty Duroxite mixing buckets and blades • 12 or 24 volt DC Emergency tilt system • 300 BBL to 700 BBL in -truss cement bin with dual 12" screw conveyors • Cumulative cement batcher • 4'/z HP aeration blower • 20 HP high -flow water pump with 4" feed line MNOE IN THE ;,91� DISTRIBUTOOR c ERIE STRAYER CO. 814.456.7001 1851 Rudolph Avenue www.eriestrayer.com Erie, PA 16502 sales@eriestrayer.com • 48" batch transfer conveyor • C&W central dust collection mounted on mobile mixer unit • 50 yard to 100 yard aggregate bin • Cumulative or individual aggregate batcher(s) • Telescopic test weight hangers • 15 HP Ingersoll-Rand air compressor • 20 HP self -erect hydraulic system • ERIE Liberty computer control system with manual panel • Automatic aggregate handling panel • Bin charging conveyors • LIL / CSA certified plant motor control panel CHARTER MEMBERS: AC PA r 0/ r 0 AEM NRMCA 30'-3" 1 1. 1-A 2-A 3-A 4-A BY ERIE STRAYER CO. MCi 7 C I AGGREGATE BIN 4 COMPARTMENT (PATT. Al I I I) 11 80 CU. YD. HEAPED CAPACITY HINGED AGGREGATE BIN EXTENSION Wl ONE REMOVABLE PARTITION 12 CU. YD. AGO BATCHING SYSTEM W/ FOUR INDIVIDUAL BATCHERS PLANT TRAVEL B SUPPORT FRAME 48" INCLINED BATCH TRANSFER CONVEYOR 45'-0" CIC W/80 H.P. DRIVE E1500 CU. FT. CEMENT BIN 19 CEMENT BIN SELF ERECT HYDRAULIC CYL. (2 REQ'D) 5" DIA. AIR LOADING PIPING FOR CEMENT BIN (4 REq'D) 12" DIA. INCLINED SCREW FEEDER W/ 50 H.P. MOTOR (2 RE(XD) 12 CU. YD. CEMENT BATCHER MIXER CHARGING CHUTE 12 CU. YD. ERIE TILT MIXER MIXERTRAILER MIXER SUPPORT SECTION MIXER SELF ERECT HYDRAULIC CYL (4 REQ'D) MIXER HYDRAULIC POWER UNIT LADDER TO MIXER PLATFORM (2 REWD) PLANT MOTOR CONTROL PANEL 1200 CU. FT. MOBILE FLYASH BIN W112" SCREW FEEDER FLYASH BIN SELF ERECT HYDRAULIC CYL. (2 REQ'D) 5" DIA. AIR LOADING PIPE FOR FLYASH BIN (4 REWD) PIVOTING MIXER NOSE PLUG 4" ELECTROMAGNETIC WATER FLOWMETER 25 H.P. AIR COMPRESSOR W1120 GAL. TANK 5 H.P. AERATION BLOWER (2 REQ'D) CENTRAL DUST COLLECTION SYSTEM SELF ERECT HYDRAULIC POWER UNIT MIXER MOTOR CONTROL PANEL AIR COMPRESSOR & PLANT MOTOR CONTROL PANEL MAINTENANCE PLATFORM W/ ACCESS LADDER CONTROL SYSTEM REMOVABLE PARTITION EXTENSION (3 REQ'D) CONTROL HOUSE CONCRETE DIRECTIONAL CHUTE W128" DIA. DISCHARGE OPENING AGGREGATE HANDLING PANEL POWER DISTRIBUTION PANEL FOR OPTIONAL AGGREGATE HANDLING ARRANGEMENT SEE 4A-265163.1 GENERAL NOTES BELOW APPLY TO EQUIPMENT SHOWN O ERIE STRAYER CO. -AGOREOATE BINSANO BIN COMPARTMENTS - POWER REQUIREMENT FOR CO 'LANT POWER °''� "0I*"'T 911 10 `O� 1`" 61�' V - 3PH - 60HZ MOBILE COMBO CENTRAL MIX PAVING PLANT ax w�nxc ro µ mcic or w nmx n¢ x0waxna Wm whau BINS, BIN RMENTSr AND ry va xur ms vm N. m.-M�RIF�IGOR O OR molnowN,el PROPOSAL P0877170EM7(REV3) CEMENT BINS. SIN N 1.. TMENRS ANO SILOS x]Usw° O0. vrvm IOMMx ro Tx9 G uuww wzaEL a». Nx mxvunxwrrxo M. wicmrsiv s�mxx IFO o°eNSTRUM N w'NWNTROL POWER LANE CONSTRUCTION CORPORATION NE Ill °x euuxc °"°" °" °' cv. M. °`" -xar ooR eausrnurnoN -ELEQrwe NoraRs ME ors 9,owr Wxea� MT V -1PH - fi0H2 uxus wmu�m Pmvasc iu vmwc xmuxs uE Nxeo m. zvisw gar. a rxw xw use � QxmRxs ro. ne 118"=1'-0" -- 4A-267059-3 BY ERIE STRAYER CO. X 75'-0" STACKABLE BIN CHARGING CONVEYOR W/ 10'-0" X 14'-0" AGG HOPPER (4 REQ'D) SINGLE PIN I BOLT 1 114' CIA. _ CONVEYOR HEAD ENO HEAD ENO SUPPORT LOCATION -AGGREGATE GINS AND GIN COMPARTMENTS -POWER REQUIREMENT FOROONTROS PLANTINOWER xcwm cwrrn.s or'rYaure ®as um Ew couP.im�Gm u¢ u R�o.x iwo xmTux -••• az 110 fi0V .iPH - 60HZ ax xruwD ro �w wxcic a mou nre xoimnNru Ylix wrzwi Dc Iron Pvt R. w DxE NVf 1Wrs P[n a. to -MODIFICATIONS OR ADDITIONS RDn aI, ro mE muwuOD sxDa++ SILOS -CYIN.. BINS, BIN COMPARTMENTS pND BILOB CEMENTN RTME TS AND I MPI9NG M 01HEA IDDIMN lD T16 FWIDY GYY PA¢i¢ 9W. BiN CDNPMIYGT YW SM1D UP.b116 h5 91DM xwxNGss CONTROL POWER u ... auw I. rc au ox Dn a. n. Pm euwv. O FO C STR CT[om -NOT FORGOMBTIIOCTION 20V•1 PH-60HZ • ELECTRIC MOTORS mxvmsE ul n[nwD Ymou ME'M mn rvx vo/4W wv. ] P�•-e m owws smPlu x N u¢ GvivYl DEIw, bN1 �NOY/.IFD OIPXHC SIMIING fCNP16Nf IxLL DE N0. Im ro aPEPAIE ox Nm YOIE LMO 2 2P M-4 5.4' AGGREGATE HANDLING ARRANGEMENT LANE CONSTRUCTION CORPORATION N'o' 4A-265163-1 E`YJ�Ii� u.s. osvuerwrtor sxzrrzxwx exsxzxs ircxz orxu suam 41, E)S'TOpo r i La =r n _ n .e y C/tu il .a q i � n r L2r � 1C`� t` �•_' ��a ��_}}+5�^'*a'�. �"E e_�y��i rn i s'� ��� tom"` z i� � <42v/'3' sls I, aid �e �✓�� - a� r���'"'s5r� ���� rX�jr�. '� ��_ � —` �. 1 — s � m , Utility Address Notification from Orange County GIS /Addressing/Land Records �528 0' 29 526 04� 8 i 133 o 527Igo • MgRy \ 1127 •123�9�9y tijO2FT�` • 2LN 121 • 113*'0109 1 117• •••'107 119 115 411� 350 �I:I:IIIIx!I:I.' 71IQ 7201-UT NC 86 S /40 wFNT266 oh/ i iA 40F Off, • 3700 0 0 This map contains parcels prepared for the ntory of real property within Orange nty, and is compiled from recorded deed, and other public records and data. Users of this map are hereby notified that the aforementioned public primary information sources should be consulted for verification of the information contained on this map. The county and its mapping companies assume no legal responsibility for the information on this m Well for Temporary Concrete Plant - Road Construction PIN 9880096500 New Address: 7201-UT NC 86 S Zipcode: 27514 - Chapel Hill Township: Chapel Hill 71201 V) W Britney Pendleton brpendleton@orangecountync.gov Orange County Tax Administration N GIS/Addressing/Land Records 919-245-2576 W E Date: 11 /22/2022 S PROJECT: 1-3306A Design Build DESCRIPTION: Concrete Plant Site SUBJECT/ TASK: Calculate Stormwater Runoff & Size Treatment System for Concrete Plant Yard CALCULATED BY: DMC DATE: 12/5/2022 —, __... _. Calculate Stormwater Runoff at proposed Concrete Yard then select and size the appropriate erosion control BMP's. Calculate Time of Concentration (t j tc _ [C/Hju-685/128 (Malcom) L = 673 Ft. Hydraulic length of watershed H = 15 Ft. Elevation change along length tt= 5.1 Minutes Minimum tc = 5 minutes tc (min) = 5.0 Minutes Use Minimum tc: calculate PeaK How Kate I Q) Q =CiA Impervious Area C = 