Loading...
HomeMy WebLinkAboutNC0074268_Wasteload Allocation_19880729NPDES WASTE LOAD ALLOCATION PERMIT NO.: NCOO 7y 2-Lg FACILITY NAME: CR01/4.3cas k,JwTPcoly o� C. rvs o K Facility Status: EXISTING (circle one) Permit Status: RENEWAL 1100E1CATION UNPERMIT ED NEW (circle one) Major Minor.. PROPOf ) Pipe No: Design Capacity (MGD): Domestic (% of Flow): Industrial (% of Flow): Comments: PersiD c-g % (3,5 M�n� RECEIVING STREAM: Ca, cakeY. Class- C_ Sub -Basin: 03-0i6.-37 Reference USGS Quad: County- l\1vJ (please attach) Regional Office: As Fa Mo Ra Wa Wi WS (circle •ws) Requested By.,j Prepared By• 4�I Date: 7/z10? Reviewed Bv• Date: Date: 7(717gg Drainage Area (mi2 ) Modeler Date Rec. G03/8P `9' Avg. Streamflow (cfs)• 7Q10 (cfs) Winter 7Q10 (cfs) 30Q2 (cfs) Toxicity Limits: IWC % (circle one) Acute / Chronic Instream Monitoring: )o � d Parameters L-< Upstream Location @, Se z 54Z- Downstream Location / 7 ^1-.4.- '.s Effluent Characteristics _'uAnt/- W/411w WA) I / �MII,. BOD5 (mg/I) 13 13 d l,,s5l.t) 14-c NI13- N (mg/1) 02 10 MiCt.% ,r t 90 D.O. (mg/I) ‘ 6 !,7Amdt, (J5/9 I �j TSS (mg/l) 30 30 % F. Col. (/ 100m1) 16 o c> l o n e) p Hyy,�(S U) l. - y (. - R �A / ,,us. c . (01,�/ Uta.A%/G. DAY MA.‘• 11 • 3Z,7 :; 4,,i,.,_ (v'/,e) 3.5 Comments- > � ade''""`"- t Request No. :4687 �. Permit Number ^° Facility Name Type of Waste Status Receiving Stream Stream Class Subbasin County Regional Office Requestor Date of Request Quad WASTELOAD ALLOCATION APPROVAL FORM : NC0074268 : CROWDERS CREEK WWTP-CITY OF GASTONIA : 42% DOMESTIC wI/�L : PROPOSED =�~�~---' �o�����m��� ; CROWDERS CF��� : : C 030837 GASTON MRO FOSTER 6/13/88 G14NW JUL 25 988 nage Area MOOR , age Flow Summer 7010 Winter 7010 3002 '---- RECOMMENDED EFFLUENT LIMITS : Wasteflow (mgd): 5-Day BOD (mg/1): Ammonia Nitrogen (mg/1): Dissolved Oxygen (mg/l): TSS (mg/1): Fecal Coliform (#/100ml): pH (SU): Total phosphorus (mg/1): Tot'res. chlorine (ug/l): Chromium (ug/l): MO. AVG DLY 6.0 13 6 30 1000 6-9 2 19 32.7 MAX Cadmium Lead Nickel Cyanide MONITORING (sq mi) (cfs) (cfs) (cfs) (cfs) (ug/I) (ug/l) (ug/l) (ug/l) 3'5 40 79.4 91 6.7 18 26 Upstream (Y/N): Y Location: SR2424 Downstream (Y/N): Y Location: 1.7 MILES DOWNSTREAM OF DISCHARGE ---------------------------------- COMMENTS ---------------------------------- RECOMMEND EFFLUENT MONITORING FOR SELENIUM, OIL & GREASE, COPPER, SILVER, AND ZINC.RECOMMEND INSTREAM MONITORING FOR TEMPERATURE,DO,FECAL COLIFORM, AND CON- DUCTIVITY. MONITORING SHOULD BE WEEKLY IN THE SUMMER AND MONTHLY IN THE WIN- TER. **TOXICITY LIMITS ATTACHED** **LIMITS DEVELOPED FROM QUAL2W MODEL RUN BY SOUTH CAROLINA'S DEPT. OF HEALTH AND ENVIRONMENTAL CONTROL. SEE ATTACHED MEMO. tjt- . � I)ya j~h s"k— ^ -~I Recommended by Reviewed by: Tech. Support Supervisor Regional Supervisor Permits & Engineering RETURN TO TECHNICAL Date Date - Date/7� ��� ------ �--�_ _ _ _ SERVICES BY Date AUG�0 1�0O ^`�u�� /��w 1,4 Facility Name CW/11:5 6-id 7-"' 6./ •i lit' Permit #t NG Oo 71Z(y p CHRONIC TOXICITY TESTING REQUIREMENT (QRTRLY) 'Ilse effluent discharge shall at no time exhibit chronic toxicity using test procedures outlined in: 1.) The North Carolina Ceriodaphnia chronic effluent bioassay procedure (North Carolina Chronic Bioassay Procedure - Revised *February 1987) or subsequent versions. The effluent concentration at which there may be no observable inhibition of reproduction or significant mortality is 58 % (defined -as treatment two'in the North Carolina procedure document). The permit holder shall perform Quarterly monitoring using this procedure to establish compliance with the permit condition. The first test will �' perf rmed after thirty days from issuance of this permit during the month of tip r Qc . Effluent sampling for this testing shall be performed at the NPDES permitted final effluent discharge below all treatment processes. All toxicity testing results required as part of this permit condition will be entered on the Effluent Discharge Monitoring Form (MR-1) for the month in which it was performed, using the parameter code TGP3B. Additionally, DEM Form AT-1 (original) is to be sent to the following address: Attention: Technical Services Branch North Carolina Division of Environmental Management P.O. Box 27687 Raleigh, N.C. 27611 Test data shall be complete and accurate and include all supporting chemicallphysical measurements performed in association with the toxicity tests, as well as all dose/response data. Total residual chlorine of the effluent toxicity sample must be measured and reported if chlorine is employed for disinfection of the waste stream. Should any test data from this monitoring requirement or tests performed by the North Carolina Division of Environmental Management indicate potential impacts to the receiving stream, this permit may be re -opened and modified to include alternate monitoring requirements or limits. NOTE: Failure to achieve test conditions as specified in the cited document, such as minimum control organism survival and appropriate environmental controls, shall constitute an invalid test and will require immediate retesting(within 30 days of initial monitoring event). Failure to submit suitable test results will constitute a failure of permit condition. 7Q10 . 7 cfs Permited Flow 6.0 MGD Recommended by: IWC% 58 Basin & Sub -basin ca. 3 Receiving Seam Ceat w(. County G'�{4,/ ate �' /r h( **Chronic Toxicity (Ceriodaphnia) P/F a Sd %, 19IX 14L "Cr , See Part 3 , Condition X. DIVISION OF ENVIRONMENTAL MANAGEMENT July 15, 1988 MEMORANDUM TO: Allen Wahab THRU: Steve Tedder Trevor Cleme David Vogt FROM: Jackie Nowelli SUBJECT: Proposed Crowders Creek WWTP - City of Gastonia NPDES No. NC0074268, Gaston County Wasteload Allocation / AT Justification The Technical Support Unit of the Division of Environmental Management has completed the Wasteload Allocation for the subject facility. During our review of the Crowders Creek WLA, it became apparent that because of the proximity of the discharge point to the N.C./S.C. state line and the large wasteflow (6.0 MGD), the discharge from the Crowders Creek facility would significantly impact the waters in the South Carolina portion of Crowders Creek. For this reason, this project was done in conjunction with the South Carolina Department of Health and Environmental Control (SCDHEC). As a result, the recommended limits for the oxygen consuming parameters were based on the QUAL2E Model run by Mr. Terry Borders, Manager of the Wasteload Allocation and Certification Section of SCDHEC (see attached letter from T. Borders). The methods used to determine model input have been reviewed and approved as part of the 1983 South Carolina / EPA Region IV agreement. Technical. Support provided the headwater inputs for the S.C. QUAL2E Model by performing a Level B analysis from the headwaters of Crowders Creek to the proposed discharge point (just below N.C. State Road 2424). This was done by using the amount of dissolved oxygen, carbonaceous BOD, and nitrogenous BOD at the end of the model as background levels for the N.C. portion of Crowders Creek. The aforementioned letter from SCDHEC provides an explanation for the recommended limits to protect water quality in South Carolina. However, there has been a change in the BOD, limit from 18 mg/1 to 13 mg/1. South Carolina used a CBOD/BOD, ratio of 1.5 to convert 27 mg/1 of CBOD, while Technical Support uses a CBOD/BOD, ratio of 2 when a municipal discharger has more than 10% industrial waste present in their wasteflow. SCDHEC is in agreement with our recommendation to reduce the BOD, limit to 13 mg/1 and concurs that a more stringent limit gives greater protection to the eutrophic waters at the mouth of Crowders Creek. The recommended metals limits are based on estimated concentrations for the proposed facility utilizing the loads from all currently permitted industrial dischargers that will be incorporated with the new Gastonia plant. In the absence of pretreatment headworks analysis, this was consid- ered to be the best method of determining limits for metals. Where esti- mated concentrations were within 1/l0th of the allowable concentrations (determined by using mass balance equations), limits were established for that parameter. Otherwise, only monitoring was required for probable con- stituents (see Appendix D). Finally, Technical Support recommends that a reopener clause be placed in the Gastonia permit to add, delete, or modify limits if monitoring data provide sufficient reason to do so. If there are any additional questions or comments on the recommended limits for the subject facility, please feel free to contact me. JN/gh Attachments cc: Rex Gleason Terry Borders Don Garbrick Samuel L. Wilkins Jim Greenfield • GIB C,-t/ JOE�.f pr.,1 d4j,•y_ 9, 3 Ga%d' n / = Co.8Z /5.3 CV, 474, Out 1/�.�6/ CAA CAS, u� (>�.)(/- c 0/3 9,3 , 765 ._ ,071 _ _Mt? _ , a737 n-54 L. 7z 4, I "Tv.f G.o4,4 9, 3 s . /s.3 = 79/0: c76. 73, 8 (,c5//e At71Lisa e (/ S. 3 c {s>( 00 z //Q> 9,3 07 M 0306 ,0 72l /Q= 3,zscj/e,t33 J/e 9,3 3,3 uo�i( Ltid /r.3c7)(;OZS.,.3//e)— 6 (oos.y,e) 9.3 c.' , 3;Lr-- of _ ,7sz r _ , 9,3 L ,;L 037, mj/,e 3Z ? 1, 3 /4 31 uty/,Q 44;3 c {T (, 0 5 4)_ �6 � , Og y-3- 4;3 9.3 �Z, (5/,e 7,3 c7 9.3 C9 �r c/v = e. 2 v /� al-) E/ �411-f_ cr �► ;,4 Dla837 ( e 7d2L- ,,6 ---7---,.-,) ,,_,„' ,. re,,..,-- ,, 0_ /or,. ), c, zi. ,:c. , ...,„ 4„,-,- ,,,,,,,i_ „ .i.J., ,,,, ,.„. ci.,,,,,, c,J,. ,J7---, ,„2- 4,,,i a ..7-- .7),„,- --,4.,:. ,v.,--_, ec.„2._, c,._<_/_ ,:_,- ,, ...,,1 /,,,, ii,,A;_ z„, ,f-,,,,,,_,-,„. 0,7,/ 6. ieoo 70.4..+, ff1 94 r /O.7cj r51. 577/0x S. 9 c s/. w79/,) _ /6 ciS /. 512.= 23c.6 F A/i7 H c FhL61, IN/} You H Gfi$- L /N A- <G , J M (ram X /, S5 c70 a 6, 7 ei 02,/4'56,JfoL 41 9�,�s,, f — L✓u ,ears Cec (1C 4)&77 �w r 6, 0 41CIO D/f=79, Y,1/z pi= 9/e{s .57 6=a,7c6 ✓/ o = /705 9z=4,6 -$ ,7,1/I. aaJ'pc 7f4.. '•79' j�1/d =OLJ c-i/u 7°9j),c/dv.o.Jz7 c{s/••,/L gj, 3 c6 7,7 ens _ ,Six /00 = Se% �\ 9.3t-.7� /c c c41$1,/,„,4 Tyr A6. C. 3 96 �J p.16o/1/c4 Q69 z jVhJ,4 ✓ e 2S7MGD 9R 72 7444s4,./ X /; ciron! �ido/S 342,5 (-#/19 (.11-# 65/P (Av/9 4 L�wJ., d1/74" 61)/A), ) 4/"Ied (ihyp ( 1;621) 16�0L.)7 ' D, /ft, 4‘9 $a % / Go % D.h y ?“ 37 /7,3 3/ .2.0 % ss:s sz O, 0247 6, /S' 3, 38 6. /' 6.70 o.y3 26/ Q. 67 2./3 Lod ( 5 oo . oz/ /o, , 3/5 O 2,441 /04,)„ e-4,s.446:„,4 7315 (4/6:/,9 -1)//yots./;7(_ -7:•A4-01 ids /2 (1,3V PO ()3G1 (,v9 r“--e V://4.,(1$54,9 4 (/ ',) 'A)(-?