Loading...
HomeMy WebLinkAboutWQ0019755_NOV-2021-PC-0324 Response #2_20211007DIEHL & PHILLIPS, P.A. CONSULTING ENGINEERS 1500 Piney Plains Rd., Suite 200 Cary, North Carolina 27518 Telephone (919) 467-9972 — Fax (919) 467-5327 October 7, 2021 Mr. Lon T. Snider, Regional Supervisor Water Quality Regional Operations Section Division of Water Resources, NCDEQ-WSRO 450 West Hanes Mill Road, Suite 300 Winston-Salem, NC 27105 Re: Notice of Violation (NOV-2021-PC-0324) Oak Ridge Commons Permit No. WQ0019755 Dear Mr. Snider: WILLIAM C. DIEHL, P.E. JOHN F. PHILLIPS, P.E. ALAN R. KEITH, P.E. As a follow-up to our previous correspondence regarding the subject Notice of Violation, we offer the following information regarding the violations cited in the NOV letter dated June 22, 2021. Tertiary Filters: The tertiary filter tank for this treatment plant was furnished with an inlet trough to distribute the influent flow to the two filters. In addition to the outlet pipes to the two filters, the trough had a third outlet pipe, located at a higher elevation. The third pipe was designed by the manufacturer to only receive flow if the water level in the trough became abnormally high due to an excessive headloss through one or both filter cells. As originally furnished, any flow into the third pipe would be released into the clearwell. After being in operation for a number of years, there were several instances of the filters becoming partially blinded, causing some unfiltered water to be diverted to the clearwell (it was subsequently discovered that one of the return sludge airlift pumps had been improperly constructed, causing periodic clarifier upsets which would sometimes lead to the filters receiving excessive solids; the airlift pump has since been repaired). The occasional discharge of solids into the clearwell caused the backwash pumps to pump solids into the filter nozzles in the filter floor, which reduced the hydraulic capacity of the filters and led to additional solids being discharged into the clearwell. Mr. Lon T. Snider October 7, 2021 Page 2of3 These problems were addressed in 2017 by the following actions: 1. A pipe was installed over the clearwell, to convey any overflow from the influent trough to the inlet trough for the tablet chlorinators, keeping solids from being deposited in the clearwell. 2. The filter media was removed, and filter nozzles were replaced or cleaned as required. 3. The original filter media consisted of 12 inches of sand under 12 inches of anthracite. The sand had an effective size in the range of 0.80 to 1.20 mm and a uniformity coefficient of 1.4 to 1.7. The anthracite had an effective size of 1.08 mm and a uniformity coefficient of 1.42. It was observed that the original anthracite layer had been washed into the mudwell over time, most likely due to backwashing with an excessive flowrate in an attempt to clean the filters. The original media (total depth of 24 inches) was replaced with 36 inches of a coarser sand media. The replacement media was gravel pack no. 3 from Southern Products & Silica Company, Inc. of Hoffman, NC. The replacement sand had an effective size of 1.91 mm and a uniformity coefficient of 1.39. It was my belief that a monomedia filter would allow vigorous air scouring and backwashing of the media while eliminating the concerns of anthracite washout or poor re -stratification of the sand and anthracite after backwashing. The resulting filter effluent quality was consistently improved with the replacement media. Mudwell Pump Discharge Piping: The original plant construction included a 2-inch force main for the mudwell pumps to return the backwash wastewater to the flow equalization basin. The operators noted that during peak wastewater flow periods the flow equalization basin would be at