0.9 *Rational Coefficient - Table 1.6 NCDOT Design Manual 1= 6.97in/hr *Rainfall Intensity- Appendix A NCDOT Design Manual Raleigh, NC - 10yr, 5-Minute Storm A= 0 AC Drainage Area, Impervious Q Imp = 0 CPS Pervious Area C= 0.5 *Rational Coefficient - Table 1.6 NCDOT Design Manual *Rainfall Intensity - Appendix A NCDOT Design Manual i = 6.97 in/hr Raleigh, NC - 10yr, 5-Minute Storm A= 2.2 AC Drainage Area, Pervious Q Per 7.67 CPS Q10TOt,l = 7.67 CFS Drainage Area = 2.2 AC Select Skimmer Basin *(NCDOT BMP Selection & Design Criteria Chart) t.aicmace oasm uesign mimmums Storage Volume= 18000F/AC *NCDOT Guidelines Min. Capacity = 3960 CIF Surface Area = 325Q10 SF *NCDOT Guidelines Min. Surface Area = 2491.775 SF Size Selected BMP Basin Length: 90 Ft Width: 30 Ft Depth: 3 Ft (At Weir) Side Slopes: 2 :1 (H:V) SURFACE AREA = 2700 SF RETENTION VOLUME = 6084 DEWATER BASIN Bottom Dimensions Length: 78 Width: 18 * Skimmer Requires Minimum 3:1 L:W Ratio Basin Size is: Good Basin Volume is: Good - Pg. 2 Depth to Dewater 2 FT Volume to Dewater: 4,056 CF Basin to Dewater in: 3 Days * NCDOT Guidelines Outflow= 1352 CF/Day SELECT SKIMMER Skimmer Size = 1.5 Inch * Faircloth Skimmer Selection Chart H = 0.125 SIZE ORIFICE D = 1.29 Inch D = SQRT(Q/(2310SQRT(H))) R = 0.64 Inch SELECT BARREL SIZE Qbarrel= 7.02 GPM 4" Barrel will Suffice * Figure C-1 (NCDOT Manual) EMERGENCY SPILLWAY Spillway Width: 22 Ft Confirm Suitability with 8.67 FT Weir Equation: COMPLETED STORMWATER BASIN DESIGN Basin Size: Basin Drainage Area: Skimmer Size: Orifice Radius: Outflow Barrel: Spillway Width: * NCDOT Method (Basin Width - 8') 90Ft x 30Ft x 3Ft 2.2 AC 1.5 IN 0.64 IN 4 IN 22 FT GOOD - Pg. 3 Waste Water Treatment Plan 1 - Background The Lane Construction Corporation has been awarded the NCDOT contract for the reconstruction of a portion of Interstate 1-40 in Orange County, NC. This project requires that approximately 150,000 cubic yards of concrete be produced and placed into the new roadway. In order to facilitate this construction, a temporary portable concrete batch plant will be erected within the Right of Way of the project at a parcel of land located at Highway NC 86 (intersection with 1-40). Please refer to the location maps provided within this application. The concrete plant that is being proposed in this application will exist solely to provide concrete for the above -referenced project. The concrete plant will only be active during intervals of concrete paving. Upon the completion of concrete paving, this plant will be removed and the site will be repurposed. 2 - Waste Water Generated There will be three different types of waste water generated at this site which need to be analyzed. The first will come from the cleaning of the concrete hauling units. Dump trucks will be utilized to haul the wet concrete and will need to have their dump bodies rinsed out after each load. This water will combine with the concrete that is rinsed out of the dump body and will contain all the elements of the concrete (Sand, Stone & Cement). No other cleaning or repair of these vehicles will occur at this site. The second waste water generated will be the wash water produced after cleaning the plant's mixing drum. The composition of this water will be the same as that produced during the dump truck rinsing operation. This cleaning of the mixing drum will occur upon of the completion of each shift and also as necessary throughout the shift. The third waste water generated will be the water used to wet the raw aggregate stockpiles. These stockpiles will be watered consistently during concrete production operations. Water that flows from these stockpiles will contain suspended fine particles that have escaped from the stockpiles. 3 - Waste Water Control & Treatment In order to effectively treat the wastewater generated by this setup, it must first be collected and brought into the appropriate containment areas. The wastewater basin is intended to collect the wastewater described in Item 2 of this document. Additionally, there is a stormwater basin intended to capture the stormwater run-off from a portion of the site. The site will be graded and diversion ditch lines will be established.to ensure that the wastewater and stormwater will flow as intended. The Concrete Wash Water will be introduced into a series of basins designed to effectively settle all suspended particles and also to ensure that the pH of the outflowing water is within the acceptable range. To do this, three basins will be created. The first basin in the series is the "Washout Pit" where the dump trucks will.be sprayed and the concrete will be directly mixed into the system. This is also the location where wash water from the mixing drum will be transported to. The second basin is designed to be the "Settling Basin" which is a very large retention basin sized to provide adequate settling time to ensure that the fine particles have settled out prior to outflowing into the final basin. The third basin is the "pH Reduction Basin" which is where a Fortrans System will be installed to monitor and regulate the pH of the wash water. As an additional measure and to increase the safety factor of the system, the water coming out of the stormwater basin will be diverted to the pH control basin to ensure this source is also within acceptable levels. Predicted Maximums and System Performance The concrete wash water treatment system has been designed for a concrete plant running at a regular maximum production of 2,000 CY per day. This volume will result in a wash water flow of approximately 2,420 CF/Day. In actuality, this production rate will only be achieved a limited number of times on this project. However, it is important to calculate the waste water treatment system based upon the project maximums and not the averages. Upon release from the treatment system, the TSS and SS levels in the outflowing water will be less than the established limits (30 mg/I and 5 ml/I respectively), and the pH will be within the acceptable 