/) ()� , ( 21174 0 N.e C/ OCth^ (# Z (9 WC/ az44.45 ala±L. 9w 00/ c DOZ 0 .6/5. ( lr.vto% At,i /*..100,04., 26C. 3 o,z 0}067 0./7 e. 95//. G (At.,) .a, 0.013 .OL O. /0, Z (0,..,14142) O.bI/is2-v...Ay O.Q/7 ,r% 7-7-6 ipe9 £/ L 4LA•nx 6.4 o I . aO7 rieJ/K pgPPrft, d l,Jvcoc c y6 tiga4i Ac C4b+,M Cam(/� e. 67 ik (2td.w JJ / �f;; 6, /7 67/f,_ � ./A 2.67 .Z if -Yc LL �'� wp a;o9 `-)e Necit.e (t * 6 Q Y e. /7' icAe, (V5" 4, Zy o, y3 Cxj// /, Y8 Z.6/ - -To Aj/02./3 04) -? )/t4A-4-(Ay/ .2c, rz- / ,.6 61.7ey 3/ 40 %# sv.) 6-' i..�l, -.. ()¢./h574L.3 tgGrwd-s40.5 6140 (#-Artqs) f# (S.d) FitieYdL hs/t) O. ofz A!& z/7- 1v' 'i 0/ 30 .36 ,/32 ooy (C.c. 0, 02� v ,vow 0 0 0 14' c-(1c( ii,b-f6 CL) u-ca9 X o 0.,2 cL C ss= (Qv,4-04\i QL4c't ()„ xo A b 1 , Q c L) pLc4e› Mowet_kke Cw -� �C3tJ}%YI A I A S c o £vS C-n--+d 4-s l_.s'LeL SJZK. 0412.04Aie t ,/rdma ThLAn/ Pi'sccsJIM �+ ) // - (. iy--"4-,t_v /L4 �i�Gr,/Sr�3 X GI,2 o, 257 6. / Sid 6, 6 /s_ o,9aa d,o2Z 6, O/2 /, 1st tfimd,i54747 2 1 977 7c 44 -.� n.7 doso9r iy- 2,3 Lo /oo ".,,� (.i 770 7y 3 Cl/611,J„,,. t596 X-.05 , zz7 ,.273, /14 = 016 J1-5/k_ a,.(2f mow. P�yJT Atsi,A c,) _ [Co( = .eso .0s s //)_ ��,7)(,013/4;/,e) 9,3 . e°°/P — , .44 9, 3 05 7/3c . 077 vo77, /Q� ,Q0g p)1 AI • Le 0 6 9 , 000$ o ant-/ 0 oo72/ _ /,451 = f,5516- .003 0/34, A ,t/ A o 208 'I M D , G 035 OW II ,0031 f a-Q po..fi'm-= 3 4 ,-S (4 Adkj Cw ^. 0035 0 0 o 3� 6.7,6 -- 9,3 e / 1 C.4S Ms-ax0 a Idefie _ . /7/ le6-o ./V = , o e / ALP-4/4-_.,tif = •0l D/Z mere / D = 0 Q %sp M6v2 ,033 f'v�( /./ ofJelk ,06.2 _,r-- .Z f to y,..s /,Q G Ara-o = /, 613 g l6 c (0 Z 5 wr-Y Q) — 4.7 c (0 os /X D. �%r • n ��( — . 03/ c 15 /Q 9,3.4 36 6 cfs • +W(/� 9. 3 c_{'s CJ � o a,Zwz.--tar t , 0 0 3 9 • °" J 517i4 ,og /J.� Cif , 25-7 �� 6 0 2 / J - -,SsiC y .OZ/025 .// 4 4( _ . d 23 _ AL c4(a s)0 9, 33 93 0 -01-44-r7-44 - . 0 0" / C -4/ �/ cid ask sfri x , 094„,/,=) 90 f/1 3af 6 */ —� 03—/ 9,3 , /4 kk,c_ig._ 4d-L._ve = , 5-/ „.> . 660i //e a a 9 / .Q 9 (/ 7C .0086 ;„,54 , 009)' . (/S. 0/Z t7e _ , 007 7f(z,t hya-fr i/7,,zw /‘,6 (1, /,e) 9,3 c, ?3 vt. . C / 7 k / ' = 00o/7 > , 0O/7 > . oo/Z , 80 /7 J AV toc.�i✓ ��� N� J"1 �'Vavrdt v/Z x lo� _ /, 4Sg ;u 41!6x /4 /6„.6 0, j 41,„.„A ./3z /3c,_/,dzz 49 -/Ad cW 9,3G� 4,30a Jf• er0 1c/1,4.1e= o3oz igloo / a 022hesic G ,036Z /V k ,4/' %3� 17-6 M69 C4S-,2S7x� Pft,ei= , 7V Adfri'x , ,3/5 = , A c-0/Y 0 Ar6,o Cf4f = . D zZ X .Z/3 = •01/7 M ` ., QIZ �� b ai/ = MEMORANDUM TO: FROM: DIVISION OF ENVIRONMENTAL MANAGEMENT June 21, 1988 Trevor Clements, Supervisor Technical Support Unit Water Quality Section Rob Brown Local Planning Management Unit Construction Grants Section SUBJECT: Gastonia and Tarboro Discharge Points The Tarboro WWTP will continue to discharge at the current location and expanded design size will be 5.0 mgd. The proposed Gastonia WWTP will discharge at the Crowder Creek site as noted on the enclosed map. Design flow is 6.0 mgd. RB/jh cc: LPMU GPF ulti; h`;• :: fr• • OR x. • T GAVOlika C11110WOCRS T AS TQ ,-.11ACICX104 soirm 00IA • / ropc?ed Crow _c o u N COUNT C A R 0 L M A 0.7r 'r:•Existing Pump Station ir",4473-; Proposed Pump Stati - .z,Proposed G ravity Outf Proposed Force Main ••• - - . Proposed Trunk InterCep co -t . • ' APPENDIX B South Carolina Department of Health and Environmental Control 2600 Bull Street Columbia, S.C. 29201 Commissioner Michael D. Jarrett March 15, 1988 Ms. Jackie Nowell State of North Carolina Department of Natural Resources and Community Development Division of Environmental Management 512 North Salisbury Street Raleigh, N. C. 27611 Re: Proposed 6MGD WWTP Crowders Creek to Lake Wylie Dear Ms. Nowell: Board Moses H. Clarkson, Jr.. Chairman Oren L. Brady, Jr., Vice -Chairman Euta M. Colvin, M.D., Secretary Harry M. Hallman, Jr. Henry S. Jordan, M.D. Toney Graham, Jr. M.D. As you informed me over the telephone, this proposed facility will discharge into Crowders Creek just above the NC/SC border. This Section has completed a QUAL2E microcomputer model on Crowders Creek beginning at the 605 feet elevation down to Hwy. 49 at elevation 550 feet. South Carolina Catawba District personnel made a visual inspection of the creek and a water quality assessment was conducted June 7 and 8, 1982. The 1982 study plan and data results are attached for your information. The dissolved oxygen analysis using the QUAL2E shows that Crowders Creek is water quality limited. The bottom of the D.O. sag (5.00 mg/1 minimum) caused by this discharger is predicted to occur in South Carolina 1.7 miles downstream from the facility at the 600 feet elevation. Recovery of the dissolved oxygen occurs before the lake cove. Background data used in this model were furnished by you. A copy of the QUAL2E model is attached for your information. The following limits are needed to assure protection of applicable Class B South Carolina dissolved oxygen water quality standards. Q 6.0 MGD BOD5 18.0 mg/1 NH3-N 2.0 mg/1 (March - October) NH3-N 10.0 mg/1 (November - February) D.O. 6.0 mg/1 (minimum - all times) Ms. Jackie Nowell Page Two March 15, 1988 Of considerable concern to South Carolina is the eutrophic condition of the Crowders Creek cove. The "trophic ranking factor" was one of several methods used in determining an overall ranking of 40 publically owned lakes addressed by the South Carolina Clean Lakes Classification Survey. Trophic ranking of the lakes was accomplished by listing the lakes in descending order by "trophic ranking factor." I've enclosed Table 6.9 from this report. The number one ranked lake (Lake Greenwood, Reedy River) corresponds to the one with the poorest trophic condition. The Crowders Creek cove of Lake Wylie, which we are now concerned with, ranked fourth, while the other areas of Lake Wylie placed further down on the list. During the winter, phosphorus is the limiting nutrient in Lake Wylie, including the Crowders Creek cove. During spring, summer, and fall, nitrogen is the limiting nutrient in the Crowders Creek cove. As you are aware, nitrogen is most likely to become limiting in highly enriched systems such as the Crowders Creek cove. Therefore, the greatest control on productivity would result from control of phosphorus inputs with some added control from nitrogen restriction in systems already enriched. South Carolina has only two small sanitary dischargers (total of 0.029 MGD) to the Crowders Creek drainage area. At 8.0 mg/1 total phosphorus, contribution is less than 2.0 lb/day. The North Carolina proposed facility would contribute 99.99% of the loading of phosphorus to the cove. In order to evaluate the impact of the phosphorus contribution to Lake Wylie by South Carolina dischargers, the Vollenweider type analyses has been employed. The attached figure depicts the results of the Vollenweider model. The TP loading rate of 8.38 g/m /year is over five times that proposed by Vollenweider as an eutrophic loading. If all South Carolina dischargers provide TP removal, the expected loading rate to the lake would still be 7.99 g/m /year, an insignificant improvement. Our District personnel do not report documented algae -related problems in the Crowders Creek cove, but a recurrence of drought conditions such as in 1980, 1981, and 1986 may induce a large growth of algae if this loading of phosphorus from such a new facility is allowed. During periods of hot, humid weather, the combination of high light intensity, high temperature and elevated nutrient levels will provide ideal conditions for algal growth in this 2.8 mile long cove from Hwy. 49 to the main channel of Lake Wylie. Ms. Jackie Nowell Page Three March 15, 1988 EPA recommends that total phosphates as phosphorus not exceed 50 ug/1 in any stream at the point it enters any lake. This recommendation is to prevent the development of biological nuisances and to control cultural eutrophication. Modelling of organic phosphorus as P and dissolved phosphorus as P with the proposed discharge show levels of these parameters as 2.95 mg/1 and 1.17 mg/1 respectively at Hwy. 49. Total phosphorus averaged 0.175 mg/1 from 26 samples taken from June 1982 through October 1987 at Hwy. 49. The current and predicted condition of the Crowders Creek cove require this Agency, in an effort to control cultural eutrophication and prevent nuisance conditions from occurring, to request that the State of North Carolina control the phosphorus input to Crowders Creek. This action should take place now in the planning stages for this development and require on the NPDES permit a total phosphorus limit of 2.0 mg/1. The recreational use of the cove is considerable. The Palmetto Girl Scout Camp, used regularly during the summer, is located at Hwy. 49. Direct body contact and other water uses associated with Crowders Creek are present at this location. South Carolina regulations require dischargers to streams not to cause a mixed instream residual chlorine concentration greater than 11.0 ug/1 (average) and 19.0 ug/1 (maximum). The model used in these analyses is attached (last page of printout). The model calculates 19.0 ug/1 (average) and 32.7 ug/1 (maximum) for this 6.0 MGD discharge. The detection limit for total residual chlorine (TRC), according to our Bureau determinations, is 100 ug/1. A limit of 100 ug/1 TRC is expected to be applied to this facility. Lastly, on March 6, our district emergency response team conducted a site inspection of Crowders Creek from Hwy. 557 upstream into North Carolina at I-85/Hwy. 29 between Kings Mountain and Bessemer City in response to complaints of the stream being black and foamy. The source of the problem was not identified but was most likely due to a dye wastewater with surfactants, possibly from a textile plant. No instream samples were taken. Can you advise as to any investigation involving this discharge/spill and the outcome of that investigation? This Agency would appreciate your comments concerning issuance of this permit and to be given the opportunity to address the permit conditions during the public notice period. Ms. Jackie Nowell Page Four March 15, 1988 Also, in reference to the letter that I sent to you in December and our later telecom, please provide me with written comments on the current status