a relatively high level, and a filter backwash would have to be delayed until the FE basin level declined. To provide more operational flexibility, the operators added a 2-inch PVC connection from the force main to one of the sludge holding tanks so that the mudwell pumped flow could be discharged there, if the level in the sludge holding tank would permit the additional flow. The clearer liquid would subsequently be decanted into the aeration basin. In addition to the pipe connection described above, a second 2-inch PVC pipe (and valving) was added to allow the mudwell pumps to discharge into the 6,000 gallon non - reclaimed quality wastewater treatment system included under WQ0019755. This allowed the backwash volume to be removed from the 30,000-gallon reclaim wastewater treatment system, but still be disposed of properly in the 6,000 gallon treatment system. I have enclosed two plans sheets that show the pipe and valve additions, and the changed filter media. Mr. Lon T. Snider October 7, 2021 Page 3of3 Summary: The modifications detailed above were considered by JPC Utilities, LLC and me to be to be maintenance repairs/improvements. They did not change the permitted treatment process or expand the plant capacity, but they did improve the plant operations and performance. Your letter implies the Permittee diverted or bypassed "untreated or partially treated reclaimed water from the subject facilities". I would disagree with that characterization. If one or both filter cells experienced a high water level and caused some flow to bypass the filters and the clearwell, that flow was still disinfected and its turbidity was still measured. If the turbidity exceeded 10 NTU, the control system would automatically divert all of the plant effluent to the non -reclaim storage pond, and subsequently to the non -reclaim irrigation zones. Once the turbidity levels dropped below 10 NTU, the controls would then re -direct the flow to the reclaim storage pond and irrigation fields. It should also be noted that while any effluent diverted to the non -reclaim pond may have had a turbidity in excess of 10 NTU, that water had received secondary treatment and disinfection before being diverted. The diversion of effluent to the non -reclaim storage pond is not a bypass of any process; it is the disposal of non -reclaim quality effluent as allowed under the permit. We apologize if these maintenance modifications should have been preceded by an application for an Authorization to Construct. If the enclosed updated drawings and this letter are not sufficient to update your files, please advise how you wish for us to proceed. Yours very truly, Diehl & Phillips, P.A. � � -1 ? Djj4- $, 1'. John F. Phillips, P.E. Cc: Ms. Jennifer Graznak Ms. Caitlin Caudle Mr. Philip Cooke Mr. Doug Smith ° v v v vv v v v v_ 1 1 RE -USE EFFLUENT STORAGE LAGOON \\ 1 1 l ll I I \ __7 I I ° 970— \ •ft I _ ' \ ♦ a' ► \ I 1 DIESEL E GINE \ I ° /DRIVEN 0 kW \ I 1 / STANDS� POWER \ \ I°ice '�� ' B(OltiER ® _- GENERATOR \ 1 ` �� I ♦ 1 1/Rp�cAT/o & — / v ft. 40 Ll 'I / \ • . \ 1 40 EXIST. FES ( 904 INV. EL. 902.09 I 2" e Lc _ \ _ 2 I EX/ j ?'RCP _ I _ 1 EXIST. 8" D.I. GRAVITY SEWER / ♦ , 1 I I _ I ll 1 �� I ll y EXIST. 2" PVC FORCEMAIN 2" PIYC FORCE MAIN* 920 —\ / / ♦ I I I \ I I l 1/ � � III r r �� w I I I I I I �� — � / /�/ ♦ I II III \ I I: �� IIIIII Ud� II/1 jl IIIIII d d�d d IIIIII' I Uw IIII �III wQ IIIiI IIIII I� � � 0 I III II �� P 1 1 1:1 ur)� IIII I 1/�/ � l l l i i� I v v I i l i i � i I I I I� _� �_-�\��-- \--• I l i i I1 ° '� ,__ — I Ex. SAN.