6-9 range. Maintenance of System Basins and BMPs will be inspected regularly, and documentation made in accordance with the facility SWPPP. Any damage to the devices will be repaired immediately and any sediment that has been built up will be removed routinely. This system has been designed to allow for easy access and maintenance which will help to ensure that it functions properly. During intervals where the concrete plant is active the wash water basins will be inspected on a daily basis. It is anticipated that at a minimum the "Washout Pit" will require routine cleaning during these intervals. The aggregates that will accumulate in this basin will begin to impact the function of the system if they are allowed to build up. It is the responsibility of Lane to ensure that this buildup of materials is removed on a timely basis. Summary The purpose of this treatment system is to monitor and control pH and settle TSS resulting from concrete washing operations before it leaves the site. This treatment system has been used successfully at previous sites for concrete batch plants, most recently this exact treatment methodology was used for similar NCDOT projects in Guilford County (Contract Nos. C203197, C 203399, and C203792). The rules and guidelines set forth by general permit NCG 140000 will be strictly adhered to and BMP's will be employed and maintained. Any questions regarding the operation of this facility can be directed to the facility contact noted in the application. PROJECT: C204632 DESCRIPTION: 1-40 Project Orange Co. SUBJECT / TASK: Calculate "Wash Water" Volume from Concrete Plant Operations & Design Treatment System CALCULATED BY: DMC DATE: 12/7/2022 Lane has proposed to construct and operate a temporary portable concrete batch plant to facilitate the construction of the above referenced project. Given the provided technical information regarding concrete plant operations, specific to this plant and project, the volume of "Wash Water" needs to be calculated and a treatment system needs to be There are two sources of "Wash Water." The first being the water used to wash out the beds of the wet batch hauling concrete dump trucks after each load. This operation is completed by spraying the truck bed with a fire hose. The wash water then flows from the truck bed into the washout pit. Once the washout pit fills, washwater will be skimmed from the surface with a pump and reused to spray out truck beds. (This is done as a water conservation effort.) The second source of wash water is the water that is used to clean the plant's mixing drum upon completion of each shift and as needed throughout the shift. This operation is completed by spraying the drum, letting it mix then dumping the wash water into a loader bucket for transport to the washout pit. TRUCK CLEANING WASH WATER Estimated Maximum Concrete Production per Day: 2000 CY Average Load Size: 10 Cy Number of Loads per Day: 200 Time Spent Cleaning Truck Bed per Load: 70 Seconds* Typical Fire hose flow Rate for this plant setup: 100 GPM Total Wash Water Needed Per Shift: 23,333 Gallons Fresh Wash Water Introduced to System: 17,500 Gallons * ( 75%Fresh Water) Wash Water "Recycled" from Wash Pit: 5,833 Gallons * ( 25%Recycled Water) Truck Cleaning Wash Water 3 Introduced to System per Day: 2,339 ft DRUM CLEANING WASH WATER Estimated Cleaning Cycles per Shift: 2 EA Amount of Water Used per Cycle: 300 Gal Total Wash Water Produced: 600 Gallons Drum Cleaning Wash Water Introduced to System per Day: 80 ft3 TOTAL WASH WATER INTRODUCED per Day: 2,420 ft3 ( * Denotes Information Provided by lane Construction, based on project projections and past m( Calculate composition Wash Water Estimate Amount of Waste Concrete Volume of Waste Concrete Washed out of Haul Trucks (Per Each): 100 Lbs. * * Provided by Lane Construction, based unnn mah maaonromnnhe and ru�unh Page 1 of 8 �r�ro.,. Volume of Waste Concrete Washed ........ out of Mixing Drum (Per Each): 125 Lbs. ` experience in North Carolina. Total Waste Concrete Dumped 20,250 Lbs. into Washout Pit per Day: Typical Mix Design for this Plant Setup: Cement: 14% Fine Agg: 29% Course Agg: 49% Water: 8% Amounts of Waste Materials Introduced into Wash Water Cement 2,754 Lbs. Fine Agg: 5,873 Lbs. Course Agg: 9,923 Lbs. Water: 1701 Lbs. _ ' Provided by Lane Construction, based upon recent History in North Carolina. 204 Gal Page 2 of 8 ana uetan of i reatment The Wash Water will contain waste concrete and as such there will be Suspended Solids. Concrete is a mixture of Course Aggregate (Stone), Fine Aggregate (Sand), Cement and Water. The aggregates will settle out of the wash water almost instantly and be deposited at the base of the system. However, the cement will require a much greater settling time due to its average particle size being quite small. It is the cement particle that this water treatment system is designed for. As detailed on the plan sheet, this system will employ three basins which will work in series. The first basin is the "Washout Pit" which is where all the aggregates will settle out of the wash water, leaving only the cement particles to flow into basin 2 which is the "Settling Basin." The "Settling Basin" is where the fine particles (Cement) will settle out of suspension. As designed, this basin is to have a 4:1 Length to Width Ratio in order to maximize the amount of time required for wash water to flow through the basin. From the "Settling Basin" the wash water will move into basin 3 which is the "PH Reduction" basin. Since cement is very alkaline (pH 12-13) it is necessary to monitor and control the wash water prior to it's release from this system. A "Fortrans" system will be setup at basin 3 which will ensure that pH levels are acceptable prior to release. (Please seethe manufacturers specifications, which are included in the Appendix, for details and performance expectations) It is also noteworthy that each basin will be connected by a "Rock Sediment Dam." These BMP structures employ wide weir's which allow