and limitations to N. C. dischargers to Steele Creek. We would like to meet in the near future in Raleigh, Columbia, or in our District office in Fort Lawn to discuss water quality management planning that directly affects both agencies. Sincerely, -Z‘K, TerryL. Borders Manager Wasteload Allocation and Certification Section TLB:krw Attachments CC: Jim Joy Chester Sansbury Al Williams File: GMGDWWTP /v c_ c- ve y APPENDIX C $$$ (PROBLEM TITLES) $$$ CARD TYPE TITLE01 TITLE02 TITLE03 NO TITLE04 NO TITLE05 NO TITLE06 NO TITLE07 YES T I TLE08 NO T ITL E09 NO TITLEIO TITLE11 YES TITLE12 TITLE13 YES TITLE14 NO TITLE15 NO ENDTITLE * * * QUAL-2E STREAM QUALITY ROUTING MODEL * * * * * * E.PA/NCASI VERSION * * * QUAL-2E PROGRAM TITLES CRGWDERS.DAT 03-08-36 CROWDERS CREEK FROM NC -LAKE WYLIE FOR PROPOSED NC DISCHARGE INLUDES BEAVERDAM CR TLB 3/3/88 CONSERVATIVE MINERAL I CONSERVATIVE MINERAL II CONSERVATIVE MINERAL III TEMPERATURE BIOCHEMICAL OXYGEN DEMAND IN M5/L ALGAE AS CHL-A IN UG/L PHOSPHORUS CYCLE AS P IN MG/L (ORGANIC-P; DISSOLVED-P) NITROGEN CYCLAS N IN MG/L (ORGANIC-N; AMMONIA-N; NITRITE-N; NITRATE-N) DISSOLVED OXYGEN IN MG/L FECAL COLIFORMS IN N0./100 ML ARBITRARY NON -CONSERVATIVE $$$ DATA TYPE 1 (CONTROL DATA) $$$ CARD TYPE LIST DATA INPUT WRITE OPTIONAL SUMMARY NO FLOW AUGMENTATION STEADY STATE DISCHARGE COEFFICIENTS NO PRINT SOLAR/LCD DATA PLOT DO AND BOD FIXED DNSTRM CONC(YES=1)= INPUT METRIC (YES=1) = NUMBER OF REACHES NUM OF HEADWATERS = TIME STEP (HOURS) _ MAXIMUM ROUTE TIME (HRS)= ENDATA1 0.00000 0.00000 0.00000 0.00000 0.00000 0. 00000 0.00000 0. 00 00 0.00000 6.00000 1.00000 0.00000 30.00000 0.0000 $$$ DATA TYPE 1A (ALGAE PRODUCTION CARD TYPE 0 UPTAKE BY NH3 OXID(MG 0/MG N)= 0 PROD BY ALGAE (MG 0/MG A) = N CONTENT OF ALGAE (MG N/MG A) = ALG MAX SPEC GROWTH RATE(1/DAY)= N HALF SATURATION CONST (MG/L)= LIN ALG SHADE CO (1/FT-U6CHA/L=) LIGHT FUNCTION OPTION (LFNOPT) DAILY AVERAGING OPTION(LAVOPT) = NUMBER OF DAYLIGHT HOURS (DLH) _ ALGY GROWTH CiC OPTION(LGROPT)= ALG/TEMP SOLAR RAD FACT(TFACT) = ENDATA1A CARD TYPE 5D-ULT BOD CONV K COEF = OUTPUT METRIC (YES=1) = NUMBER OF JUNCTIONS = NUMBER OF POINT LOADS = LNTH. COMP. ELEMENT (DX)= TIME INC. FOR RPT2 (HRS)= 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.25000 0. 00000 0.00000 2.00000 0.10000 0. 0 0000 0.00000 AND NITROGEN OXIDATION CONSIANIS) $$$ 3.1400 1.6000 0.0850 2.5000 0.3000 0.0880 2.0000 1.0000 14.0000 2.0000 0.4400 0.0000 CARD TYPE 0 UPTAKE BY NO2 OXID(MG 0/MG N)= 0 UPTAKE BY ALGAE (MG 0/MG A) _ P CONTENT OF ALGAE (MG P/MG A) _ ALGAE RESPIRRTION RATE (1/DAY) _ P HALF SATURATION CONST (MG/L)= NLIN SHADE(1/FT-(UGCHA/L)**2/3)= LIGHT SAT'N COEF (BTU/FT2-MIN) _ LIGHT AVERAGING FACTOR(AFACT) = TOTAL DAILY SOLR RAD (BTU/FT-2)= ALGAL PREF FOR NH3-N (PREEN) = NITRIFICATION INHIBITION COEF = 1.4300 2.0000 0.0120 0. 1(xX, 0.1000 0.0540 0.0400 0.9400 400.0000 0.5000 0. 6000 0. WOO In-t. 1b IILMPLKHIUNt LUfflLL11UN LUNSIHNIS FUH CARD TYPE RATE CODE THETA VALUE MIL CULFF1l:10IS) $$$ THETA( 1) BOD DECA 1.047 DFLT THETA( 2) BOD SETT 1.024 DFLT THETA( 3) OXY TRAN 1.024 DFLT THETA( 4) SOD RATE 1,060 DFLT THETA( 5) ORON DEC 1.047 DFLT THETA( 6) ORGN SET 1.024 DFLT THETA( 7) NH3 DECA 1.083 DFLT THETA( 8) NH3 SRCE 1.074 DFLT THETA( 9) NO2 DECA 1.047 DFLT THETA(10) PORG DEC 1.047 DFLT THETA(11) PORG SET 1.024 DFLT THETA(12) DISP SRC 1,074 DFLT THETA(13) ALG GROW 1.047 DFLT THETA(14) ALG RESP 1.047 DFLT THETA(15) ALG SETT 1.024 DFLT THETA(16) COLT DEC 1,047 DFLT THETA(17) ANC DECA 1.000 DFLT THETA(18) ANC SETT 1.024 DFLT THETA(19) ANC SRCE 1.000 DFLT ENDATA1B $$$ DATA TYPE 2 CARD TYPE STREAM REACH STREAM REACH STREAM REACH STREAM REACH STREAM REACH STREAM REACH ENDATA2 $$$ DATA TYPE 3 CARD TYPE ENDATA3 $$$ DATA TYPE 4 CARD TYPE FLAG FIELD FLAG FIELD FLAG FIELD FLAG FIELD FLAG FIELD FLAG FIELD ENDATA4 $$$ DATA TYPE 5 CARD TYPE HYDRAULICS HYDRAULICS HYDRAULICS HYDRAULICS HYDRAULICS HYDRAULICS ENDATA5 $$$ DATA TYPE CARD TYPE ENDATR5A $$$ DATA TYPE CARD TYPE REACT COEF REACT COEF REACT COEF REACT COEF REACT COEF REACT COEF ENDATA6 (REACH IDENTIFICATION) $$$ REACH ORDER AND IDENT 1.0 RCH =ELEV 610-600 2.0 RCH =ELEV 600-590 3.0 RCH =ELEV 590-580 4.0 RCH =ELEV 580-570 5.0 RCH =ELEV 570-560 6.0 RCH =T0 HWY 49 0.0 FROM FROM FROM FROM FROM FROM (TARGET LEVEL DO AND FLOW AUGMENTATION R. MI/KM 9.5 TO 7,6 TO 6.3 TO 5.2 TO 3.8 TO 2.0 TO O. 0 SOURCES) $$$ R. MI/KM 7.6 6.3 5.2 3.E 2.0 0.0 0.0 REACH RVRIL HDWS TAROT ORDER OF AVAIL SOURCES 0. 0. 0.0 0. 0. 0. 0, 0. 0. (COMPUTATIONAL REACH FLA6 FIELD) $$$ REACH ELEMENTS/REACH 1. 19. 2. 13. 3. 4. 5. 6. O. 11: 14. 20, 18, 0. COMPUTATIONAL FLAGS 1,E,.2.2.2.2.2.2.2.2.2.2.2.2.2.2,2.2.2.O. 2.2.2.2.2.2,2.2.2.2.2,2.2.0.0,0.0,0.0.0. 2,2.2.2,2.2.2.2.2.2,2.0.0.0.0,0.0.0.0.0. 2. 2. 2. 2, 2. 2. 2, 2. 2, 2. 2. 2. 2, 2. 0. 0. 0. 0. 0, 0. 2, 2.2.2.2.2.2.2.2,2.2.2.2.2.2,2.2.2.6,2. 2.2.2.2,2:2.2.2,2,2,2,2.2.2,2.2.2.5.0.0. O.O.O.O.O.O.O, 0.0. 0.0. 0.0. 0.0. 0.0. 0.0. 0. (HYDRAULIC DATA FOR DETERMINING VELOCITY AND DEPTH) $$$ REACH COEF-DSPN 1. 5.90 2, 5.90 3. 5.90 4, 5.90 5. 5.90 6. 5.90 0. 0.00 COEFQV 0.450 0.450 0.450 0.450 0.450 0.450 0.000 EXPOCV 0.001 0.001 0.001 0.001 0.001 0.001 0.000 COEFQH 1.000 1. 000 1.000 1,000 1.000 1.000 0,000 EXPOQH 0.001 0.001 0.001 0.001 0,001 0.001 0.000 5A (STEADY STATE TEMPERATURE AND CLIMATOLOGY DATA) $$$ DUST REACH ELEVATION COEF 0. 0.00 0.00 CMANN 0.047 0.047 0.047 0.047 0.047 0.047 MOO CLOUD DRY BULB WET BULB ATM SOLAR RAD COVER TEMP TEMP PRESSURE WIND ATTENUATION MO 0.00 0.00 0.00 0 0.00 0,00 6 (REACTION COEFFICIENTS FOR DEOXYGENATION AND REAERATION) $$$ REACH K1 K3 SOD RATE 1. 0.60 0.00 0.000 2. 0.40 0.00 0.0(80 S, 0. 40 0.00 0.000 00 4. 0.40 0.00 0.000 5, 0.40 0.00 0.000 6. 0.40 0.00 0.000 0. 0.00 0.00 0.000 K2OPT K2 COEQK2 OR EXPQK2 TSIV COEF OR SLOPE FOR OPT 8 FOR OPT 8 1. 2.60 0.000 0.00000 1. 4.50 0.000 0.000(ro 1. 5.20 0.000 0, 00W0 1. 4.10 0.000 0.00000 1. 2.90 0.000 0.00000 1. 3.20 0,000 0. 00000 0. 0.00 0.000 0.00000 $$$ DATA TYPE 6A (NITROGEN AND PHOSPHORUS CONSTANTS) $$$ CARD TYPE N,AND" COEF REACH CKNH2 SETNH2 1. 0.21 0.00 0 1 0.00 CKNH3 0.30 0.30 CKPORG SETP'JRG 0, (u) 0.00 0.00 0.00 SP04 0.00 0.00 .et u.uu u.JU 0.00 1.00 U.UU 0.00 0.00 N AND P COEF 5. 0.21 0.00 0.30 0.00 1.00 0.00 0.00 0.00 N AND P COEF 6. 0.21 0.00 0.30 0.00 1.00 0.00 0.00 0.00 ENDATA6A 0. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 $$$ DATA TYPE 68 (ALGAE/OTHER COEFFICIENTS) $$$ CARD TYPE REACH ALPHAD AL6SET EXLuLF CK5 CKANC SETANC SRCANC CKCOLI ALG/OTHER COEF 1. 55.00 0.00 0.01 0.00 0.00 0.00 0.00 ALG/OTHER COEF 2. 55.00 0.00 0.01 0.00 0.00 0.00 0.00 ALG/OTHER COEF 3. 55.00 0.00 0.01 0.00 0.00 0.00 0.00 ALG/OTHER COEF 4. 55.00 0.00 0.01 0.00 0.00 0.00 0.00 ALG/OTHER COEF 5. 55.00 0.00 0.01 0.00 0.00 0.00 0.00 ALG/OTHER COEF 6. 55.00 0.00 0.01 0.00 0.00 0.00 0.00 ENDATA6B 0. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 $$$ DATA TYPE 7 (INITIAL CONDITIONS) $$$ CARD TYPE EACH TEMP D.O. 800 CM-1 CM-2 CM-3 ANC COLI INITIAL COND-1 1. 78.80 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-1 2. 78.80 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-1 3. 78.80 0.00 0.00 0.00 0,00 0.00 0.00 0.00 INITIAL COND-1 4. 78.80 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-1 5. 78.80 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-1 6. 78.80 0.00 0.00 0.00 0.00 0.00 0.00 0.00 ENDATA7 0. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 $$$ DATA TYPE 7A (INITIAL CONDITIONS FOR CHOROPHYLL A, NITROGEN, AND PHOSPHORUS) $$$ CARD TYPE REACH CHL-A ORG-N NH3-N NO2-N NO3-N ORG-P DIS-P INITIAL COND-2 1. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-2 2. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-2 3. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-2 4, 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-2 5. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 INITIAL COND-2 6. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 ENDATA7R 0. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 $$$ DATA TYPE 8 (INCREMENTAL INFLOW CONDITIONS) $$$ CARD TYPE REACH FLOW TEMP D.O. BOD CM-1 CM-2 CM-3 ANC COLI INCR INFLOW-1 1. 0.260 78.80 7.20 3.04 0.00 0.00 0.00 0.00 0.00 INCR INFLOW-1 2. 0.200 78.80 7.20 3.04 0.00 0.00 0.00 0.00 0.00 INCR INFLOW-1 3. 0.100 78.80 7.20 3.04 0.00 0.00 0.00 0.00 0.00 INCR INFLOW-1 4, 0.060 78.80 7.20 3.04 0.00 0.00 0.00 0.00 0.00 INCR INFLOW-1 5. 0.130 78.80 7.20 3.04 0.00 0.00 0.00 0.00 0.00 INCR INFLOW-1 6. 0.280 78.80 7.20 3.04 0.00 0.00 0.00 0.00 0.00 ENDATA8 0, 0.000 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 $$$ DATA TYPE 8A (INCREMENTAL INFLOW CONDITIONS FOR CHLOROPHYLL A, NITROGEN, AND PHOSPHORUS) $$$ CARD TYPE REACH CHL-A ORG-N NH3-N .NO2-N NO3-N ORG-P DIS-P INCR INFLOW-2 1. 2.00 0.50 0.44 0.00 0.00 0.00 0.00 INCR INFLOW-2 2. 2.00 0.50 0.44 0.00 0.00 0.00 0.00 INCR INFLOW-2 3, 2.00 0.50 0.44 0.00 0.00 0.00 0.00 INCR INFLOW-2 4. 2.00 0.50 0.44 0.00 0.00 0.00 0.00 INCR INFLOW-2 5. 2.00 0.50 0.44 0.00 0.00 0.00 0.00 INCR INFLOW-2 6. 2.00 0.50 0.44 0.00 0.00 0.00 0.00 ENDATA8A 0. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 $$$ DATA TYPE 3 (STREAM JUNCTIONS) $$$ CARD TYPE JUNCTION ORDER AND IDENT UPSTRM JUNCTION TRIB ENDATA9 0. 0. 0. 0. $$$ DATA TYPE 10 (HEADWATER SOURCES) $$$ CARD TYPE HDWTR NAME ORDER HEADWTR-1 1. CROWDERS CR ENDATA10 0. FLOW TEMP D.D. BOD CM-1 CM-2 CM-3 6.70 78.80 7.20 3.04 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 $$$ DATA TYPE 10A (HEADWATER CONDITIONS FOR CHLOROPHYLL NITROGEN PHOSPHORUS, COLIFORM AND SELECTED NON -CONSERVATIVE CONSTITUENT) $$$ CARD TYPE HDWTR ANC COLI CHL-A ORG-N NH3-N NO2-N NO3-N OR6-P DIS-P ORDER HEADWTR-2 1. 0.00 0.00 2.00 0.50 0.44 0.00 0.00 0.00 0.00 ENDATA10A 0. 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 $$$ DATA TYPE 11 (POINT SOURCE / POINT SOURCE CHARACTERISTICS) $$$ POINT CARD TYPE LOAD NAME EFF FLOW TEMP D.O. BOD CM -I CM-2 CM-3 ORDER POINTLD-1 1. PROPOSED NC 0.00 9.30 78.80 6.00 27.00 0.00 0.00 0.00 p» UNiH IYPt i� tI PtKNIUKt LUKKEl:I1luN��U^iziiWill( Kp�`tll�.110- I�UO Iti1 1$1u U.00 tlVl)HIN11 fir• $$$ DATA TYRE 11R (CCOLIFORMS ANDCSELECTEDINON-CONSERVATIIVECHLOROPHYLL CONSTITUENT) $g;FHOSF'Fh7RUS, 0.00 U. 00 POINT �' CARD TYPE LOAD ANC COLI CHL-R DRG-N NH3-N NO2-N NUS N DRG-P DIS-P ORDER POINTLD-c 1. 0.00 0.00 0,00 0.00 E• 00 0. 0) i;, >0 0. l0 0. 00 _ I POINTLD-2 2. 