� TOP. 92. INV. IN: \ I I I I IIII 1 �� IIIII III ' 1 ° / INV. OUT: v �v � v �., 1 I I I I , I: 1 I I I� � III � I I I► I I EXIST. TAOOR LET 11 CHLORINA EFFLUENT STORAGE I I I � \ \ _ _ \��— — — — �\ j /� I ° \\ EXISTING LAGOON \ I I . I I / `\ — _ _ _ _ _ _ _ _ MM EXIST. RESEDG I cnrEUAL Fu \ 4 1 I I I I OW METER OX / I ��; /. ° 14 \ \ ) I l 11 I 1 I I I 1 1 1 EXIST. RECIRC. / / \ 55 SPOTTER BOX / / I 1 I� I /• EXIST. \ I 8» WYE­\--_\----------------- \� I 1 / I / -- °_915IRRIGATION PUMP ° - o __ OPEXIST. SPRAY --�-\ / �HOUS 921.5 MANHOLE 1ISTATION w/ INV. 915.36 4 VALVE VAULT _\l • . - EXIST. 14,000 GAL. EXIST� GRAVEL ACCESS DRIVE / SEPTIC TANK EXIST. WATER 1 _ \TANK �. / II / j \\ I I I I I I / _ _ _ _ _ _ _ _ \- ♦ ` EXIST. 12,000 GAL. RECIRC. P.S. \ \ \ \ III ♦ \ 1. \ \ �\ \___--- — ��, r— IIII 1 �� \\�� �--- \..—,•;' � I \� \1 �� \�,�, j II I I \ \ 44* RAF 40 ,, ss / DESIGN JFP DRAWN JLB CHECKED JFP � scALE - FILE ORC-WWTF z 0 w • n • �\0 U CD °� N zW� aud+ 1 \5, Q � H W Z � z�� Lr) W }a U W H G O �zU O W nH a Ea U�� a r H U - O - -_— U) w [� — UQ � W II * FOR ADDED PIPING II AND VALVES ONLY a w GROCER Y �yCARQ/ O 2 2 0 5 B ,..-o .KIL�o••.���--.. AL I - �0 3 - SHEET 1 Px� OF 2 FT 6" D.I.P. TO RE -USE STORAGE LAGOON 4" THK. CONC. COLLAR 6" MJ MOTORIZED PLUG VALVE WITH MANUAL HANDWHEEL OPERATOR INV. EL. 913.50 o `r SAFETY CHAIN SEE DETAIL SHT. 11 w w L- 4'-0" UNIOI\ (TYP.) C(D 2" 90° BEND BAFFLE WALL #1 2" GATE VALVE CHECK VALVE IN RISER (TYP.) OUT 906.90 6" TIDEFLEX SERIES 35-1 FLANGED CHECK VALVE OR APPROVED EQUAL 4'-6" C.C.C. 6 "0 P. E. CONN - ULTRASONIC FLO BAFFLE WALL # (JL 1-CHLUR MUULL 7 7 U OR APPROVED EQUAL) CGS SRO NCR TN l v/1O 8 3� TURBIDIMETER WITH INTERFACE MODULE, SUBMERSIBLE PROBE AND CABLE, WEATHER HOOD/SUNSHIELD, PIPE STAND, ADJUSTABLE MOUNTING BRACKET, AND PROBE ADAPTER (ALL PROVIDED BY TURBIDIMETER SUPPLIER) 23'-2" 6'- 6 2,-8" 5'-6' CLEARWELL FILTER CELL MUDWELL (2,625 GALLONS) (TWO @ 10.68 (3,127 GALLONS) SF/CELL) WELDED STEEL HANDRAIL (TYP.) FILTER CELL FLOW CONTROL INLET- GATE VALVE 12" THROTTLE VALVE 4" BACKWASH PUMP PIPING 4" SCH. 80 PVC FILTER ii-r2 x 2 x 4 SUPPORT ANGLE (TYP.) B.W. TROUGH EDGE OF CONCRETE SLAB (TYP.) 1 "' AIR LINE FROM BLOWER & IRRIGATION PUMP BUILDING- 4" STEEL FILTER FILTER #1 OVERFLOW LINE LEVEL SENSOR BRACKET 0 cl- 4CHECK 2 J UNION VALVE z GATE VALVE TYP. CPI ACI--I P1 ATl- PT. A N VTFW 2" BALL VALVE SCALE: 3/8"= 1 '-0" ALUMINUM ACCESS LADDER cr U I (j cj_ z w cQ� o�owo ::7)ow� zio�^ IN z �,oQcZn WELDED STEEL HANDRAIL 12" AIR SUPPLY HEADER 4" G.V. WITH EXTENDED HANDLE FOR FLOW 4" STEEL FILTER INLET TROUGH ADJUSTMENTS OVERFLOW LINE TOP EL. 914.79 6" STEEL INLET PIPE TABLET CHLORINATORS �Y9 (JET-CHLOR MODEL - � tLEVE 110 OR APPROVED 4" SCH. 80 PVCEQUAL) FILTER OVERFLOWL SENSORS EXTENSION ADDED W.L. 2 " G. V. BACKWASH TROUGH TOP/GRATING 2" UNION EL. 910.79 W L. - N.W.L. i f d / - 12" H TYP. 6" MJ DIP SAFETY CHAIN �q 2" MUD_WELL DISCHARGE TO F.E. BASIN (SEE SITE PLAN - SHT. 1 FOR CONTINUATION) � 12" AIR LINE FROM BLOWER & IRRIG. PUMP BLDG. 4" CABC OVER GEOTEXTILE WEED BARRIER -PLACE BETWEEN PLANT AND FILTER, AND AROUND PLANT & FILTER FOR A 6 FOOT WIDTH I ALARM & BACKWASH INTERRUPT EL. 912.00 LAG PUMP ON EL. 911.00 2 CHECK I .. 4 VENT VALVE -------- PIPING NORMAL HIGH WATER ALARM EL. 909.00 W. L. i BACKWASH - OUTLET BOX LAG PUMP UN EL. 908.50 z z BON. OF 2 C C PUMP ON EL. 908.00 V-NOTCH WEIWEIR i J J EL. 908.79 � C C 6" EFFLUENT FILTER MEDIA* � Zi � z- INV. EL. 907.20 �W WAT w m PUMP ON T OFFER SWITCH `r FILTER FLOOR EL. 906.00 d WITH NOZZLES PUMPS OFF PUMPS OFF EL. 905.00 - EL. 905.00 AIR SCOUR DIFFUSER GRID TOP/SLAB EL. 903.79 12 "x 12" OPENING IN BAFFLE WALL (TYP.) ELEVATION SCALE: 3/8"= 1 '-0" * FILTER MEDIA CONSISTS OF 36" OF SAND WITH EFFECTIVE SIZE OF 1.91 MM AND U.C. OF 1.39. (GRAVEL PACK No. 3 SOUTHERN PRODUCTS & SILICA CO.) DESIGN JFP DRAWN JLB CHECKED JFP SCALE FILE ORC-WWTF a Ea U Q O FOR PIPE ADDITIONS W AND MEDIA REPLACEMENT ONLY w �s�tiuuur 0 CAR&lle#, Q H =off;o��:ssi'N•.�ti°�;.� w SHEET ••• OF