for a thin layer of surface water to slowly move between each basin. The main purpose of a sediment dam is to "skim" the surface water (cleanest water) from the upstream basin and allow it move on to the next basin in the series. This "skimming" characteristic is essential for the proper operation of this system. It essentially works to trap the smallest particles (cement) that are suspended in the wash water. These tiny cement particles range in size with its smallest particle being only 1 Micron in diameter. The retention time required to completely settle out a 1 Micron particle is extremely difficult to provide. However, creating a system that traps these minute particles is much more feasible. This system is designed to trap suspended particles in each basin, the smallest of which will be trapped and eventually settled out in basin 2, the "Settling Basin." Page 3 of 8 BASIN 1- "WASHOUT PIT" Select Treatment Device (BMP Device) TRSD -Type B Size Selected BMP Basin Top Dimensions Length: 20 Ft Width: 20 Ft Depth: 3 Ft (At Weir) Side Slopes: 2 :1 (H:V) SURFACE AREA= 400 SF RETENTION VOLUME= 624 CF WEIR LENGTH = 10 Ft BASIN 2 - "SETTLING BASIN" *NCDOT BMP Selection & Design Criteria Chart for Application -(Settle Aggregates) Bottom Dimensions Length: 8 Width: 8 Basin Volume is: Good Best Fit I Select Treatment Device (BMP Device) *NCDOT BMP Selection & Design Criteria Chart Best TRSD -Type B Fit for Application - (Sized Large to provide extended retention time to facilitate settling of Small Particles) Size Selected BMP Basin Top Dimensions Length: 140 Ft Width: 40 Ft Depth: 3 Ft (At Weir) Side Slopes: 2 :1 (H:V) SURFACE AREA = 5600 SF RETENTION VOLUME = 13664 CF WEIRLENGTH= 10 Ft DAJIN 3 - Yn KCUUII IUN CA]IN Select Treatment Device (BMP Device) TRSD -Type B Size Selected BMP Basin Top Dimensions Length: 50 Ft Width: 30 Ft Depth: 3 Ft (At Weir) Side Slopes: 2 :1 (H:V) SURFACE AREA = 1500 SF RETENTION VOLUME = 3197 CF WEIR LENGTH = 10 Ft Retention Time Pri Basin One Bottom Dimensions Length: 128 Width: 28 Basin Volume is: Good *NCDOT BMP Selection & Design Criteria Chart for Application - (Provide Surface Area) Bottom Dimensions Length: 38 Width: 18 Capacity Offered: 624 CF Basin Volume is: Good Best Fit Page 4 of 8 Volume of Wash Water: 2,420 CF/DAY Retention Time: 0.26 DAY Basin Two Capacity Offered: 13664 CF Volume of Wash Water: 2,420 CF/DAY Retention Time: 5.65 DAY Basin Three Capacity Offered: 3197 CF Volume of Wash Water: 2,420 CF/DAY Retention Time: 1.32 DAY TOTAL: 7.23 DAY netenuon i ime negwrea to beive the Average cement rarticie Particle Settling Velocity Average Diameter of Cement Particle 1 micron Average Diameter of Cement Particle Density of Cement Density of Water Viscosity of Water Gravity Settling Velocity for Average Cement Particle: Depth of Settling Basin: Settling Ti me for Avg. Cement Particle: 0.15 Days < - V=gd2(Pi-P2)/18µ 15 microns 3.28E-06 Ft 4.92E-05 Ft 94 Ib/ft3 62.4 Ib/ft3 5.98E-04 If/ft-sec 32.2 ft/secz 2.29E-04 ft/sec 3 Ft 13,106 Sec. _ 0.26 Days Therefore: The average Cement Particle will settle out of the wash water in the "Washout Pit." This will leave only the smallest of particles to analyze in the "Settling Basin." 3.64 Hours = 0.15 Days Page 5 of 8 beinement or Particles too Fine to Completely Settle Out Realistically most of the suspended cement particles have settled out in the Washout Pit. Then, an additional amount of suspended cement settled out at the Rock Sediment Dam. However, for an increased factor of safety the analysis of basin 2 is to be performed with the assumption that all suspended cement has passed from basin 1 into basin 2. •.emem araul nae uisuiouuon NIJI Diameter (microns) Size dlStrlbU[IOn `e < Amount in System (Lbs) Diameter (Ft) Settling Velocity (Ft/Sec) Time settle to Bottom off Basin (Days) 1 4.7 4.7 129.44 3.28E-06 1.02E-06 34.13 1.5 2.6 7.3 71.60 4.92E-06 2.29E-06 15.17 2 4.8 12.1 132.19 6.56E-06 4.07E-06 8.53 2.5 2.8 14.9 77.11 8.20E-06 6.36E-06 5.46 3 2.8 17.7 77.11 9.84E-06 9.16E-06 3.79 4 4.6 22.3 126.68 1.31E-05 1.63E-05 2.13 6 7.6 29.9 209.30 1.97E-05 3.66E-05 0.95 8 6 35.9 165.24 2.62E-05 6.51E-05 0.53 12 10.5 46.4 289.17 3.94E-05 1.46E-04 0.24 16 8.2 54.6 225.83 5.25E-05 2.60E-04 0.13 24 13.8 68.4 380.05 7.87E-05 5.86E-04 0.06 32 10.3 78.7 283.66 1.05E-04 1.04E-03 0.03 48 12.4 91.1 341.50 1.57E-04 2.34E-03 0.01 64 5.2 96.3 143.21 r 2.10E-04 4.17E-03 0.01 96 2.8 99.1 77.11 3.15E-04 9.38E-03 0.00 U. 0.4 99.5 11.02 4.20E-04 1.67E-02 0.00 >128 0.5 100 13.77 Total Settling Time Provided by Basin 2: 5.65 Days * Calculated Previously Therefore: 2 Micron sized particles are the largest that might not completely settle out. These particles will need to be "Trapped" to prevent them from moving on. Nequlrea to tttectlyely " I rap" Suspenaea Particles Depth of Basin (At outlet Weir): 3 Ft Length of Basin: 140 Ft Assuming that flow is spread equally across width of basin (Baffles should ensure this) settling time of suspended particles will have a linear correlation to Basin Length. For an added factor of safety assume that all suspended particles need to have settled at least one third of the total weir depth to be considered effectively "trapped." Settled depth of Smallest "Trapped" Particle (1 Micron) at Weir: 0.5 Ft Retention time required to settle a 1 Micron particle to this depth: 5.69 Days Page 6 of 8 Calculate Amount of Suspended Cement Settled and Trapped in Settling Basin Diameter (microns) Amount of Suspended Cement Introduced to System (Lbs.) %of Settling Time Achieved by Basin Amount of Suspended Cement Settled to Bottom (Lbs.) %of Trapping Time Achieved by Basin N Amount of Suspended Cement Trapped in Basin (Lbs.) 1 129.44 16.55% 21.42 99.28% 107.08 1.5 71.60 37.23% 26.66 100.00% 44.95 2 132.19 66.1891 87.49 100.00% 44.70 2.5 77.11 100.009/ 77.11 100.00% 0.00 3 77.11 100.009/ 77.11 100.00% 0.00 4 126.68 100.00% 126.68 100.00% 0.00 6 209.30 100.00% 209.30 100.00% 0.00 8 165.24 100.00% 165.24 100.00% 0.00 12 289.17 100.00% 289.17 100.00% 0.00 