0,00 0.00 0I,00 0,50 0.77 0,00 ENDATAI IA O. C. 00 0.00 O.00 0,00 0. 00 0.00 O. 00 0, 00 I $$$ DATA TYPE 12 (DAM CHARACTERISTICS) $$$ DAM RCH ELE ADAM BDAM EDAM HDAM ENDATAI2 O. O. 0. 0.00 0.00 0.00 0.00 $$$ DATA TYPE 13 (DOWNSTREAM BOUNDARY CONDITIONS-1) $$$ CARD TYPE TEMP D.O. DOD Cr 1 CM-2 CM-3 ANC COLI ENDATA13 DOWNSTREAM BOUNDARY CONCENTRATIONS ARE UNCONSTRAINED $$$ DATA TYPE 13A (DOWNSTREAM BOUNDARY CONDITIONS-2) $$$ CARD TYPE CHL-A ORG-N NH3-N NO2-N NH3-N ORG-P DIS-P ENDATA13A DOWNSTREAM BOUNDARY CONCENTRATIONS ARE UNCONSTRAINED STEADY STATE ALGAE/NUTRIENT/➢ISSOLVED OXYGEN. SIMMULATION; CONVERGENCE SUMMARY: VARIABLE NUMBER OF ITERATION NONCJNVERGENT ELEMENTS rr NITRIFICATION INHIBITION 1 95 NITRIFICATION INHIBITION NITRIFICATION INHIBITION 3 95 NITRIFICATION INHIBITION 4 95 NITRIFICATION INHIBITION 95 NITRIFICATION INHIBITION 6 NITRIFICATION INHIBITION 7 NITRIFICATION INHIBITION .1 li DISSOLVED OXYGEN IN MG/L RCH/CL 1 2 3 4 5 6 7 1 7.19 6.40 2 5.04 5.13 3 5.87 5.94 4 6.37 6.37 5 6.44 6.42 6 6.30 6.31 6.28 5.21 6.00 6.38 6,40 6.31 6.15 5.29 6.05 6.38 6,338 6.32 6.04 5.93 5.83 5.36 5.43 5.49 6.10 6.15 6.19 6.39 6.39 6.40 6.36 6.35 6.33 6.33 6.34 6.34 ITERATION 8 8 9 10 11 12 13 14 15 16 17 18 19 20 5.73 5,64 5.55 5,47 5.40 5.32 5.26 5,220 5.14 5.09 5,04 4,99 5,56 5.61 5.67 5.72 5.77 5.82 6,24 6.28 6.31 6.35 6.41 6.41 6.42 6,43 6.43 6,44 6.45 6.32 6.31 6.30 6.29 6.28 6.27 6.26 6.26 6.25 6.25 6.24 6.30 6.29 6.35 6.36 6.37 6.38 6.39 6.39 6.40 6.41 6.42 6.43 6,44 BIOCHEMICAL OXYGEN DEMAND IN MG/L RCH/CL 1 2 3 4 5 6 7 8 9 1 3.04 2 13.74 3 12.42 4 11.43 5 10.32 6 8.56 16.79 16.60 16.42 16.23 16.05 13.64 13.53 13.43 13.32 13:22 12.32 12.23 12.14 12.05 11.96 11.35 11.27 11.19 11.11 11,02 10.25 10.17 10.10 10.02 9.95 8.49 8.43 8.36 8.30 8,24 15.87 15.69 15.51 13.11 13.01 12.91 11.87 11.78 11.69 10.94 10.87 10,79 9.88 9.80 9.73 8.17 8.11 8.05 ORGANIC NITROGEN AS N IN MG/L RCH/CL 1 2 3 4 5 6 7 8 1 0.50 0.21 2 0.20 0.20 3 0.19 0.19 4 0.19 0.19 5 0.18 0.18 6 0.19 0.19 0.21 0.20 0.19 0.19 0.18 0.19 0.21 0.21 0.20 0.20 0.19 0.19 0.19 0.19 0.18 0.18 0.19 0.19 0.21 0.21 0.21 0.21 0.20 0.20 0.20 0.20 0.20 0.20 0.20 0.20 0.19 0.19 0.19 0.19 0.19 0.19 0.19 0.19 0.18 0.18 0.18 0.18 0.18 0,18 0.18 0.18 0.18 0.18 0.17 0.17 0.17 0.17 0.19 0.19 0.19 0.18 0.18 0.18 0.18 AMMONIA AS N IN MG/L RCH/CL 1 2 3 4 5 6 7 8 9 10 11 12 1 0.44 1.34 2 1.20 1.19 3 1.10 1.10 4 1.03 1.03 5 0.95 0.95 6 0.84 0.84 1.33 1.32 1.31 1.31 1.30 1.29 1.28 1.27 1.26 1.26 1.18 1,17 1.17 1,16 1,15 1.15 1.14 1.13 1.12 1.12 1.09 1.08 1.08 1.07 1.06 1.06 1.05 1.05 1.04 1.02 1.01 1.01 1.00 1.00 0.99 0.99 0.98 0,97 0.97 0.94 0.93 0.93 0.92 0,92 0.91 0.91 0.90 0.90 0.89 0.83 0.83 0.82 0.82 0,81 0.81 0.80 0.80 0.79 0.79 NITRITE AS N IN MG/L RCN/CL 1 2 3 4 5 6 7 8 9 10 11 12 1 0.00 0.01 0.02 0.02 0.03 0.04 0.05 0.05 0.06 0.07 0.07 0.08 2- 0.13 0.13 0.14 0.14 0.15 0.15 0.16 0.16 0.16 0.17 0.17 0.18 3 -0.18 0.19 0.19 0.19 0.20 0.20 0.20 0.21 0.21 0.21 0.22 4 0.22 0,22 0.22 0.23 0,23 0.23 0.23 0.24 0.24 0.24 0.24 0.24 5 0.25 0.25 0.25 0.25 0.25 0.26 0.26 0.26 0.26 0.26 0.26 0.26 6 0.25 0.26 0.26 0.26 0.26 0.26 0.26 0.26 0.26 0.26 0.26 0.26 RCH/CL 1 1 0.00 2 0.02 3 0.06 NITRATE AS N IN MG/L 2 3 4 5 6 7 8 9 10 11 12 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.01 0.01 0.01 0.03 0.03 0.03 0.03 0.03 0.04 0.04 0.04 0.05 0.05 0.05 0.06 0.06 0.07 0.07 0.07 0,08 0.08 0.09 0.09 0.09 ITERATION 8 10 11 12 13 14 15 16 17 18 19 20 15.34 15.16 14.99 14.83 14.66 14.49 14.33 14.17 14.01 13.85 12.81 12.71 12.61 12.51 11.61 11.52 10.71 10.63 10.55 10.48 10,40 9.66 9.59 9.52 9.45 9.38 9.31 9.24 9.17 9.11 8.69 8.63 7.99 7.93 7.87 7.81 7.75 7.69 7.63 7.57 7.52 ITERATION 8 9 10 11 12 13 14 15 16 17 18 19 20 0.20 0.20 0,20 0.20 0.20 0.20 0.20 0.19 0.18 0.18 0.17 0.17 0.17 0.17 0,17 0.17 0.19 0.19 0.18 0.18 0.18 0. 18 0.18 0.18 ITERATION 8 13 14 15 16 17 18 19 20 1.25 1.24 1.23 1.23 1.22 1.21 1.20 1.11 0.96 0.96 0.89 0.88 0.88 0.87 0.87 0.86 0.85 0.85 0.78 0.78 0.77 0.77 0.77 0.76 ITERATION 8 13 14 15 16 17 18 19 20 0.09 0.09 0.10 0.10 0.11 0.12 0.12 0.18 0.24 0.25 0.26 0.26 0.27 0.27 0.27 0.27 0.25 0.25 0.26 0.26 0.26 0.26 0.26 0.26 ITERATION 8 13 14 15 16 17 18 19 20 0.01 0.01 0.01 0.02 0.02 0.02 0.02 0.05 4 u.1U _1i: 0 U. 0 U; it U.li • 'GI U. Ic •U: 12- U. 1, (1: lt; •• U.14- c5 15 0.'15 5 0.15 0.16 0.16 0.17 0.17 0.18 0.18 0.18 0.19 0.19 0.20 0.20 0.21 0.21 0.22 0.22 0.22 0.23 0.22 0. 2 6 0.23 0.23 0.24 0.24 0.25 0.25 0.25 0.26 0.26 0.27 0.27 0.28 0.28 0.28 0.29 0.29 0.30 0.30 STREAM QURLITY SIMULATION OUTPUT PAGE NUMBER 1 QUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** HYDRRULICS SUMMARY ** ELE RCH ELE BEGIN END POINT INCR TRVL BOTTOM X-SECT DSPRSN ORD NUM NUM LOC LOC FLOW SRCE FLOW VEL TIME DEPTH WIDTH VOLUME AREA AREA COEF MILE MILE CFS CFS CFS FPS DAY FT FT K-FT-3 K-FT-2 FT-2 FT-2/5 1 1 1 9.50 9.40 6.71 0.00 0.01 O.451 0.014 1.002 14.863 7.86 8.91 14.89 0.48 2 1 cc 9.40 9.30 16.03 9.30 0.01 0.451 0.014 1.003 35.419 18.75 19.76 35.52 0,48 3 1 3 9.30 9.20 16.04 0. 00 0,01 0. 451 0. 014 1.003 35.449 18.77 13,78 35.55 0. 48 4 1 4 9.20 9.10 16.05 0.00 0.01 0.451 0.014 1.003 35.480 18.79 19.79 35.58 0.48 5 1 5 9.10 9.00 16.07 0.00 0.01 0.451 0.014 1.003 35.510 18.80 19,81 35.61 0.48 6 1 6 9.00 8.90 16.08 0,00 0.01 0.451 0.014 1.003 35.540 18.82 19.82 35.64 0.48 7 1 7 8.90 8.80 16.10 0.00 0.01 0.451 0.014 1.003 35,570 18.83 19.84 35.67 0.48 8 1 8 8.80 8.70 16.11 0.00 0.01 0.451 0,014 1.003 35.600 18.85 19.86 35.70 0.48 9 1 9 8.70 8.60 16.12 0.00 0.01 0.451 0.014 1.003 35.631 18.87 19.87 35,73 0.48 10 1 10 8.60 8.50 16,14 0.00 0.01 0.451 0,014 1.003 35.661 18.88 19.89 35.76 0.48 11 1 11 8.50 8,40 16.15 0.00 0.01 0.451 0.014 1.003 35.691 18.90 19.90 35.79 O.48 12 1 12 8.40 8.30 16.16 0.00 0.01 0:451 0.014 1.003 35.721 18.91 19.92 35,82 0.48 13 1 13 8.30 8.20 16.18 0.00 0.01 0.451 0.014 1.003 35.751 18.93 19.94 35.85 0.48 14 1 14 8.20 8.10 16.19 0.00 0.01 0.451 0.014 1,003 35.781 18.95 19.95 35.88 0.48 15 1 15 8.10 B.00 16.21 O.00 0.01 0.451 0.014 1.003 35.812 18.96 19.57 35.91 0,4E 16 1 16 8.00 7.90 16.22 0.00 0.01 0.451 0.014 1.003 35.842 18.98 19.98 35.94 0.48 17 1 17 7.90 7.80 16.23 0.00 0.01 0.451 0.014 1.003 35.872 18.99 20.00 35.97 0.48 18 1 18 7.80 7.70 16.25 0,00 0.01 0,451 0.014 1.003 35.902 19.01 20.02 36.00 0.48 19 1 19 7.70 7.60 16.26 0.00 0.01 0.451 0.014 1.003 35.932 19.03 20.03 36.03 0.48 20 2 1 7.60 7.50 16.28 0.00 0.02 0.451 0.014 1.003 35.966 19.04 21 2 2 7.50 7.40 16.29 0.00 0.02 O.451 0.014 1.003 36.000 19.06 22 2 3 7.40 7.30 16.31 0,00 0.02 0.451 0.014 1.003 36.034 19.08 23 2 4 7.30 7.20 16.32 0.00 0.02 0.451 0.014 1.003 36.068 19.10 24 2 5 7.20 7.10 16.34 O. 00 0.02 0.451 0.014 1: 003 36.102 19.12 25 2 6 7.10 7.00 16.35 0.00 0.02 0.451 0.014 1.003 36.136 19.13 26 2 7 7.00 6.90 16.37 0.00 1:3.02 0.451 0,014 1.003 36.170 19.15 27 2 8 6.90 6.80 16.38 0. 00 O. 02 0.451 0,014 1.003 36.204 19.17 28 2 9 6.80 6.70 16.40 0,00 0.02 0.451 0.014 1.003 36.238 19.19 29 2 10 6.70 6. E0 16.41 0. 00 O. 02 0,451 0. 014 1.003 36.272 19.21 20,05 20.07 20.08 20.10 20.12 20.14 20.16 20.17 20.19 20.21 36.07 0.48 36.10 0.48 36.13 0.48 36.17 0.48 36.20 0.48 36.24 0,48 36.27 0.48 36.31 (3.48 36,34 0.48 36.37 0.48 STREAM QUALITY SIMULATION OUTPUT PAGE N'.JMBER 2 QUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** HYDRAULICS SUMMARY ** ELE RCN ELE BEGIN END POINT INCR TRVL BOTTOM X-SECT DSPRSN ORD NUM NUM LOC LOC FLOW SRCE FLOW VEL TIME DEPTH WIDTH VOLUME AREA AREA COEF MILE MILE CFS CFS CFS FPS DAY FT FT K-FT-3 K-FT-2 FT-2 FT-2/S 30 2 11 6,60 6.50 16.43 0.00 0.02 0.451 0,014 1.003 36.306 19.22 20,23 36.41 0.48 31 2 12 6.50 6.40 16.44 0.00 0.02 0.451 0.014 1.003 36.339 19.24 20.25 36:44 0.48 32 2 13 6.40 6.30 16.46 0,00 0.02 0.451 0.014 1.003 36.373 19.26 20.26 36.48 0.48 33 3 1 6.30 6.20 16.47 0.00 0.01 0.451 0.014 1.003 36.393 19.27 20.27 36.50 0.48 34 3 2 6.20 6,10 16.48 0.00 0.01 0.451 0.014 1.003 36.414 19.28 20,29 36.52 0.48 35 3 3 6.10 6.00 16,49 0.00 0.01 0.451 0.014 1.003 36.434 19.29 20.30 38.54 0.48 36 3 4 6.00 5.90 16,50 0,00 0,01 0.451 0.014 1.003 36.454 19.30 20,31 36.56 0.48 37 3 5 5.90 5.80 16,51 0.00 0.01 0.451 0.014 1,003 36.474 19.31 20,32 36.58 0.48 38 3 6 5.80 5.70 16.51 0,00 0.01 0.451 0.014 1.003 36.494 19.32 20.33 36.60 0.48 39 3 7 5.70 5.60 16,52 0.00 0.01 0.451 0.014 1,003 36.514 19.33 20.34 36,62 0.48 40 3 8 5.60 5.50 16.53 0,00 0.01 0.451 0.014 1.003 36,534 19.34 20.35 36,64 0.48 41 3 9 5.50 5.40 16,54 0,00 0.01 0.451 0.014 1.003 36.554 19.35 20.36 38.66 0,48 42 3 10 5.40 5.30 16.55 0,00 0.01 0.451 0.014 014 1.003 36.574 19.37 20,37 36.68 0.48 43 3 11 5.30 5.20 16.56 0.00 0.01 0.451 0.014 1.003 36.534 19.38 20.38 36,70 0.48 -J 44 4 1 5.20 5.10 16.56 0,00(0 0,00 0.451 0. 014 1.003 36.603 19.38 20.39 36.71 0.48 45 4 2 5.10 5.00 16.57 0.00 0,00 0,451 0.014 1.003 36.613 19.39 20.39 38.72 0.48 46 4 7n 5.00 4.90 16.57 0.00 0.00 0.451 0.014 1.003 36.622 19.39 20.40 3.6.73 0.48 47 4 4 4.90 4.80 1E. 58 0.00 0.00 0.451 0.014 1.003 36.632 19,40 20.40 36,73 0.48 48 4 5 4.80 4.70 16.58 0.00 0.00 0.451 0,014 1.003 36.641 19.40 20,41 36.74 0.48 49 4 6 4.70 4.60 16.59 0.00 0.00 0.451 0.014 1.003 36.651 19.41 20.41 36.75 0.48 50 4 7 4.60 4.50 16.59 0,00 0.00 0.451 0.014 1.003 36.660 19.41 20.42 26,76 0.48 51 4 8 4.50 4.40 16.59 0.00 0.00 0.451 0.014 1.003 36,670 19.42 20.42 36,77 0.48 52 4 9 4.40 4.30 16.60 0.00 0.00 0.451 0.014 1.003 36.679 19.42 20.43 36.78 0.48 53 4 10 4.30 4.20 16.60 0,00 0.00 0.451 0.014 1.003 36.688 19.43 20.43 36.79 0.48 54 4 11 4.20 4,10 16,61 0.00 0.00 0.451 0.014 1,003 36.633 19.43 20,44 36.80 0,48 55 4 12 4.10 4,00 16.61 0.00 0,00 0 0,451 0.014 1.003 36.707 19.44 20.44 36.81 0.48 56 4 13 4.00 3.90 16.62 0.00 0.00 0.451 0,014 1.003 36.717 19.44 20,45 36,82 0.48 .. • a• . . h • , , - .s�"YP-r -- --• �"cc _.r-.r •.ice• -..,• STREAM QUALITY SIMULATION OUTPUT PAGE NUMBER 3 QUAL-2E STREAM QUP.LITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** HYDRAL!LICS SUMMARY ** ELE RCH ELE BEGIN END POINT INCR TRVL BOTTOM X-SECT DSPRSN ORD NUM NUM LOC LOC FLOW SRCE FLOW VEL TIME DEPTH WIDTH VOLUME AREA AREA COEF MILE MILE CFS CFS CFS FPS DAY FT FT K-FT-3 -FT-2 FT-2 FT-2/S 57 4 14 3.90 3.80 16.62 0.00 0.00 0.451 0.014 1.003 36.726 19.45 20.45 36.83 0.48 58 5 1 3.80 3.70 16.63 0.00 0.01 0.451 0.014 1.003 36.741 19.45 20.46 36.84 0.48 59 5 2 3.70 3.60 16.63 0.00 0.01 0,451 0.014 1.003 36.755 19.46 20.47 36.86 0.48 60 5 3 3.60 3.50 16.64 0.00 0.01 0.451 0.014 1.003 36.769 19.47 20.47 36.87 0.48 61 5 4 3.50 3,40 16.65 0.00 0.01 0.451 0.014 1.003 36.784 19.48 20.48 36.89 0.48 62 5 5 3.40 3.30 16.65 0.00 0.01 0.451 0,014 1.003 36.798 19.48 20.49 36.90 0.48 63 5 6 3.30 3.20 16.66 0.00 0.01 0.451 0.014 1.003 36.812 19.49 20.50 36.92 0.48 64 5 7 3.20 3.10 16.67 0.00 0.01 0.451 0,014 1.003 36.827 19.50 20.50 36.93 0.48 65 5 8 3.10 3.00 16.67 0.00 0.01 0.451 0.014 1.003 36.841 19.51 20.51 36.94 0,48 66 5 9 3.00 2.90 16.68 0.00 0.01 0.451 0.014 1.003 36.855 19.51 20.52 36.96 0.48 . 