16 225.83 100.00% 225.83 100.00% 0.00 24 380.05 100.00% 380.05 100.00% 0.00 32 283.66 100.00% 283.66 100.00% 0.00 48 341.50 100.00% 341.50 100.00% 0.00 64 143.21 100.00% 143.21 100.00% 0.00 96 77.11 100.00% 77.11 100.00% 0.00 128 11.02 100.00% 11.02 100.00% 0.00 >128 13.77 100.00% 13.77 100.00% 0.00 2754.00 2556.33 196.73 0.94 Amount of Suspended Cement Passing out of Settling Basin (Lbs.) 0.94 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Calculate Amount of Suspended Cement Settled in Basin 3 Diameter of Suspended Cement Time Cement Settled TimeAchieved Cement Trapped In (microns) Introduced to Achieved by to Bottom by Basin Basin (Lbs.) System (Lbs.) Basin (Lbs.) 1 0.94 1.5 0.00 2.5 0.00 3 0.00 Amount Of %of Amount of Suspended Settling Suspended %of Trapping Amount 0.94 0.00 0.00 0.94 Contribution of Basin 3 not counted towards reduction of Suspended Cement for two reasons: 1 Effects of Fortran System circulating Water may reduce settling effectiveness. 2 Any Settlement Achieved in basin 3 will add to overall factor of safety for this system. Amount of Suspended Cement Passing out of Settling Basin (Lbs.) 0.94 0.00 0.00 0.00 0.00 0.00 0.00 Page 7 of 8 Laicuiaie maximum ually 155 Levels In outtlowing Wash Water Total Suspended Cement Discharged from System: Water Discharged from System: Amount of Suspended Cement in Outflowing Wash Water: 1 mg/L = Daily TSS: Maximum Allowable per NCDENR Regulations: SYSTEM IS: 0.94 Lbs. 18,304 Gal 5.13E-05 Lbs./Gal 8.34538E-06 Lbs./Gal 6.14 mg/L 30 mg/L Acceptable Page 8 of 8 F'"OkRTRANS M CONTROL SYSTEMS CONCRETE REMOVERS Copyrighted information The Model 5000 series pH Control systems use a patented Dif-JetTM non -fouling carbon dioxide gas diffusion and injection process to lower the pH of process water and or storm water at ready mix concrete plants, and precast concrete manufacturing operations. These systems also lower Total and Suspended Solids to low levels. The programmable logic controller in the system can be set to lower the pH to almost any end point. The controller is pre-set to maintain a pH of 7.5 in the detention basin. The system is installed on a 10'x 10' concrete pad adjacent to the pit, basin or tank with the cleanest, most settled water. The system circulates the water in the containment basin with a submersible pump in a closed loop piping system and continually monitors the pH level. When the pH rises to 8.25, the controller will actuate a solenoid valve and begin to diffuse and inject carbon gas. Once the water is at a pH of 7.5, the valve shuts off and the water circulates until the pH rises to 8.25 again. The range may be adjusted to the owner's preference. For example, the "on" set point can be set to 7.5 and the "off' set point can be 7.0 for a lower tighter range. High pH process water contains a high levels of suspended and dissolved solids, primarily calcium hydroxide. The carbon dioxide forms carbonic acid when it is dissolved in water, the reaction between the carbonic acid and calcium hydroxide forms calcium carbonate which is insoluble in water and precipitates out of the water. Typically, the 'Total Suspended Solids" reading will be from 14 to 17 after pH adjustment. The EPA permits discharge of treated process water when the pH is 9.00 or lower and the TSS (Total Suspended Solids) is under 30. As part of a water recycling program, the treated water may be used to batch concrete, for dust control, truck washing and irrigation of lightweight aggregate or release from the property according to the storm water permit for the plant. The treated water may also be returned to the municipal waste water system. pH adjusted water does not scale up windshields or paint. It will not scale up pumps, valves or fittings so maintenance costs are lower compared to using high pH process water to batch concrete. Also, having a basin or pit of pH adjusted water will generally help in managing stormwater as the "buffered water" will neutralize most of the stormwater that enters the basin. These systems are useful for treating and maintaining stormwater containment to avoid discharging high pH water. Carbon Dioxide costs about .29 lb delivered. Typical CO2 cost will be around $6.00 per day per 10,000 gallons of high pH water. This figure may vary depending on the actual pH and total alkalinity of the process water, The systems include everything needed to operate except the CO2 supply and tank. Fortrans supplies a Victor SR-31-320 high flow CO2 regulator and nylon supply hose. The final 115V- 20 A electrical connection is by others. A small amount of schedule 80 PVC piping and fittings to construct the return outlet per our supplied drawing will also be required. Fortrans does not recommend "batch treating" of process water. Once the system is installed; run continually during plant operating hours. The system will not use more CO2 than if batch treating and scaling in piping and lines will be greatly reduced. The Model 50005, 50008 and 5000SK all have the capacity to treat up to 75,000 GPD. The systems are supplied with operation manuals that contain detailed operating and maintenance instructions, installation instructions and drawings that show how to set up the pump and pump boom and how to install the discharge piping Comoetitive Information The Model 5000S pH Control Systems cost approximately 60 to 70% Tess to purchase and operate than acid based neutralization systems. The cost savings is based on using less pounds of CO2 than sulfuric acid or hydrochloric acid. Sulfuric Acid based systems or sodium bisulfate systems will increase Total Suspended Solids. A separate filter will be required to meet EPA standards for discharge. Fortrans' systems do not use corrosives, all of the components last longer. No. hazardous chemical permits are required. All systems are ouaranleed to perform to our customer's satisfaction F"T"RTRANS •. �4rw\{r��\Yl n.Fr{MMNr{1 IN$, ALLAJ Q LJN5JR"_JQii5 MODEL SOOOB MODEL 5000SK PH CONTROL SYSTEMS WARNING: DO NOT LOCATE CO2 CYLINDER]. TANKS OR REGULATORS INSIDE ENCLOSURE! TURN OFF THE CO2 SUPPLY VALVE BEFORE WORKING IN THE SYSTEM 1 8 X 8 concrete pad for enclosure 2 Dewar s type 400 lb Tanks or Micro Bulk tanks 50 D hgn pressure CO2 cylinders are also acceptable 3 A Victor Model SR-310-320 high flay- lair pressure CO2 regulator should be used with the system 4 Do not use CO, welding regulators They do not have enough now to support the system 5. 115V-20 Amp electrical connect on to disconnect on rear of system or bad center in control panel for Model 500OSK 6 10 of 2' diameter schedule 80 PVC pipe - 2' Schedule 80 Female adapter and 2' Schedule 80 elbow "ing 12 required) 7. Clean out pit or basin being treated before commencing operation. Do not place pump or discharge Into slurry layer In basin. INSTALLATION IN$TUCTIONS: 1 Place panel on concrete pad and level with shims Fasten steel L brackets to concrete pad and Tex 4X4 base tot stability Connect 115V- 20 AMP electrical service to disconnect on the back Not applicable to Model 5000SK The SK system requires 115V 20 AMP electric service to the load center on the control panel. Mount control panel on wall Install the supplied %' hose to hose fitting on solenoid valve and then to the hose fitting on the Dd-Jet gas injector 2 Connect hose to regulaor and then connect to :' NPT fining on bottom rear of CO2 flow meter Remove now, meter bracket for easy connection A 75 lb pressure relief valve is installed on the CO, line Do not Install a check valve in the line from the CO2 regulator to the solenoid valve. 3 A check valve has been installed on the Dd-Jet^' injector to prevent any back now Use CO2 pas to operate the system. Do not use liquid CO2. 4 The operating pressure should be set at 18 — 25 PSI Do not exceed 30 PSI Check for CO2 leaks using a soap and water solution Check for leaks at tank and all inside fittings after every CO2 delivery Small CO2 leaks are very cosity Ensure that the nylon flat washer is installed on me regulator If regulator -ices' up quicklythere is a CO, leak 5 Screw (use Teflon tape on threads) pH probe into the IA' bushing installed in the Y shaped probe holder on the discharge line Hand Ugrian probe 6 Connect the wires from the pH probe to the 'green' pm terminal on the rear of the Sip down panel A winng diagram is included inside the box the probe was shipped in 7 pH probe has been calibrated at the factory It should be re -calibrated every week. See laminated mstruoUon sheet for step-by-step calibration instructions Cut breaker to pump or unplug pump when calibrating Nor, Ensure that pit probe Jeee n , freeze A 200'Nnn panel heater q inslelled in 5000E models FORTRANS INC. 7400 8 Siemens Road - PO Boa 40 - Wendell, NC 27591 •919-365-8004. 865958-7267 • www.fortransinc.com F"TRANS re CPNiaPI SvsnuS rONOIln REW"IMi - - - 8 Catalog S 2866-L pH 4 01 buffer and catalog If 2881-L pH 7 buffer Binds are included Purchase a gallon bottle of distilled water for rinsing probe and small plastic cups for calibrations HOSE CONNECTIONS. 9 Suction or inlet and dischargeroutfet quick connect fittings are pre-mstalled in rear of the unit- DO NOT INSTALL A 90° ELBOW ON THE DISCHARGE PIPING AT THIS LOCATION. Use supplied hose for discharge, do not hard pipe. 10 Construct discharge piping per our drawing and install in pre or basin. The discharge should not be placed In any Slurry present In the pit or basin. Fabricate discharge line per installation drawing detail to ensure discharge flows parallel to surface of water not down Into bottom of basin. i 1 Connect the suction hose to the hose barb on the submersible pump a heat gun is required Fasten the other and to the quick connect filling marked -suction in rear of unit Conned return/discharge hose to the quick connect fitting in rear of unit Fasten the 6' length of hose to the discharge fitting on rear of system and then connect the 19length to n. The short length is for easy cleaning if hose scales up 12 Install supplied pump boom Place the submersible pump in the basin above any slurry, Plug pump power cord into to the back of the Boat switch plug into the GFCI Pullet on rear of unit On Model 5000SK units the receptacle is furnished loose, the bell box. GFCI receptacle and 4 W deep weather proof cover are to be installed by customer 13 Install alarm light bulb and red cover. On Model 5000SK systems install the alarm light on exterior of owner supplied enclosure and wire to relay C in controller. 14 The controller is preset at factory to activate the normally dosed solenoid valve to teed CO, if pH is over 8 25 It will feed CO2 gas until the pH reaches 7.5 The pump continually circulates the water. When the pH reaches 8 25, the controller restarts the CO, feed automatically. Preset PH range is 7 5 to 8 25 15 The solenoid valve will cycle on for 60 seconds and off for 30 seconds while feeding CO2 to ensure the regulator does not ice up Cycle bores are easily changed for field conditions. 16 The alarm light will turn on if the pH exceeds 9.0 or if the pH is lower than 6 5 17 If System is slow W lower pH, ensure that the regulates is a high now design similar to a Victor model SR-3 to. 320 and not a CO2 welding regulator 18 Once pump has been turned on Check the water lbw meter Depending on head pressure the system should be operating at 45 to 70 GPM Check the :low meter on a regular bass to ensure flow G maintained. If Bow begins Dropping, check discharge hose for scaling and Check pump to ensure it is not clogged or scaled up FOR SUPPORT CALL 856-958-7267 or 919-365-8004 FORTRANS INC. 7400 B Siemens Road • PO Box 40 • Wendell, NC 27591 •919.365.8004. $66-958-7267 - www.fcaransmccom ENGINEERS CERTIFICATION OC THE MODEL 5000-5 PH MONITORING AND CONTROL SYSTEM Ay: G.C. Environmental, Inc. P.O. Box 40125 Raleigh, NC 27629 For. Fortrans Inc. P.O. Box 40 Wendell, NC 27591 Dated: September 11, 2003 G. C. Environmental, Inc. 5312 Pinewood Court Wendell, NC 27591. (919)266-2864 Scptcanber 11, 2003 PURPOSE G.C. Environmental, Inc., was contracted to provide