67 5 10 2.90 2.80 16.68 0.00 0.01 0.451 0.014 1.003 36.870 19.52 20.53 36.97 0.48 68 5 11 2.80 2.70 16.69 0.00 0.01 0.451 0.014 1.003 36.884 19.53 20.53 36.99 0.48 69 5 12 2.70 2.60 16.70 0.00 0.01 0.451 0.014 1,003 36.898 19.54 20.54 37.00 0.48 70 5 13 2.60 2.50 16.70 0.00 0.01 0.451 0.014 1.003 36.913 19.54 20.55 37.02 0.48 71 5 14 2.50 2.40 16.71 0.00 0.01 0,451 0.014 1.003 36.927 19.55 20.56 37.03 0.48 72 5 15 2.40 2.30 16.72 0.00 0.01 0.451 0.014 1.003 36.941 19.56 20.56 37.05 0.48 73 5 16 2.30 2.20 16.72 0.00 0.01 0.451 0.014 1.003 36.956 19.57 20.57 37.06 0.48 74 5 17 2.20 2.10 16.73 0.00 0.01 0.451 0.014 1.003 36.970 19.58 20.58 37.07 0,48 75 5 18 2.10 2.00 16.74 0.00 0.01 0.451 0.014 1,003 36.984 19.58 20.59 37.09 0.48 76 5 19 2.00 1.90 17.81 1.07 0.01 0.451 0.014 1.003 39.358 20.84 21.84 39.47 0.48 77 5 20 1.90 1.80 17.82 0.00 0.01 0.451 0.014 1.003 39.373 20.85 21.85 39.49 0.48 78 6 1 2.00 1.90 17.84 0.00 0.02 0.451 0.014 1.003 39.407 20.87 21.87 39.52 0.48 79 6 2 1.90 1.80 17.85 0.00 0.02 0.451 0.014 1.003 39.441 20.89 21.88 39.55 0.48 80 6 3 1.80 1.70 17.87 0.00 0.02 0.451 0.014 1.003 39.475 20.90 21.90 39.59 0,48 81 6 4 1.70 1.60 17.88 0.00 0.02 0.451 0.014 1.003 39.510 20.92 21.92 39.62 0.48 82 6 5 1.60 1.50 17.90 0.00 0.02 0.451 0.014 1.003 39.544 20.94 21.94 39.66 0.48 83 6 6 1.50 1.40 17.91 0.00 0.02 0.451 0.014 1.003 39.578 20.96 21.96 39.69 0.48 STREAM QUALITY SIMULATION OUTPUT PAGE NUMBER QUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** HYDRAULICS SUMMARY ** ELE RCH ELE BEGIN END POINT INCR TRVL BOTTOM X-SECT DSPRSti ORD NUM NUM LOC LOC FLOW SRCE FLOW VEL TIME DEPTH WIDTH VOLUME AREA AREA COEF MILE MILE CFS CFS CFS FPS DAY FT FT K-FT-3 K-FT-2 FT-2 FT-2/S 84 6 7 1.40 1.30 17.93 0.00 0. 02 0.451 0.014 1.003 39.613 20.98 21.97 39.73 0.48 85 6 8 1.30 1.20 17.94 0.00 0.02 0.451 0.014 1.003 39.647 20.99 21.99 39.76 0.48 86 6 9 1.20 1.10 17.96 0.00 O.02 0.451 0, 014 1.003 39.681 21.01 22.01 39.80 0.48 87 6 10 1.10 1.00 17.98 0.00 0.02 0.451 0.014 1.003 39.716 21.03 22.03 39.83 0,48 BB 6 11 1.00 0.90 17.99 O. 00 0.02 O.451 O.014 1.003 39.750 21, 05 22, 05 39.86 0.48 89 6 12 0,90 0.80 18.01 0.00 0.02 0,451 O.014 1.003 39.784 21.07 22,07 39.90 0,45 90 6 13 0. 80 O. 70 18. 02 0. 00 0. 02 0. 451 0. 014 1. 003 39. 818 21. 09 22, 08 39. 93 0. 48 91 6 14 0.70 O.60 18,04 0.00 0.02 0.451 0.014 1.003 39.653 21.10 22.10 39.97 O.48 92 6 15 O. 60 0. 50 18. 05 O. 00 0. 02 O. 451 O. 014 1. 003 39, 887 21.12 22,12 40. 00 O. 48 93 6 16 0.50 0.40 18.07 O,00 0.02 0.451 0.014 1.003 39.921 2i.14 22.14 40.04 0.48 94 6 17 0.40 O.30 18.08 0.00 O.02 0.451 0,014 1.003 39,956 21,16 22.16 40,07 0.48 95 6 18 0.30 O.20 18.10 O. 00 0, 02 O.451 0.014 1. 00.3 39.990 21.18 22,17 40,11 0.48 STREAM DUALITY SIMULATION OUTPUT PAGE NUMBER 5 DUAL-_E STREAM DUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** REACTION COEFFICIENT SUMMARY ** RCH ELE DO K2 OXYGN BOD GOD SOD OREN ORB NH3 NH3 NO2 ORSP ORGP DISCI C➢LI ANC ANC ANC: NUM NUM SAT OPT REAIR DECAY SETT RATE DECAY SETT DECAY SRCE DECAY DECAY SETT SRCE DECAY DECAY SETT SRCE Mb/L 1/DAY 1/DAY 1/DAY G/F2D 1/CRY 1/DAY 1/DAY NG/F2D 1/DAY 1/DAY 1/DAY Mt/F2D 1/DAY 1/DAY 1/DAY MG/F2D 1 1 8.11 1 3, 00 0, 79 0, 00 0. 00 0.28 0.0 0.48 0, 00 1.30 0. 00 0. 00 0.0 0, 00 0,00 0.00 0,00 1 2 8.11 1 2.00 0.79 0.00 0,00 o. c8 3) OO 0.47 0. 00 L 29 0, (;O O, O(i (', O(1 O, Oq 0 00 O, 0O 0.0 1 3 8.11 1 3,0 0.79 0,0(1 1),O) 0.213 0.W 0,47 0,00 1,c9 0,(3} (1,O1) 0,00 1).W 0,00 OM 0,(10 1 4 8.11 1 3.00 O. 75 0, 00 0. (u) O. 28 0.00 0.47 0, o0 ha O, Di1 U.1'i 0, (t) t1, 01) mo 0, DO 0. 00 1 5 8.11 1 3, 00 0.79 0.1)1 0, 00 0, LB 0.0 0.47 0.00 1, 28 0.0 0.00 t. 00 0.00 0.OA 0. 00 1 6 8.11 1 3. O(1 0, 79 u, 00 0. DU 0. _8 0.0 0.47 0.0 1.28 0.00 O, (f(.) 0.00 0.0 0, (:0 0, 0O ii, (10 1 7 IA 1 IN 0.79 0.0 0.00 0.28 0. 00 0.47 O, OO 1.28 OM 0,11O 1),110 0.00 0.00 0, C10 0.0 1 8 8, 11 1 3. m o.79 (1, 1)) il, (1)j (1, _8 0, 11(1 O, 47 o (1(1 1, L2 O, Ix; 0.00 0,0 0.0 0.0 0. W 1), ))!1 9 8,11 1 loo 0: 79 (1, OO 0.00 0.28 0. Di! 0.47 0.00 1.27 1), 0) 0. 00 1),1)Q OM 0.0 0.00 0,1 1 10 8,11 1 3, 00 0.75 (1: O0 0,00 0, _8 0.W 0.47 0, 00 1.27 0.00 0.0 OM 0.0 0, 00 MO '1. 00 1 i l 8,11 1 3, 00 0.79 O, OO 0,0 0.28 0. 00 0.47 0.00 1.27 0,0 0, 0+.) 0, 00 0, 00 0. 00 0, 00 OM 1 12 8,11 1 3.m (1. 79 O, O0 0.0 0.28 0.0 0.47 0.00 1,27 0.0 0, 00 ii, 00 0. 00 0.0 0,1) 0. 0O 1 13 8.11 1 3, 00 0.79 0, 13 0.0 0.28 0.0 0.46 0.0 1.26 0. 0) 0.00 0.00 0.00 0. 00 0. (x) 0, W 1 14 MI I 1 3, 00 0.79 0, 01 ) 00 O, c8 0. 00 0.48 0.0 1,26 0.00 0.0 10 0.0 0.00 0. DO 0. 00 0, t,(i 1 15 8,11 1 IN 0.79 1). 00 0, 00 0,28 0.00 0.46 0.00 i , c6 1) )A) 0, 00 0.1 ') 0, 00 0,10 0.00 0. 00 1 16 8.11 1 3, 00 (1, 79 0. (10 0.0 0.28 0, OD 0.46 0.00 1.26 (1.1(' 0.0 0.0 0.0 0. (K1 0. 00 0. W 1 17 8.11 1 3, (u! 0. 79 0, 01) O, O(1 (1, 28 1), D)) O, 46 0.00 1.26 0, 0C 0,0 O, M)O O, 00 1 .O'3 0.0 0.00 1 18 8, 11 1 3. (N1 0. 79 0, 00 0, W 0.28 0.11 0.46 0. 0) 1.25 0, u) 0. 00 0.0 0.00 1) 00 0,00 0.0 1 19 8.11 1 IN 0,79 0. 00 O, 00 0.28 0. 00 0.46 0, 00 ' . 25 O, 00 O, 11Q 0.0 0. 0O 0.00 i), 110 0. 00 n r rar r0rorun_)r�rL 1 8.11 1 4.09 0. 53 0. M 0. 00 0. 28 0. 00 0.46 0. 00 1. 25 0, 0) 0.0 0. 00 0. 00 0. 00 0. 00 MO 0 2 8,':1 1 5, 19 0.2 0, 1))) O, DD 0.28 0, ii0 0,46 0.00 1. c6 O, Oft 0: 00 0. 00 0.00 0.00 0,00 In 1 1 5,19 0.2 0.00 0.00 0.22 0.00 0.46 0.0 1.26 0.0 0, 00 0.0 (1, Oil 0.0 OM 0. W 4 8,11 1 5.19 0.53 0.00 0.00 0.22 0.00 0.4E 0. (;(! 1.26 0.00 0.00 0.00 0.00 0.00 0.00 0.00 5 8.11 1 5.15 0.53 0, 00 0. (1'U 0.28 0, flu 0.46 OM 1.26. 0. WW1 O, f0 (1, OO 0.00 0, 00 O,1)) 0.0 6 8.11 1 5,19 0.53 0, 00 0, 01 0,28 O, 00 0.47 0, 0N! 1, 27 0, 01 0, 00 O, (x) 0, )jN 0.00 0. 00 0,00 7 8. 11 1 5,19 0.2 0, N 0.00 0.28 0. 00 0.47 0. W LP 0.00 O. 00 0.00 OM O, 00 0, 00 0. DO 8 8.11 1 5.19 0.53 0, OO 0,1j0 0, c8 0, 00 0.47 0, D 1.27 0, ('O 0, DD 0.00 0, (10 O: 00 O, 00 0. (10 9 8,11 1 5.19 0.53 0, 00 0, 00 0, a i1 DO 0.47 0, OO 0, Ot1 (', (1 (•, 00 U. DO 0. ;it) 0, 0) (', DO i0 8.11 1 5.19 0.53 0, 00 0. 00 O. 28 0, 00 0.47 0, 00 1.27 0_ (x 0. 00 0. (1t' 0.00 0.00 0,00 STREAM QUALITY SIMULATION OUTPUT PAGE :NUMBER 6 QUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** REACTION COEFFICIENT SUMMARY ** RCH ELE DO 1(2 OXYGN B0D BOD SOD ORGN ORGN NH3 NH3 NO2 ORGP DRGP DISK COLT ANC ANC AN; NUM NUM SAT OPT REPO DECAY SETT RATE DECAY SETT DECAY SRCE DECAY DECAY SETT SRCE DECAY DECAY SETT SRCE MG/L 1/DAY 1/DAY 1/DAY S/F2D 1/DAY 1/DRY 1/DAY MG/F2D 1/DAY 1/DAY 1/DAY MG/F2D 1/DAY 1/D4 1/DAY MG/F2D 2 11 8.11 1 5. 19 0.53 0.00 0.00 0.28 0.00 0.47 ,:).00 1.28 0.00 0.00 0.00 0.00 0.00 0,00 0.00 2 12 8.11 1 5.19 0.53 0.00 0.00 0,28 0.00 0.47 0.00 1.28 0,00 0,00 0,00 0.00 0,00 0.00 0.00 2 13 8. 11 1 5.19 0.53 0.00 0.00 0.28 0.00 0.47 0.00 1,28 0.00 0.00 0.00 0.00 0.00 0.00 0,00 3 1 8.11 1 5.59 0.53 0.00 0.00 0.28 0.00 0.47 0.00 1.28 0.00 0.00 (.00 0.0U �.00 0,00 0.00 3 2 8.11 1 6,00 0,53 O. 00 0,00 0,28 O. (0 0. 47 0,00 1.28 O. 00 0,00 0, 00 0.00 0,00 O. 00 0,00 3 3 8.11 1 6. o0 o, 53 Q. 00 O. OQ 0. 28 0,00 0.47 0, 00 ha i t, 00 0 oo (;, 00 0, 00 0. (;(; 0. 00 (:, Qi1 3 4 8,11 1 6.00 0.53 0. 00 0, 00 0.28 0. 0i1 0.47 0, 00 1, 28 0, 00 0, (30 O ii0 0.00 0.00 0, 00 (j, (; i 3 5 8,11 1 6.00 0.53 0. (i(; 0.00 0.28 0. 00 0.47 0.00 1.28 0.00 0.00 0.00 0.00 0, ). 0. 00 0, Q(% 3 6 8.11 1 6. 00 0. 5.3 0.00 0, (;;j 0.28 0. 00 0.47 0. 00 1,6 0. 00 0.00 0. 0n 0.00 0.00 0.00 0, W 3 7 8, i 1 1 6, 00 0. 53 0.00 0.00 0.28 0,00 0.47 0. 00 1, 29 0, (0 0. 00 0. 00 0. (i0 0.00 0.00 0, 00 t. 3 8 8,11 i 6. 00 0. 53 0. 00 0, Q(, Q, 28 (;, (;0 0, 47 0. 00 1, 23 0, 00 0. 00 0, (i(; 0, 00 0, 00 i;, 00 0. 0ij 3 9 8.11 1 6.00 0,53 0.00 0,00 0,28 0.00 0.47 0.00 1.29 0.00 0,00 0.00 0.00 0.00 0.00 0.00 3 10 8.11 1 6.00 0. 53 0. UO 0. 00 0.28 0.00 0. 47 O. 00 1.29 0.00 0.00 O. 0;i O. OG 0.00 O. 00 O. Q0 3 11 8.11 1 6.00 0,53 0. 00 0,00 0. 28 0. 00 0,47 0. 00 1. 29 0. 00 0. 00 0, 00 O. 00 0. 00 0.00 0. 00 4 1 8.11 1 5. _,6 0. 53 0. 00 0.00 0.28 0,00 0.47 0,00 1,29 0. 00 0. 00 0. 00 0. 00 0. 00 0. 00 0.00 4 2 8.11 1 4.73 0. 53 0. 00 0. 00 0, c8 0. 00 0.47 0. 00 1.29 Q. 00 0, 00 0, 00 0.00 0, 00 0, 00 0, 00 4 3 8,11 1 4.73 0. 53 0, 00 Q. (0 0. 28 0, 00 0.47 0.00 1, 29 0.00 0.00 O. 00 0.00 O. 00 0, 00 0, 00 4 4 8.11 1 4.73 0.2 0.00 0.00 0.28 0,00 0.47 0.00 1.29 0.00 0.00 0.00 0, 00 0. Qii 0, 0(l 0, (li 4 5 8.11 1 4.73 0.2 0.00 0.00 0.28 0.00 0,47 0.00 1,29 0, 00 0, 00 it, fiO 0.00 (;, Qil 0.00 0,00 4 6 9.11 1 4.73 0. 53 0.00 0. 00 0. 28 0.00 0.47 0. 00 1.29 0: 00 0.00 0.00 0.00 0. p0 0. (;0 0,00 4 7 8.11 1 4.73 0. 53 0. 00 0.00 0.28 0. 00 0. 47 0. Q0 1.29 Q. 00 0.00 (;, 00 O. 00 O. O0 0, 00 0, co 4 8 8.11 1 4.73 0.53 0.00 0,00 0.28 O.00 0.47 O.00 1.29 0,00 0,00 0.00 0.00 0.00 0,00 0,00 4 3 8.11 1 4.73 0. 53 O. iii) 0, (;r) 0.28 0.00 0.47 0, 00 1, 29 0, 00 0, 00 0, i10 0, 00 (j, 00 (j, 0(j 0, 00 4 10 8.11 1 4. 73 0. 53 0. (i(? 0. 00 0. 28 (i, 0(; 0. 47 0. 00 I. 29 0.00 0,00 0. QQ 0.00 0.00 O. 00 0,00 4 11 8.11 1 4.73 0.53 0.00 0. 00 0.6 0.00 0.47 0. 00 1.6 (i, r)(i 0, (ui 0.00 0, (nj 0, 00 0. 00 0.00 4 12 8,11 1 4.73 0. 53 0, 00 0, 00 0. 28 0, O(i i.;, 47 0. 00 1. 29 0. 00 0, 00 0.00 0.00 0. 0(i 0, 00 0,00 4 13 8.11 1 4,73 0. 53 0.00 0,00 0. 28 0,00 0. 47 0,00 1.29 0,00 0.00 0, o: 0,00 O. 00 0,00 0,00 RCH ELE NUM NUM STREAM QUALITY SIMULATION OUTPUT PAGE NUMBER 7 QUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** REACTION COEFFICIENT SUMMARY ** D0 K2 OXYGN 80D 80D 50D ORGN ORGN NH3 NH3 NO2 ORGP NSA DISP COLI ANC ANC ANC SAT OPT REAIR DECAY SETT RATE DECAY SETT DECAY SRCE DECAY DECAY SETT SRCE DECAY DECAY SETT SRCE MG/L 1/DAY 1/DAY 1/DAY G/F2D 1/DAY 1/DAY 1/08? 'i8/F2D 1/DAY 1/DAY 1/DAY MG/F2D 1/DAY 1/DAY 1/DAY M6/F2D 4 14 8.11 1 4.73 0.53 0.00 0.00 0.28 0.00 0.47 0.00 1.29 0.00 0. 00 0.00 0.00 0.00 0.00 0.00 5 1 8.11 1 4.04 0. 53 0, 00 0. 00 0. 28 0. 00 0. 47 0. 00 La 0. 00 0. 00 0. 00 0. 00 O, 00 5 2 8,11 1 134 0. 53 MO O. 00 0.28 0.00 0.47 0, 00 La 0. Oi) 0, 0O O, 00 0, i)i) 0.0 (, 00 0. 00 5 3 8.11 1 134 0. 53 0.00 0. 00 0.28 0. 00 0.47 O. 0 1.29 0,00 0, 00 0.00 0.00 0, 00 ( ()0 (1, 00 5 4 8.11 1 134 0,53 MO 0. i)i) 0.28 0.0 0,47 0.00 1,29 0. 00 0, (n) 0,00 0,00 0,00 0. 00 0.00 5 5 8.11 1 3.34 0. 53 0.00 0.00 O. 28 0.00 0.47 0, 00 1. 29 0 00 0. (r) 0. DO 0. 00 0. 00 (1. 00 0, (0 5 6 8.11 1 134 0.53 0.00 0.00 0.28 0.0 0.47 0.00 1.6 0.0 0,00 0. (1i) 0,00 0,00 0,00 0,00 5 7 8.11 1 8 8.11 r.34 ).5 3.34 0.53 0.00 0.00 0,28 0.00 0.47 0.00 1. 29 O, (1O 0.0 0.00 0.00 0.00 0.00 0.0 5 ( 0.00 0.00 0.28 0.00 0.47 0.00 1.6 0.00 (1, 00 0, Oi) (i, Ili) (1, i)0 i1, 00 O, M � .,,< , 5 9 8.11 1 134 0.53 0, 00 0, 00 0. 28 0, 00 0.47 0, 00 1.29 MO 0.00 0.00 (1, ( 0.00 0.00 0.0 5 10 8.11 1 134 (. 53 0.00 (, 0O 0.28 0. 00 0.47 0. 0 1.29 MO i), 00 0, 00 0.00 0.00 0, 0 0,00 5 11 8, 11 1 34 0. 53 0. 00 0. 0{. 0. 2a (i, OO 1), 47 (1, 00 1, 29 0.00 O. 00 o o 1 O, 00 0.00 O, 00 0,00 5 12 8,11 1 3.34 0.53 0,i)0 (.00 0.28 0,00 0.47 0.00 1.29 0,00 0,00 0,00 0.00 0,00 0,00 0,00 5 13 8.11 1 3. 34 0. 53 0.00 0, 0' 0.28 0.00 0.47 0.00 1.29 0.00 O. O0 0.00 0 (10 0.00 0, 00 0, 00 5 14 8.11 1 3.34 0. 53 (1 0(1 0. 0i.) 0. 28 0. 00 0.47 0. (0 La 0. i)0 O. GO 0, i)0 (. 00 (, 00 0. 00 0. 00 5 15 8.113.34 0.53 0.0 0, 00 0, 28 0, 00 0,47 (1, O(1 1. 29 0. 00 0.00 0 00 0. 0O 1. 00 0.00 0.00 5 16 8.11 1 134 0. 52 O, 0i) O, O(i O, 28 i), 0(1 0.47 0. 00 La 0.00 O. 00 0.0 0.00 0.00 0. 00 0. 00 5 17 8.11 1 134 0.53 0.0 O 00 0.28 0.0 0,47 0.0 1.29 0.0 0.0 0,00 0.0 0.00 0.0 0, (1O 5 18 8,11 1 3. 34 0.53 0, 00 O. (x) 0, 28 0. 00 0.47 0. 00 La ('), 00 0, 00 0. 00 1 00 i1 00 0. 00 5 19 8.11 1 3. 34 0. 53 0.00 0. 00 0.28 O. 00 0.47 0. 00 L 29 (()() 1 00 0. 00 0, 00 0, 00 t), 00 O, O0 5 20 8. i 1 1 134 0.53 0. 00 0, OO 0.28 0.00 0.47 0.00 La 0, 00 o. (x) i), 00 0. 00 0.0 0.00 6 1 8.11 1 3.52 0.53 0.00 0.00 0.28 0.00 0.47 0.00 1.29 0.00 0.00 0.00 0.00 0.00 0.00 0.00 6 L 8.11 1 2 63 11..i3 0. ()( 0.00 O. 28 (. u0 0.47 0.00 1.29 O, ()(,I t), (Il) 0.00 0.0 0.00 0.0 O. ()() 6 3 8.11 1 3.69 0.53 0, 0O (1, (y: (1, 28 0, 00 0. 47 0. OO La O. 00 1 00 0.00 0, (1O O.10 0.00 O. 00 6 4 8.11 1 3.69 0.53 0.00 0,00 0.28 0.00 0.47 O.00 1.29 0,01 O. 0.00 0.00 0.00 0.00 0.00 6 5 8.11 1 3.69 0.53 0.00 0.(10 0,28 0.00 0.47 0.00 LEI 0.00 0.00 0,00 0.0(1 0,00 0.00 0.00 6 6 8.11 1 3,69 0.53 (1, 00 0. (u) 0.28 0, (y) 0.47 i), i)O La 0, OO 0. )0 0. (x0. i)0 0. 00 i), Oo 0. 00 STREAM QUALITY SIM&ATION OUTPUT PAGE NUMBER 8 DUAL-2E STREAM QUALITY ROUTIN3 MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** REACTION COEFFICIENT SUMMARY ** RCH ELE DO K2 OXYGN HOD BCD SOD ORGN ORGN NH3 NH3 NO2 ORBP ORGP DISP COLI ANC ANL ANC NUM NUM SAT OPT REAIR DECAY SETT RATE DECAY SETT DECAY SRCE DECAY DECAY SETT SRCE DECAY DECAY SETT SRCE MG/L I/DAY 1/DAY 1/DAY G/FeD 1/DAY 1/DAY 1/DAY MG/FcD 1/DAY I/DAY 1/DAY MG/F?D 1/DAY I/DAY 1/DAY MG/F2D 6 7 8,11 1 3.69 p, 53 0, 00 0. 00 0, c8 0. 00 0, 47 O. 00 1, 29 p, 00 0. 00 o. 00 O.00 0. pit p, 00 6 8 8.11 1 169 0.53 0.00 0.0 0.28 0.0 0.47 0.00 1.29 0.00 0.00 0. 00 0.00 0. 00 0.0 0.00 6 9 8.11 1 169 0.53 0.00 0.00 0.28 0.00 0,47 0.00 1.29 0.00 0.00 0.00 0.00 00 0.00 0.00 6 10 8.11 1 3.69 0.2 0.0 0.00 0.28 0.00 0.47 0.0 1.29 ((. O(( 0.00 0, 00 0.00 0, 00 0. 00 MO 6 11 8, I 1 1 3.69 0.53 0.00 0.0 0.28 0.0 0.47 0.00 1.6 0, pp 0.00 0.00 0.0 0.00 0.00 0, a 6 2 8.11 1 3.69 0.2 0.00 00 0.28 MO 0.47 0. 00 1.6 0. DO 0. DO 0.00 0, (u) 0.00 0.00 (:, pp 6 13 8.11 1 3.69 0.53 0.00 0. W 0.28 MO 0.47 0. N 1.6 :i, 0(J 0.00 0.00 0.00 p, (rci 0.00 0.00 6 14 8.11 1 3.69 0.2 0. p0 0.0 0.28 0.0 0.47 0.0 1. L 0.00 0.00 0.0 0.00 0.0 0.0 p: Op 6 15 8.11 i 169 0.53 MO 0.00 0.28 0.00 0, 47 0.00 1.29 0.00 0.00 O, 00 p, (((3 MO O, OO 0.00 6 16 8.11 1 3.69 0.53 0.0 0.00 ((. c8. 0.00 0.47 0.00 1.29 O.00 O: 00 0,00 0.00 0. (TM( 0.00 0.00 6 17 8.11 i 3.69 0.53 0.00 0. (n; 0.28 0. (u) 0.47 0. Di) 1.29 0, pO (, (H) 0,00 0, OO 0.00 0.00 0.00 6 18 8,11 1 169 0.2 (+. 0 ( 0.00 0.28 0.00 0.47 0.0 1.6 MO 0. O( 0.0 0.00 0.00 0.00 0. pO STREAM QUALITY SIMULATION OUTPUT PAGE ►AMBER 9 QUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** WATER QUALITY VARIABLES ** IRCH ELE CM-1 CM-2 CM-3 ANC NUM NUM TEMP DO BOD ORGN NH3N NC2N NO3N SUM-N ORGP DI5-P SUM-P COLT CHL4 DES-F MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L #/100M` UG/L 1 1 78.80 0.00 0.00 0.00 7.19 3.04 0.50 0.44 0.00 0.00 0.94 0.00 0.00 0.00 0.00 0.00 0.00 1 2 78.80 0.00 0.00 0.00 6.40 16.79 0.21 1.34 0.01 0.00 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 3 78.80 0.00 0.00 0.00 6.28 16.60 0.21 1.33 0.02 0.00 1.55 0.00 0.00 0.00 0.00 0.00 0,00 1 4 78.80 0.00 0.00 0.00 6.15 16.42 0.21 1.32 0.02 0.00 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 5 78.80 0.00 0.00 0.00 6.04 16.23 0.21 1.31 0.03 0.00 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 6 78.80 0.00 0.00 0.00 5.93 16.05 0.21 1.31 0.04 0.00 1.55 0.00 0,00 0.00 0,00 0.00 0.00 1 7 78.80 0.00 0.00 0.00 5.33 15.87 0.21 1.30 0.05 0.00 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 8 78.80 0.00 0.00 0,00 5.73 15.69 0.21 1.29 0.05 0,00 1.55 0.00 0.00 0.00 0.00 0,00 0.00 1 9 78.80 0.00 0.00 0.00 5.64 15.51 0.21 1.28 0.06 0.00 1.55 0.00 0,00 0.00 0.00 0.00 0.00 1 10 78.80 0.00 0.00 0.00 5.55 15.34 0.20 1.27 0.07 0.01 1.5-5 0.00 0.00 0.00 0.00 0.00 0.00 1 11 78.80 0.00 0.00 0.00 5.47 15.16 0.20 1.26 0.07 0.01 1.55 0.00 0.00 0.00 0.00 0.00 0 0.00 1 12 78.80 0.00 0.00 0.00 5,40 14.99 0.20 1.26 0.08 0.01 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 13 78.80 0.00 0.00 0.00 5,32 14.83 0.20 1.25 0.09 0.01 1.55 0.00 0.00 0.00 0.00 0.00 0. 00 1 14 78.80 0.00 0.00 0.00 5.26 14.66 0.20 1.24 0.09 0.01 1.55 0,00 0.00 0.00 0.00 0.00 0.00 1 15 78.80 0.00 0.00 0.00 5.20 14.49 0.20 1.23 0.10 0.01 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 16 78.80 0.00 0,00 0,00 5,14 14.33 0.20 1.23 0.10 0.02 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 17 78.80 0.00 0.00 0.00 5.09 14.17 0.20 1,22 0.11 0.02 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 18 78.80 0.00 0.00 0.00 5.04 14.01 0.20 1.21 0.12 0.02 1.55 0.00 0.00 0.00 0.00 0.00 0.00 1 19 78.80 0.00 0.00 0.00 4.99 13.85 0.20 1.20 0.12 0.02 1.55 0.00 0.00 0.00 0.00 0.00 0.00 2 1 78.80 0,00 0.00 0.00 5.04 13.74 0.20 1.20 0.13 0.02 1.55 0.00 0.00 0.00 0.00 0.00 0.00 2 2 78.80 0.00 0.00 0.00 5.13 13.64 0.20 1.19 0.13 0.03 1.54 0.00 0.00 0.00 0.00 0.00 0.00 2 3 78.80 0.00 0.00 0,00 5.21 13.53 0.20 1.18 0.14 0.03 1.54 0.00 0.00 0,0+) 0.00 0.00 0.00 2 4 78.80 0.00 0.00 0.00 5.29 13.43 0.20 1.17 0.14 0.03 1.54 0.00 0.00 0.00 0.00 0.00 0.00 2 5 78.80 0.00 0.00 0,00 5.36 13.32 0.20 1,17 0.15 0.03 1.54 0.00 0.00 0.00 0.00 0.00 0.00 2 6 78.80 0.00 0.00 0.00 5.43 13.22 0.20 1.16 0.15 0.03 1.54 0.00 0.00 0.00 0.00 0.00 0.00 2 7 78.80 0.00 0.00 0.00 5.49 13.11 0.20 1.15 0.16 0.04 1.54 0.00 0.00 0.00 0.00 0.00 0.00 2 8 78.80 0.00 0.00 0.00 5.56 13.01 0.20 1.15 0.16 0.04 1.54 0.00 0.00 0.00 0.00 0.00 0.00 2 9 78.80 0.00 0.00 0.00 5.61 12,91 0.20 1.14 0.16 0,04 1.54 0.00 0.00 0.00 0.00 0.00 0.00 2 10 78.80 0.00 0.00 0.00 5.67 12.81 0.20 1.13 0.17 0.05 1.54 0.00 0.00 0.00 0.00 0.00 0.00 STREAM QUALITY SIMULATION OUTPUT PAGE NUMBER 10 DUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** WATER QUALITY VARIABLES ** RCN ELE CM -I CM-2 °A-3 ANC NUM NUM TEMP DO BOD ORGN NM3N NO2N NO3N SUM-N ORGP DIS-P SUM-P COL: CHLA DEG-F MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L #/100ML US/L 2 11 am m() mo mo 5.72 12.71 0. 13 1.12 0.17 0.05 1,54 0.00 0.00 0.00 0,00 0.00 0.00 2 12 78.3D 0.00 0,00 OM 5,77 12.61 0.19 1.12 0.18 0,05 1.54 0.01) 0.00 0,00 0.00 1) 0)) 0.00 2 2 am mo mo om 5.82 12,51 0.19 1. 11 0.18 0,05 154 0.00 0.00 0.00 0.00 0.00 0.00 3 1 i 78.80 0.00 0,00 0.00 5.87 12,42 0,19 1.10 0.18 0.06 1.54 0.00 O. 00 O. 00 0.00 O. 00 O. 00 3 2 78.80 0.00 O. 00 O. 00 5.94 12.32 O. 13 1,10 0,19 0.06 1.54 O. 00 O. 00 0.00 O. 00 O. 00 O. 00 3 3 78.80 O. 00 O. 00 O. 00 6.00 12.23 O. 19 1. 09 O. 19 O. 06 1.54 1) 0) O. 00 O. 00 O. i". 0 O. 00 O. Ou 3 4 78,80 ;2.00 O. 00 O. 00 E,. 05 12.14 O. 19 1.(18 0.19 :.). 07 1.54 O. 00 O. 00 O. 00 1) IX, O. 00 1) '.10 3 , 5 78.80 O. 00 0.00 O. 00 6,10 12.05 O. 13 1.08 O. 20 0.07 1.54 0.00 O. 00 0.00 O. 00 u. 00 o. 00 3 6 78.80 O. 00 (1 0)) O. 00 s. 15 11 96 0,19 1.07 O. 20 0,07 1.54 O. 00 O. 00 0,00 O. 00 O. 00 O. 00 3 7 78.80 O. 00 O. 00 0,00 6.19 11,87 0.19 1.08 O. 20 0.08 1.54 O. 00 O. 00 0.00 0.00 O. (g) O. 00 8 78.80 O. 00 0,00 0,00 6. 24 11.78 O. 19 1.06 0,21 0,08 1.54 O. (1' 0.00 O. 00 0.00 O. 00 3 9 am mo om mo 6.28 11.69 0.19 1,05 0.21 0.09 1,54 0.00 0.00 0.00 0.1)1) 0.00 0.00 3 10 78, Bo ,-.., 00 0,00 o. 00 B, 31 11, 61 0,19 1„ 05 0.21 (1 09 1,54 0,0,) 0, 00 0, 00 0, 00 0, 00 0, 00 3 11 78.80 0.00 0.00 0. 00 6.35 1 i . 52 0, 19 1.04 0. 22 O. 09 1.53 0.00 0.00 0.00 O. 00 0.00 0.00 4 1 78.80 0.00 0.00 0.00 6,37 11.43 0.19 1.06 0.22 0.10 1,53 0.00 0.00 OM OM 0.00 0.00 4 2 am o.w om mo 6.37 11.35 0.19 1.0,3 0,22 0.10 1,53 0.00 0.00 0,00 0.0 0.00 0.00 4 3 78.80 O. 00 O. 00 1.) ((1 E.. 38 11.27 O. 19 1, c.12 0.22 O. 10 1.53 O. 00 O. 00 0.00 O. 00 O. 00 0,00 4 4 78.80 0,00 0.00 0,00 6.38 11 19 0.19 1.01 O. 23 0,11 1.53 0.00 O. 00 0,00 0.00 1). 00 O. 00 4 5 78.80 0,00 O. 00 O. 00 6.39 11 11 O. 19 1.01 O. 23 O. 11 1,53 O. 00 O. 00 O. 00 O. 00 O. 00 O. 00 4 6 78.80 0,00 O. 00 O. 00 6.39 11.02 O. 18 1.00 0,23 0,12 1.53 0.00 O. 00 0.00 O. 00 O. 00 0.00 4 7 78.80 O. 00 0,00 O. 00 6.40 10.94 0,18 1,00 O. 23 0.12 1,53 O. 00 0.00 O. 00 O. 00 0,00 O. 00 4 8 78.80 0,00 O. 00 O. 00 6.41 10,87 O. 18 O. 99 0.24 O. 12 1.53 O. 00 0.00 O. 00 O. 00 0.00 O. 00 4 9 78.80 O. 00 O. 00 0,00 E,. 41 10.79 O. 18 O. 99 O. 24 0.13 1.53 O. 00 O. 00 O. 00 0.00 O. 00 O. 00 4 10 78.80 0.00 O. 00 0,00 6,42 10. 71 O. 18 0.58 O. 24 0.13 1.53 O. 00 O. 00 O. 00 O. 00 O. 00 0,00 4 11 78.80 0,00 O. 00 O. 00 6.43 10.63 0.18 O. 97 O. 24 0,14 1.5.13 0.00 O. 00 O. 00 O. 00 O. 00 0.00 4 12 78.80 O. 00 0.00 O. 00 6.43 10,55 0,18 0.97 O. 24 0.14 1.53 O. 00 O. 00 0.00 O. 00 O. 00 1) 00 4 13 78.80 O. 00 O. 00 0,00 6.44 10.48 O. 18 O. 96 0,24 0. 15 1. 53 0. 