an engineers review and certification that the Model 5000-S pH Monitor and Control System manufactured by Coastal Carolina Supply in Morehead City, NC, could cffectivelyprovide on a continuous basis, an average pl-1 range of6-9 units on the supernate layer of a stormwater/rinse water sedimentation basin typically found at Redi-mix concrete facilities. SCOPE OF WORK During theweck of August 11, 2003, G.C. Environmental, Inc., witnessed the operation oftlte Model 5000-5 self-containcdpH Monitoringand Control System ata Rcdi-mix plant located in Durham, NC. During the two (2) day test program, measurements were made within the facilities :normwatcr/rinse water sedimentation basin for pl-1, temperature and depth (both supernateand sludge). DuringthefirsL day of testing, the basin was (found to be heavily loaded with solids and adjustments were made to the solids blanket to complete testing the following day. TEST M ETHODOLOGY A primary sedimentation basin located at a Red! -mix concrete plant located in Durham, NC was treated utilizing the Model 5000-5 pH Monitor and Control System, During the test program, the basin .vas, on a semi -continuous basis, being fed rinse water from the exterior cleaning or cement trucks. Measurements for pH, temperature, supernate and sludge blankets were made within the sedimentation basin. Initial pH measurements showed pl-I levels of at least 12.0 units. The sedimentation basin was rectangular in shape with concrete walls and bottom. The basin ranged in depth oft ° at the inlet to approximately Y atthedeepest point. Sludge measurements within the basin showed that at least 213 of the basins depth was comprised of sludge and the remainder supernate. TheModc15000-S pl-I Monitor and Control System Was setup at the rectungularsedimentation basin with the intake and discharge hoses situated at opposite ends of the basin. Both the intake and discharge lines were set at depths within the supernate layer orthe basin. A clockwise flow pattern was established once the unit began operation and pl-I and temperature measurements were made at several locations throughout the supernate layer of the sedimentation basin. Approximately eighteen (18) pl-I and temperature measurements were collected with it mean pH value of SSG and mean temperature values or30 94 °C. The pH system was left to run essentially on a continuoushacis over a four (4) hour period. An estimated volume existing within the sedimentation basin was 25, 000 gallons with a little over 8000 gallons consisting of relatively clear Supernate. The amount of 25% Sulfuric acid (H,SO,) used to treat the sedimentation basins supernate was approximately 18-20 gallons. MODEL 5000-S Pit MONITOR AND CONTROL SYSTEM The model 5000-S pH Monitor and Control System is comprised ofa Hayward Power plow 11 (3/4 hp, 56 GPM) centrifugal pump which delivers raw water to a completely contained pH sensor connected to a pF1 meter equipped with control relays which operate two (2) stenner (60 GPD) acid injection pumps. The acid 25% H,SO4 is injected into the pump discharge line which empties into the sedimentation burin. Sulfuric acid is delivered to the system by 15 gallon carbuoys located outside of the fiberglass weatherproofenclosurc which houses all ofthe aforementioned equipment. On top of the enclosed is an alarm lightwhich is tied into the pH meterwhich is activated when pH levels exceed 8.5 pH units or are below 6.0 units. CONCLUSION 1. The Model 5000-S pH Monitor and Control System is an effective system for the pH balancing of sedimentation basins which are used to collect stormwater runolfand rinse water, commonly found at Rcd-mix concrete plants. 2. During the test program an average pH of 8.54 units was measured in the subject sedimentation basin with a range of 7.95 to 9.34 measured. 3. Sludge levels existing within the rectangular sedimentation ranged from 6.0 inches to 2.0 feet. PH' values after pH stabilization at the sludgetsupemate interface were approximately 12,0 units 4. For this test program, approximately 180 mgA ofsulfates were added to the sedimentation basin as a result of pH adjustment with 25% sulfuric acid. 5. 'rho 5000-S pH Monitor and Control System is fully automated and provides a pH adjusted waste water which could effectively he reused within the Redi-mix concrete industry. FORTRANS pH CONTROL SYSTEMS FORTRANS pH CONTROL SYSTEMS are completely automatic. They continually monitor/test the pH of the influent water and compares • it to the PH setting of the control unit. If a change In pH is detected, the controller activates the solenoid valve for the CO2. The pH adjustment chemical is then fed to the return side of the circulation pump until the pH is again at the proper level set at the controller. The unit will continuously circulate the water until a change in pH is detected and the treatment cycle begins once again. The unit also features a digital pH meter connected to a probe In the sample cell to ensure unit Is functioning properly and that the correct pH level Is maintained. The pH CONTROL SYSTEMS are designed to treat and maintain a specked pH level in a body of water usually 100.000 gallons or less to allow the permitted discharge of treated water to the environment. Permits must be obtained from the local governing agency to allow any discharge to the environment. Treated water may be used for wetting of rock and/or dust control to aid compliance with stormwater run off regulations. Treated water may also be used in water recycling systems. These systems offers precise monitoring and control of the pH In settling basins, lagoons and other outfall containment devices. -The pH CONTROL SYSTEMS will treat up to 57 gallons per minute - Max 20' head pressure. Unique water circulation design eliminates the need for separate neutrallzatlon tank. •1.5" quick connect fittings on inlet and return for easy hook-up. The standard unit Is equipped with 2-30'sections of 1.5" flexible hose with quick connect 0ttings. Inlet and outlet (filings at