00 O. 00 O. 00 0.00 0.00 ((.00 STREAM QUALITY SIMULATION • QU-PUT PAGE NUMBER 11 QUAL-2E STREAM QUALITY ROUTING MODEL Ertl/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** HATER QUALITY VARIABLES ** RCH ELE CM-1 CM-2 CM-3 ANC NUM NUM TEPP DO BUD ORGN NH3N NO2N NO3N SUM-N ORGP D1S-P SL -P COLI CHLA DEG-F MG/L MG/L MG/L MG/L MG/L MM3/L MG/L MG/L MG/L MG/L #/100ML UG/L 4 14 78.80 0. 00 0.00 0. 00 6.45 10.40 0.18 0.96 0. 25 0.15 1.53 0,00 0. 00 O.00 0. 00 0. 00 0.00 5 1 78.80 0.00 0.00 0.00 6.44 10.32 0.18 0.95 0.25 0.15 1.53 0,00 0.00 0,00 0.00 0.00 O.00 5 2 78.80 0. 00 0. 00 0.00 6.42 10.25 0.18 0. 95 0. 25 0.16 1,53 0. 00 0. 00 0. 00 0. 00 O. 00 0. 00 5 3 78.80 0.00 0. 00 0. 00 6.40 10.17 0.18 0,94 0. 25 0.16 1.53 0. 00 0.00 0.00 0.00 0.00 0.00 5 4 78.80 0. 00 0. 00 0.00 6.38 10.10 0.18 0. 93 0.25 0.17 1.53 0. 00 0. 00 0. 00 0. 00 0.00 0,00 5 5 78.80 0. 00 0. 00 0. 00 6.36 10.02 0.18 0. 93 0.25 0.17 1.53 O. 00 0.00 0,00 0.00 0.00 3.00 5 6 78.80 0.00 0.00 0. 00 6.35 9. 95 0.18 0. 92 0.26 0.18 1.53 0. 00 0.00 0.1)0 0,00 0.00 0. 00 5 7 78.80 0.00 0.00 0.00 6.33 9.88 0.18 0.92 0.26 0.18 1.53 0.00 0.00 0,00 0.00 0.00 0.00 5 8 78.80 0,00 0.00 0.00 6.32 9,80 0.18 0.91 0.26 0.18 1.53 0,00 0.00 0. 00 0.00 0.00 0.00 5 9 78.80 O. 00 0.00 0.00 6.31 9.73 0.17 0.91 O. 26 0.19 1,53 0.00 0.00 0.00 0.00 0.000 0.00 5 10 78. 80 0.00 0. 00 0.00 6.30 9.66 0.17 O. 90 0.26 0.19 1.53 O. 00 0.00 0.00 0. 00 0.00 O. 00 5 11 78.80 0.00 0.00 0.00 6,29 9.59 0.17 0.90 0.26 0.20 1.53 0.00 0.00 0,00 0.00 0.00 0.00 5 12 78. B0 0. 00 0. 00 0. 00 6.28 9.52 0.17 0. 89 0. 26 0.20 1,53 O. 00 0. 00 O. 00 0,00 0,00 0. 00 5 13 78.80 0.00 0.00 0.00 6,27 9.45 0.17 0.89 0.26 0.21 1.53 0.00 0.00 0.00 0.00 0.00 0.00 5 14 7B. 80 0. 00 0.00 0.00 6.26 9.38 0.17 0. 88 0.26 0. 21 1.53 0. 00 0. 00 0,00 0,00 0,00 O. 00 5 15 78.80 0.00 0.00 0.00 6.26 9.31 0.17 0.88 0.27 0.22 1.53 0.00 0.00 0.00 0.00 O.00 0.00 5 16 78.80 0.00 0.00 0.00 6.25 9.24 0.17 0.87 0.27 0.22 1.53 0.00 0.00 0.00 0.00 0. 00 0.00 5 17 78.80 0.00 0. 00 0. 00 6.25 9.17 0.17 0. 87 0. 27 0. 22 :. 53 O. 00 0.00 0,00 0. 00 0. (X) 0. 00 5 18 78.80 0.00 0.00 0.00 6.24 9.11 0.17 0.86 0.27 0.23 1.53 0.00 0.00 0.00 0.00 0.00 0.00 5 19 78.80 0,00 0.00 0.00 6.30 8.69 0.19 0.85 0.25 0.22 1.51 0.00 0.00 0.00 0.00 0.00 0.00 5 20 78.80 O. 00 0. 00 0. 00 6.29 8.63 0.19 O. 85 0,25 0. 22 i. 51 O. 00 0,00 0. 00 0. 00 O. 00 0. 00 6 1 78.80 0. 00 0.00 0.00 6.30 8.56 0.19 0.84 0.25 0.23 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 2 78.80 0. 00 0. 00 0,00 6.31 8.49 0.19 0.84 O. 226 0. 23 1.51 0. 00 0.00 0.00 0.00 0. 00 0.00 6 3 78.80 0.00 0.00 0. 00 6.31 8.43 0.19 0. 83 0. 26 0. 24 1.51 0. 00 0. 00 0.00 0. 00 0. 00 0. (X) 6 4 78.80 0.00 0. 00 0. 00 6.32 8.36 0.19 0. 83 0. 26 0. 24 1.51 0. 00 0. 00 0,00 0.00 0. 00 0,00 6 5 78.80 0.00 0.00 0.00 6.33 8.30 0.19 0.82 0.26 0.25 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 6 78.80 0.00 0.00 0.00 6.34 8.24 0.19 O.82 O.26 0.25 1.51 0.00 0.00 0.00 0.00 0.00 0.00 STREAM QUALITY SIMULATION OUTPUT PAGE NUMBER 12 QUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** WATER QUALITY VARIABLES ** RCH ELE CM-1 CM-2 CM-3 ANC NUM NUM TEMP DO BOD ORGN NH3N NON NO3N SUM-N ORGP DIS-P SUM-P COLI CHLA DEG-F MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L MG/L #/100ML LAC/L 6 7 78.80 0.00 0.00 0.00 6.34 8.17 0.19 0.81 0.26 0.25 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 8 78.80 0.00 0.00 0.00 6.35 8.11 0.19 0.81 0.26 0.26 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 9 78.80 0.00 0.00 0.00 6.36 8.05 0.18 0.80 0.26 0.26 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 10 78.80 0.00 0.00 0.00 6.37 7.99 0.18 0.80 0.26 0.27 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 11 78.80 0.00 0.00 0.00 6.38 7.93 0.18 0.79 0.26 0.27 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 12 78.80 0.00 0.00 0.00 6.39 7.87 0.18 0.79 0.26 0.28 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 13 78.80 0.00 0.00 0.00 6.39 7.81 0.18 0.78 0.26 0.28 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 14 78.80 0.00 0.00 0.00 6.40 7.75 0.18 0.78 0.26 0.28 1.51 0.00 0.00 0.00 0.00 0.00 0,00 6 15 78.80 0.00 0.00 0.00 6.41 7.69 0.18 0.77 0.26 0.29 1.51 0.00 0.00 0.00 0.00 0.00 0.00 6 16 78.80 0.00 0.00 0.00 6.42 7.63 0.18 0.77 0.26 0.29 1.50 0.00 0.00 0.00 0.00 0.00 0.00 6 17 78.80 0.00 0.00 0.00 6.43 7.57 0.18 0.77 0.26 0.30 1.50 0.00 0.00 0.00 0.00 0.00 0.00 6 18 78.80 0.00 0.00 0.00 6.44 7.52 0.18 0.76 0.26 0.30 1.50 0.00 0.00 0.00 0.00 0.00 0.00 STREAM QUALITY SIMULATION OUTPUT PAGE NUMBER 13 PURL-2E STREAM QUALITY ROUTING MODEL EFTA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** DISSOLVED OXYGEN DATA ** COMPONENTS OF DISSOLVED OXYGEN MASS BALANCE (MG/L-DAY) ELE RCH ELE DO DO TAM NIT ORD NUM NUM TEMP SAT DO DEF INPUT INHIB F-FNCTN OXYGN NET DEG-F MG/L MG/L MG/L MG/L FACT INPUT REAIR C-BOD SOD P-R NH3-N NO2-N 1 1 1 78.80 8.11 7.19 0.92 0.00 0.99 531.19 2.76 -2.40 0.00 0.00 -0.66 -0.01 2 1 2 78.80 8.11 6.40 1.71 0.00 0.98 257.53 5.12 -13.28 0.00 0.00 -1.99 -0.01 3 1 3 78.80 8.11 6.28 1.84 0.00 0.98 0.45 5.51 -13.13 0.00 0.00 -1.98 -0.03 4 1 4 78.80 8.11 6.15 1.96 0.00 0.98 0.45 5.88 -12.98 0.00 0.00 -1.96 -0.04 5 1 5 78.80 8.11 6.04 2.08 0.00 0.97 0.45 6.22 -12.83 0.00 0.00 -1.94 -0.06 6 1 6 78.80 8.11 5.93 2.19 0,00 0.97 0.45 6.55 -12.69 0.00 0.00 -1, 93 -0.07 7 1 7 78.80 8.11 5.83 2.29 0.00 0.97 0.45 6.86 -12.54 0.00 0.00 -1.91 -0.08 8 1 8 78.80 8.11 5.73 2.39 0.00 0.97 0.45 7.15 -12.40 0.00 0.00 -1.90 -0.10 9 1 9 78.80 8.11 5.64 2,48 0.00 0.97 0.45 7.42 -12.26 0.00 0.00 -1,88 -0,11 10 1 10 78.80 8.11 5.55 2.56 0.00 0.96 0.45 7.68 -12.13 0.00 0.00 -1.87 -0.12 11 1 11 78.80 8.11 5.47 2.64 0.00 0.96 0.45 7.92 -11.99 0,00 0.00 -1.85 -0.13 12 1 12 78.80 8.11 5.40 2.72 0.00 0.96 0.45 8.15 -11.85 0.00 0.00 -1.84 -0.15 13 1 13 78.80 8.11 5.32 2.79 0.00 0.96 0.45 8.36 -11.72 0.00 0.00 -1.82 -0,16 14 1 14 78.80 8.11 5.26 2.86 0.00 0.96 0.45 8.56 -11.59 0.00 0.00 -1.81 -0.17 15 1 15 78.80 8.11 5.20 2.92 0.00 0.96 0.45 8.74 -11.46 0.00 0.00 -1.79 -0.18 16 1 16 78.80 8.11 5.14 2.97 0.00 0.95 0.45 8.92 -11, 33 0.00 0.00 -1.78 -0.19 17 1 17 78.80 8.11 5.09 3.03 0.00 0.95 0.45 9.08 -11.20 0.00 0.00 -1.77 -0.20 18 1 18 78.80 8.11 5.04 3.08 0.00 0.95 0.45 9.23 -11.08 0.00 0.00 -1.75 -0.21 19 1 19 78.80 8.11 4.99 3.12 0.00 0.95 0.45 9.36 -10.95 0.00 0.00 -1.74 -0.22 20 2 1 78.80 8,11 5.04 3.08 0.00 0.95 0.50 12.59 -7.24 0.00 0.00 -1.73 -0.23 21 2 2 78.80 8.11 5.13 2.99 0.00 0.95 0.50 15.50 -7.19 0.00 0.00 -1.72 -0.24 22 2 3 78.80 8.11 5.21 2.90 0.00 0.96 0.50 15.07 -7.13 0.00 0.00 -1.72 -0.25 23 2 4 78.80 8.11 5.29 2.83 0.00 0.96 0.50 14.67 -7.08 0.00 0.00 -1.71 -0.25 24 2 5 78.80 8.11 5.36 2.75 0.00 0.96 0.50 14.29 -7.02 0.00 0.00 -1.70 -0.26 25 2 6 78.80 8.11 5.43 2.68 0.00 0.96 0.50 13.93 -6.97 0.00 0.00 -1.70 -0.27 26 2 7 78.80 8.11 5.49 2.62 0.00 0.96 0.50 13.59 -6.91 0.00 0.00 -1.69 -0.28 27 2 8 78.80 8.11 5.56 2.56 0.00 0.96 0.50 13.27 -6.86 0.00 0.00 -1.68 -0.29 28 2 9 78.80 8.11 5.61 2.50 0.00 0.97 0,50 12.96 -6.80 0.00 0.00 -1.67 -0.30 29 2 10 78.80 8.11 5.67 2.44 0.00 0.97 0.50 12.68 -6.75 0.00 0.00 -1.66 -0.31 OUTPUT PAGE NUMBER 14 ***** STEADY STATE SIMULATION ***** EPA/iv'CASI VERSION' ** DISSOLVED OXYGEN DATA ** ELE RCN ELE DO DOCOMPONENTS OF DISSOLVED OXYGEN '"ASS BALANCE (MG/L-DAY) ORD NUM NUM TEMP SAT DO .1DAM NIT DEG-F MS/L M /L D- INPUT INHIB F-FNCTN OXYGN G MG/L MG/L FACT INPUT REAIR C-BOD NET SOD P-R NH3-N NO2-iN STREAM 0U LITY SIMULATION OVAL-2E STREAM 6:UALITY ROUTING MODEL 30 2 11 78,80 r 3i 8, 11 5, 72 2. 39 0. Cif) 12 78, 8ci 8, II 5, 77 2: 34 0. 00 U. 97 O. 50 12. 41 -6. 70 O0032 2 13 Ifs. 80 8, 11 5O. 00 0 000 -ia b655 -O, 31 . 82 2, 3) O. i 0 0 50 12.15 _6.65 0, 00 0. 00 -1.65 -0. 32 i1. 1 6.59 O.00 O.00 -1,84 -0,33 45 4 2 44 4 1 78.80 8.11 6.37 1,74 0.00 0.98 45 4 3 78.80 88. 11 6.37 1.74 0. 00 0.98 47 4 6.38 I.74 0.00 0.98 48 4 4 78.80 8.11 6.38 1.73 0.00 0. 98 5 78. 49 4 6 78.8f 8. 11 6.39 1.72 0. 00 0.98 50 4 7 78.80 8.11 6. 40 1.71 O. 00 O. 98 51 4 8 78.80 8.11 6.41 1.71 0. 00 0.98 52 4 9 78.8t) 1.7I O. t)tj O. 98 53 8.11 6.41 1.70 0. 00 0. 98 4 10 78.80 8.11 6.42 1.69 0. 00 0.98 54 4 11 78.80 8. 11 6, 43 1.69 0. 00 0.98 55 4 12 78.80 8.11 6.43 1.68 0.00 0.98 56 4 13 78.80 8.11 6.44 1.67 0.00 0.98 33 3 1 78. 80 2, 24 O. 00 0, 34 •J L 78. 80 8,11 94 0 97 0. 29 12. 53 -6. 54 0, 00 O. 00 - z 35 J L,18 ()a C)u O. 97 0.' 1 r - C 1. J,3 -tJ, .34 J 78. 8i) 8.11 6. 00 2.12 O. 00 O. 37 29 { 3, )5 -6. 50 O. 00 O. 00 -1. 62 -0, 34 36 4 78. 80 8.11 6,05 O. 29 70 -6, 45 0,00 O. 00 61 35 :,7 5 78.80 2. 06 O. 00 0, 97 O. 29 12. 37 -6, 40 O. 00 0, 00 -1, 60 -0, 36 8.ti 6.1U e.u1 U,OO 38 3 6 78, 80 11 0. 997 O. 29 12, 06 -6, 35 0, 00 0, 00 -I. 60 -O. 36 8.6a 15 1. 96 O. 00 0, 98 O. 29 11. 77 6, 30 0, t)Ci O. 0) 39 3 7 78. BO 8. 11 6, 19 1, 92 O. (xi 0, 98 c 40 3 8 78.80 0.29 11.50 0 -1.59 -tj, ,37 41 3 8,11 6. 24 i.88 O. 0(i O. 9 O. 23 11. 25 _6 Li O. I)I) O. GO -1. `�8 -0. 37 9 78. 80 8,11 6. 28 I a 84 O. Ot) O. 9g 6, 21 O. 00 O. 00 -1, 57 -O. 38O. 42 3 10 78.80 8.11 6. 31 1.80 00 O. 98 O. 29 11, 01 -6,16 O. 00 O. 00 -1, 56 -0, 39 43 3 11 78. 80 8. 11 6, 35 1. 76 0, 00 O. 99 ) 0. B 6`9 10. 79 -6. 12 0, t i O. 29 10. 5 - O. 00 -1. 55 -0, 39 . E )7 Or 00 0, 00 -1. 54 -O. 40 0.14 0.14 0. 14 0.14 0.14 O. 14 0.14 0.14 0.14 0.14 0.14 0,14 0.14 9.36 8.23 8.21 B.18 8.16 8.13 8.10 8.07 8.04 8.01 7.98 7.95 7.91 -6.03 -5. 98 -5,94 - 5.85 -5.81 - 5, 77 -5.73 - 5.68 -5, 64 - 5, 60 -5. 56 5.52 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 O. 00 0. 00 0, 00 0.00 0, 00 0,00 00 0, 00 0,1)0 O. 00 0. 00 0. 00 0.00 -1.54 - 1.53 -1.52 - 1.51 - 1.50 - 1.49 -1.48 - 1, 48 - 1, 47 -1, 46 -1.45 -1.44 -1.43 -O. 40 -(i. 41 -O. 41 -0. 42 -0, 42- -O. 43 - O. 43 - 0.43 - 0.44 -0.44 -O. 44 -O. 45 -0.45 STREAM QUALITY SIMULATION OUTPUT PAGE NUMBER 15 G��-2E STREAM QUALITY ROUTING MODEL EPA/NCASI VERSION ***** STEADY STATE SIMULATION ***** ** DISSOLVED OXYGEN DATE x * COMPONENTS OF DISSOLVED OXYGEN MASS BALANCE (MG/L-DAY) ELE RCH ELE DO DO DAM NIT ORD NUM NLM TEMP SAT D0 DEF INPUT INHIB F-FNCTN OXYGN NET DEG-F M6/L MG/L MG/L MG/L FACT INPUT REAIR C-801) SOD P-R NH3-N NO2-N 57 4 14 78.80 8. 11 6.45 1.67 0.00 0.98 0. 14 7,88 -5.48 0.00 0.00 -1.42 -0.46 58 5 78.80 8.11 6.44 1.67 0,00 0.98 0.21 6.76 -5.44 0,00 0.00 -1.42 -0,46 59 5 78.80 8,11 6.42 1,70 0.00 0.98 0.21 3.67 -5. 40 0.00 0,00 -1, 41 -0.46 60 5 78.80 8,11 6.40 1.72 0,00 0.98 0.21 5.74 -5,36 0,00 0.00 -1.40 -0.46 61 5 4 78.80 8.11 6.38 1.73 0.00 0.98 O. 21 5.80 -5. 