the basin or lagoon are per our specifications- -Unit is shipped completely assembled. The chemical controller Is preprogrammed to maintain a pH of 7.5. Just attach hoses and PVC fillings. .1 year warranty on all component parts and housing. Fortrans.: FORTRANS. INC. • 7400 t..S'(ernen9 Rd, • Wendell N.C. 27691 1.069.365.0760 - 1,919,624.0032 Irdo®fortrans.blz - www.fortrunx.blz The Model 5000-S pH Control System is a self- contained pH monitor and control system housed in a weatherproof facility with lockable doors and adequate space to house the instrumentation and circulation pump.The system Is configured for carbon dioxide gas operation - The Model 5000-SK Skid Mounted pH Control System contains all of the instrumentation and components of the regular Model 5000-S System and Is shipped on a 44707" plastic skid with a durable solid plastic surface. The Control Panel is provided loose with all components Installed and Is designed to be attached to an interior wall of the control building. The tubing to the sample cell and from the CO2 solenoid valve to the Sparger stone feed assembly must be inserted after receipt of the unit. The system features a 115V-30Amp Breaker Box and two GFCI receptacles, The system is shipped with a CO2 feed system. =ORTRANS pll CONTROL SYSTEMS - MODEL 5000-S & 5000-SK intake line detail Ovahmd vices staring hoein� Relum Ilue nriw ow waft OeN I Jr.' c•n, lock quick coma 1C I lr" ahedule CU U�drh a ld be 1 ocalceaUtaed uhmr �nler Imt dtcck nlv ve rnn hecftanal j�J/ 5orn.dwlKrw n�rcmt'n pike r � lac<mmtinlrasin.Tda ryryMM of �Pkortlum lira lr mWled'1Povcr � Ilmhi6're wall, _ Return line detail Option Y ' N qulcckm loam Iwft Reium Une "Uticl epp lava y Ilc hatom at n¢ Iraalo Rdum Ilne Outlet ix cams qcd qth 1 Ir"bthrdule AU INC Fortrans.. .9000 Origlnnl Henry RV.. P.O. BOX 769 • Henry. Vs, 2002 • 077.307.0S09 - www.fortrans.bIr Model 5000 S & SK pH Control Systems INSTALLATION NOTES 1. Connect'YV hose to hose Clung on the white CO2 injector and the other end of the hose to the hose fitting on the check valve at the solenoid valve. Push hose ends all the way into the W hose fittings. (SK Model only) Note: The CO2 injector is shipped in an upside down position on skid mounted systems. Turn it to an upright position and lighten union connection. (SK Model) 3. Connect hose fitting on return fine to the Hose Fitting marked "inlet" on the sample cell with the M." hose. (SK Model) 4. Connect hose fitting on the intake or suction line to the hose fitting marked "outlet" on sample cell. (SK Model) S. Insert pH probe Into probe fitting and lighten. Do not let probe dry. If necessary add water to sample cell through the probe holder and reinsert pH probe. 6. pH probe has been calibrated at the factory. It should be re -calibrated every week. See operations manuaf for calibration instructions. 7. Catalog # 2886-L ph 4.01 buffer and catalog # 2681-L ph 7 buffer agent are included. These materials may be re -ordered from Fortrans Inc. 8. It may be necessary to Install a V9 PVC ball valve on Intake line In order to fill Fine with water to help prime the pump. See drawing in operation manual for placement of the ball valve. 9• Use PVC Cleaner and PVC Cement to install Intake and outlet fitting through the back of the housing. 10. Plug the pH Controller into the 1000 joule surge suppressor_ 11. Ground pump to copper grounding rod. 12 Position outlet in basin se that the waterflows parallel to surface of water. This will create a circular flow In the basin. See drawing for more detail. 13. Install warning light and plug into outlet on right side of controller. 14. Tighten all union connections before operating. nkttoollhMohn&Prooucls... Sbn03 PH Cnulnd iY.Anm • Wilmm"n' •f:rmcrnln Wuunvnr •;ah•3oaP lr •Stdn �;n�c+ • Carrinby-Churly Crv$UGP- ; e Olralo/• Truck Wnah •rUllnlr 1 One" ;uc huk' ::"pnrShc" • Wund 141WTWI� • Molorryrin Clmmir, .H;w1n W-'CW-no.kol Wm:h— SpnY Or19hr' Map of Location of Proposed Temporary Concrete Plant 1-40 Widening From 1-85 IN Orange County to The Durham County Line with Interchange Modifications TIP PROJECT: 1-3306A / W-5707C Date Drawn By Revision No 10/21 /2022 Rob Morales 01 lane P,.O* 40 . 130 . 7 .tth Z 0 k CF �J _ • '� \\ \ cui rr 20 �� .•ob =�.i ciornrr �\ P 4� i K1V112 it le Silt fence M, 1 516 `__f,tl. E iS i 1CN JTE- 520 W \ \ �\ Drainage , \ Area 3.2 AC Drainage Area 2.2 AC y '� 4iS0•rOr • 4S Pi i 4+' _ . K.'ir.•�SA•.��5 �Se:.�=�r�.i0 sot - W y Table Legend \ — Grading Contou Drainage Area Slope Drain Temporary Silt r " Silt Fence alp GRAPHIC SCAT Grading and Erosion Control Plan of Proposed Temporary Concrete Plant Date: 12/12/2022 1-40 Widening From 1-85 IN Orange County to The Durham County Line with Interchange Modifications Drawn By: Rob Morales TIP PROJECT: 1-3306A / W-5707C Revision No. 01 1 Lane r� I 4A k WASHOUT PIT Section C-C 12"( I Pipe 1.5' (Min.) SETTLING BASIN Coir Fiber Mat Soil Stabilization Geotextile Unclassified Earth Material 18in. Overlap Natural Ground REMEE =—► A Waste Water Treatment System Washout Pit Info: 20 FT x 20 FT Top Dimensions Side Slopes: 2:1 (H:V) Settling Basin Info: 160 FT x 40 FT Top Dimensions (at weir) 140 FT x 20 FT Bottom Dimensions Side Slopes: 2:1 (H:V) Depth at Spillway: 3.5 FT If site conditions permit, could be converted to "tiered" basin PH Reduction Basin Info: 50 FT x 30 FT Top Dimensions (at weir) 30 FT x 10 FT Bottom Dimensions Side Slopes: 2:1 (H:V) Depth at Spillway: 3.5 FT PH REDUCTION BASIN =iB C11 1C Outfall No. 1 Fortrans PH Control System Model 5000-S Section A -A 5 FT ---------------- 3.5 Fr Fortrans PH Control System: Refer to Manufacturer's Catalog and Operation Instructions Date: 12/13/2022 Concrete Washout Pit and Wastewater Treatment System Drawn By: RM Revision No: 00 Proposed Temporary Concrete Plant Site For the 1-40 Widening From 1-85 IN Orange County to The Durham County Line with Interchange Modifications TIP PROJECT: 1-3306A / W-5707C 10 FT 20 FT 10 FT 01 Section B-B �5Fi 3.5 FT 10 FTt 10 FT 10 FT i l lane