32 O. 00 O. 00 -1, 39 -O. 47 62 5 5 78.80 8,11 6.36 1.75 0.00 0.98 0.21 5.85 -5.28 0.00 0.00 -1. 38 -0.47 b3 5 6 78.80 8,11 6.35 1.77 0.00 0.98 0.21 5.91 -5.24 0.00 0.00 -1.37 -0.47 64 5 7 78.80 6.11 6,33 1.78 0.00 0.98 0.21 5.95 -5.20 0.00 0.00 -1.37 -0, 47 65 5 8 78.80 8.11 6. 32 1,73 0.00 0.98 0.21 6.00 -5.17 0.00 0.00 -1.36 -0.48 66 5 9 78,80 8.11 6.31 1.81 0,00 0.98 0.21 6.04 -5.13 0,00 0.00 -1.35 -0.48 67 5 10 78.80 8.11 6.30 1.82 0.00 0.98 0.21 6.08 -5.09 0.00 0.00 -1.34 -0,48 68 5 11 78.80 8.11 6.29 1.83 0.00 0.98 0.21 6.11 -5.05 0.0) 0.00 -1.33 -0.48 69 5 12 78.80 8.11 6.28 1.84 0.00 0.98 0.21 6.14 -5. 02 0.00 0.00 -1. 32 -0.48 70 5 13 78.80 8.11 6.27 1.84 0,00 0.98 0.21 6.17 -4.38 0.00 0.00 -1.32 -0.49 71 5 14 78.80 8,11 6.26 1.85 0,00 0,98 0.21 6.19 -4. 94 0.00 0,00 -1. 31 -0.49 72 5 15 78.80 8.11 6.26 1.86 0.00 0.98 0.21 6.21 -4.91 0.0)) 0.00 -1,30 -0.49 73 5 16 78.80 8.11 6.25 1.86 0.00 0.38 0.21 6.23 -4.87 0.00 0.00 -1, 29 -0.43 74 5 17 78.80 8.11 6.25 1.87 0.00 0,98 0.21 6.24 -4.83 0.00 0.00 -1.29 -0.49 75 5 18 78.80 8.11 6.24 1.87 0.00 0.98 0.21 6,26 -4.80 0.00 0.00 -1, c8 -0.49 76 5 19 78.80 8,11 6,30 1.82 0.00 0.98 32,13 6.017 -4.58 0.00 0.00 -1.26 -0.47 77 5 20 78.80 8.11 6.29 1.82 0.00 0.98 0.19 6.08 -4.55 0.00 0.00 -1.26 -0.47 78 6 1 78.80 8.11 6.30 1.82 0.00 0.98 0.46 6.38 -4,51 0.00 0.00 -1.25 -0.47 79 6 2 78.80 8.11 6.31 1.81 0.00 0.98 0.46 6.67 -4.48 0.00 0.00 -1. 224 -0.47 80 6 3 78.80 8.11 6.31 1.80 0.00 0.98 0.46 6.64 -4.44 0.00 0.00 -1.24 -0.47 81 6 4 78.80 8.11 6.32 1.79 0.00 0.98 0.46 6.62 -4.41 0.00 0.00 -1.23 -0.47 82 6 5 78.80 8.11 6.33 1.79 0.00 0.98 0.46 6,59 -4.37 0.00 0.00 -1.22 -0.47 83 .6 6 78.80 8.11 6.34 1.78 0.00 0.98 0.46 6.56 -4.34 0.00 0.00 -1.21 -0.47 STREAM QUALITY SIMULATION OUTPUT PAGE NUMBER 16 DUAL-2E STREAM QUALITY ROUTING MODEL EPA/NCASI ERSION ***** STEADY STATE SIMULATION ***** ** DISSOLVED OXYGEN DATA ** COMPONENTS OF DISSOLVED OXYGEN MASS BALANCE (MG/L-DAY) ELE RCH ELE DO DO DAM NIT ORD NUM NUM TEMP SAT DC DEF INPUT INHIB F-FNCTN OXYGN NET DEG-F MG/L MG/L MG/1 MG/L FACT INPUT REAIR C- BIID SOD P-R NH.3-N N0 N 84 6 7 78.80 8.11 6.34 1.77 0.00 0.98 0.46 6.53 -4.31 0.00 0.00 -1.21 -0.48 85 6 8 78.80 8.11 6.35 1.76 0.00 0.98 0,46 8.50 -4. 28 0.00 0.00 -1.20 -0.48 86 6 3 78.80 8.11 6.36 1,75 0.00 0.98 0.48 5.47 -4. 24 0.00 0.0 -1.13 -0.48 97 6 i0 78.90 8.11 8.37 1.74 0.00 0.38 0.46 6.44 -4.21 0.00 0.00 -1.19 -0.48 88 6 11 78.80 8.11 6.38 1.74 0.00 0.98 0.46 6.41 -4. 18 0.00 0.00 -1.18 -0.48 89 6 12 78.80 8.11 6.39 1,73 0.00 0.98 0.46 6,37 -4,15 0,00 0.00 -1.17 -0.48 90 6 13 78.80 8.11 6.39 1,72 0.00 0.98 0,46 6.34 -4. 12 0.00 0.00 -1. 17 -'). 48 91 6 14 78,80 8.11 6.40 1.71 0,00 0,98 0.46 6.31 -4.08 0.00 0.00 -1.16 -0,48 92 6 15 78.80 8.11 6.41 1.70 0.00 0.38 0.46 6.28 -4.05 0.00 0.00 -1.15 -0.48 93 6 16 79.80 8.11 6,42 1,63 0.00 0,98 0.48 6,25 -4. 0c 0.00 0.00 -1.15 -0.48 94 6 17 78.80 8.11 6.43 1.68 0.00 0.98 0.46 6,21 -3. 93 0,00 0.00 -1.14 -0.48 95 6 18 78.80 8.11 6.44 1.68 0.00 0.98 0.46 6.19 -3.36 0.00 0.00 -1.13 -0.48 .+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++� �+ + �+ + + +� + + + + + + 4. + + + + +� + + C. + 4- J CO+t++ +O[J -- + ++++ _.I + +dam -I- + V (D C. -++++ +�C] M + + + + + c:cM + rk + M Z' +* * :•k :!r * * ,}c * * at. * * * * * 'k * * `k 4. * * * ,k rk �k •k �M .k �i 7E L•J �4++++ %k * ** * * +4 + * :k ak .I. * * 'k �k + + + + `. C C. + * :{ y ++ * ,i* * + m Z x + .4.* * * .I. .fc ,k * * * + W CD If] + + + + * * ,k + t • * 4 + '}' C1.1 * x r,J + {S o ... > ++++ + II Jet+. ++++"J U7 C + + U :f) -+ + + + r`7 + . .--. 4.+ 4 + + Q -I- C.. + + 4- + + + + + . + 411 414 44-1 + + + + + + ++++if) 1. + + + + + + + + •..^ + + + + + + + + + + + In + + + + + + t + + + + + + + t + . InIf)an If) If) tf) 1.17 tf ) .., 0 m Li-3 - r`] ,l) .--• li7 LU tr z .-, J W DISSOLVED OXYGEN BIOCHEMICAL OXYGEN DEMAND = SCDHEC CHLORINE LIMIT CO{PUTATION FOR CLASS A A -TROUT B, AND B-TROUT WATERS OF THE STATE OF SOUTH CAROLINA. NAME OF DISCHARGER? PROPOSED NORTH CAROLINA DISCHARGE NAME OF STREAM? TO CROWDERS CREEK JUST ABOVE BORDER DATE OF ASSESSMENT? 3/3/88 NAME OF MODELLER? BORDERS PLEASE ENTER THE DISCHARGER FLOW IN MGD? 6.0 PLEASE ENTER THE BACKGROUND (STREAM) FLOW IN CFS? 6.71 PLEASE ENTER THE BACKGROUND CHLORIN CONCENTRATION IN uG/L? 0 THE MONTHLY AVERAGE CHLORINE CONCENTRATION IN THE DISCHARGE NOT TO EXCEED A MIXED INSTRE.AM TOTAL RESIDUAL CHLORINE CONCENTRATION OF 11.0 uG/L IS ----) 19.0 uG/L THE DAILY MAXIMUM TRC LIMIT IN THE EFFLUENT NOT TO EXCEED A MIXED INSTREAM TOTAL RESIDUAL CHLORINE CONCENTRATION OF 19.0 uGIL IS ----) 22,7 uG/L ANY FURTHER CALCULATIONS? (YIN) SOUTH CAROLINA AMMONIA TOXICITY TEST NAME OF DISCHARGER? PROPOSED NORTH CAROLINA DISCHARGE NAME OF STREAM? TO CROWDERS CREEK JUST ABOVE BORDER DATE OF ASSESSMENT? 3/3/88 NAME OF MODELLER? BORDERS TEMPERATURE, IN DEGREES CENTIGRADE? 26 WHAT pH? 7 THE Cwqs VALUE IS ---) 8.39 PLEASE ENTER BACKGROUND AMMONIA CONCENTRATION (Cu) IN MG/_? .44 PLEASE ENTER DISCHARGER FLOW 03d) IN MGD? 6 PLEASE ENTER BACKGROUND FLOW (Qu) IN CFS? 6.71 THE MAXIMUM ALLOWABLE AMMONIA CONCENTRATION IN THE DISCHARGE IS ===)) 13.9 MG/L ANY FURTHER CALCULATIONS (Y!N) APPENDIX D Sample Calculation for Determining Cadmium Limit Facility Ow * Daily Max. = Load Balance (mgd) (mg/1) Carolina & Southern 0.257 0 0 Precision Seals 0.146 0.028 0.004 Lithium Corp. 0'615 0 0 Homelite-Textron 0.400 * 0.00084 A.B. Carter 0.022 0.11 0.0024 Rauch Industries 0.012 0 0 _______ Total Industrial Ow 1.454 0.00724 + + Total Domestic Ow 4.546 0.003** 0.0136 ______ _______ Total Ow 6.000 0.02084 Domestic Ow = Total Ow - Ind. Ow = 6.0 - 1.454 =4.546 mgd Actual Cw = Total load balance / Total Ow = 0.02084 / 6.0 mgd Actual Cw = 0.0035 m~/ Allowable Cw= Qd*Cd - Qu*Cu / Ow Cw = Waste Concentration Qd = Downstream flow = 7q10 flow + Ow Qd = 6.7 cfs + 9.3 cfs = 16 cfs Cd = Downstream Concentration (WQ Standard) Cd = 2 ug/l or .002 mg/l Qu = Upstream 7q10 flow = 6.7 cfs Cu = Upstream Concentration Ow = Wasteflow in cfs Qw = 6.0 mgd * 1.55 = 9.3 cfs Allowable Cw - 16 cfs*.002 mg/l - 6.7 cfs*0 / 9.3 cfs = 0.032 cfs*mg/l - 0 / 9'3 cfs Allowable Cw = 0.0034 mg/l Limit,if Actual 1/10 Allowable Cw 0.0035 mg/l ` 0.00034 mg/l Therefore must limit for Cadmium, using the Allowable Cw * Homelite daily max. value already converted to load. conc. ** Default Industrial Effluent Concentration for Domestic/ Commercial Facilities * i'IODEL SUMMARY DATA **.r Discharger- e CAROLINA rSOHERN Receiving Stream . CROWDERS CREEK Summer 010 6.4 Design Temperature: 23. Subbi-:tsi n 030837 Stream Class: C Winter 7G310 ;LENGTH; SLOPEI VELOCITY ; DEPTHI Kd ; Kd Ka 1 Ka ; Kl: ; K1# KNR ; KNR 1 mile 1 ftimi; fps 1 ft ;design; a2G' ;design; 320' ;design; 320' ;design; a20' Segment 1 1 2.101 55.001 0.118 ; 0.47 ; 0.84 1 0.73 ;12.45 1 11.671 0.63 1 0.50 1 0.38 1 0.30 1 Reach 1 1 ' 1 , , 1 Segment 1 1 0.501 34.00; 0.135 1 0.71 ; 0.43 1 0.33 1 8.79 : 8.241 0.63 1 0.50 1 0.38 1 0.30 1 Reach 2 . 1 1 Segment 1 1 1.501 34.001 0.143 1 0.75 1 0.44 1 0.39 1 9.35 1 8.761 0.63 1 0.50 1 0.38 1 0.30 ; Reach 3 1 1 1 1 1 1 1 Segment 2 1 1.301 70.001 0.625 1 0.51 1 0.98 1 0.85 153.37 1 50.001 0.63 1 0.50 1 0.38 1 0.30 1 Reach 1 1 i , , 1 , ; , i Segment 2 ; 0.601 28.001 0.338 1 0.80 1 0.48 1 0.42 '18.20 1 17.051 0.63 1 0.50 1 0.38 1 0.30 1 Reach 2 1 1 ' Segment 3 1 1.001 13.001 0.243 1 1.13 1 0.33 1 0.29 1 6,07 1 5.691 0.38 1 0.30 1 0.38 1 0.30 1 Reach 1 1 Segment 3 ; 3.20: 6.001 0.192 1 1.30 1 0.27 1 0.24 1 2.21 1 2.07; 0.38 1 0.30 1 0.38 1 0.30 1 Reach , 1 Segmer,t 3 1 0.901 6.001 0.192 1 1.31 1 0.27 1 0.24 ; 2.21 1 2.07; 0.38 1 0.30 1 0.38 1 0.30 1 Reach 3 , I , , , Segment 3 1 1.301 6.001 0.192 1 1.34 ; 0.27 1 0.24 1 2.21 1 2.071 0.38 1 0.30 1 0.38 1 0.30 1 Reach 4. 1 1 1 1 Segment 3 1 2.601 6.001 0.196 ; 1.39 1 0.27 1 0.24 1 2.26 1 2.11; 0.38 1 0.30 1 0.38 1 0.30 1 Reach 5 1 n 1 , 1 1 n , 1 0 30 i , 1 Segment 3 0.30: 6.001 O.c4:� 1.630.27 i 0.23 i 2.77 c.60, 0.38 i ....,. 0.380.30 , Reach 6 1 Segment 3 ; 0.601 6.001 0.249 1 1.68 1 0.27 1 0.23 ; 2.07 1 1.94; 0.38 ; 0.30 1 0.38 1 0.30 1 Reach 7 1 1 1 i 1 i . Segment 3 1 1.301 6.001 0.249 1 1.69 ; 0.27 1 0.23 ; 2.07 1 1.94; 0.38 1 0.30 1 0.38 1 0.30 1 Reach 8 ^ SUMMER MODEL FOR 201 PROJECT FOR CROWDERS CREEK BASIN � | Seg # | Reach # | Seg Mi 1 D.O. CBOD NBOD 1 Flow � 1 1 0.00 7.04 2.00 3.00 0.20 1 1 O.10 7'64 1.91 2.94 0.22 ^ 1 1 0.20 7.93 1.84 2.89 0.24 1 1 0.30 8.08 1.77 2.84 0'25 1 1 0.40 8.16 1.71 2.80 0.27 1 1 0.50 8.20 1.65 2.75 0.29 1 1 0.60 8.23 1'60 2.71 0.31 1 1 0.70 8.25 1.56 2.68 0.32 1 1 0.80 8.26 1.51 2.64 0.34 1 1 0.90 8.27 1.47 2.61 0.36 1 1 1.00 8.28 1.43 2.58 0.38 1 1 1.10 8.28 1.39 2.54 0.40 1 1 1.20 8.29 1.36 2.51 0.41 1 1 1.30 8.30 1.33 2.48 0.43 1 1 1.40 8.30 1.30 2.46 0.45 1 1 1.50 8.31 1.27 2.43 0.47 1 1 1.60 8.31 1.24 2.40 0.48 1 1 1.70 8.32 1.21 2.38 0.50 1 1 1.80 8.32 1.19 2.35 0.52 1 1 1.90 8.33 1.16 2.33 0.54 1 1 2.00 8.33 1.14 2.30 0.56 1 1 2'10 8.34 1.11 2.28 0.57 1 2 2.10 7.80 1.48 2.58 0.97 1 2 2.20 7.97 1.46 2.54 0.99 1 2 2.30 8.07 1.44 2.50 1.01 1 2 2.40 8.15 1.42 2.47 1.03 1 2 2.50 8.20 1.40 2.44 1.05 1 2 2.60 8.23 1.38 2.40 1.06 1 3 2.60 8.23 1.38 2.40 1.06 1 3 2.70 8.26 1.37 2.38 1.08 1 3 2.80 8.28 1.35 2.35 1.10 1 3 2.90 8.29 1.34 2.32 1.12 1 3 3.00 8.30 1.32 2.29 1.13 1 3 3.10 8.31 1.31 2.27 1.15 1 3 3.20 8.31 1.29 2.24 1.17 1 3 3.30 8.32 1.28 2.22 1.19 1 3 3.40 8.32 1.27 2.19 1'21 1 3 3'50 8.33 1'25 2.17 1.22 1 3 3.60 8.33 1.24 2.15 1.24 1 3 3.70 8.33 1.23 2.12 1.26 1 3 3.80 8.34 1.22 2.10 1.28 1 3 3.90 8.34 1.20 2.08 1.29 1 3 4'00 8.34 1.19 2.06 1.31 1 3 4.10 8.34 1.18 2.04 1.33 2 1 0'00 5.00 22.50 13.50 2.33 2 1 0.10 6.24 22.13 13.37 2.34 2 1 0.20 6.97 21.77 13.24 2.36 2 1 0.30 7.40 21.42 13.12 2.38 2 1 0.40 7.66 21.07 13.00 2'40 2 1 0.50 7.82 20.73 12.87 2.41 2 1 0.60 7.92 20.40 12'75 2.43 2 1 0.70 7.97 20'07 12.64 2.45 2 1 0.80 8.01 19.76 12.52 2.47 2 1 0.90 8.04 19.44 12.41 2.49 2 1 1.00 8.05 19.13 12.29 2.50 2 1 1.10 8.07 18.83 12.18 2.52 2 1 1,20 8.08 18.54 12.07 2.54 2 1 1.30 8.09 18.25 11.97 2.56 2 2 1.30 7.89 15.35 10.07 3.16 2 2 1.40 7.87 15.14 9.96 3.17 SUMMER MODEL FOR 201 PROJECT FOR CROWDERS CREEK (T=26,7.3) | Seg # | Reach # | Beg Mi 1 D.O. CBOD | NBOD | Flow | 1 1 0.00 7.30 2.00 3'00 0.20 1 1 0.10 7.55 1.90 2.93 0.22 1 1 0.20 7.66 1.82 2.86 0.24 1 1 0.30 7.72 1.74 2.80 0.25 1 1 0.40 7.76 1.67 2.75 0.27 1 1 0.50 7.78 1.61 2.69 0.29 1 1 0.60 7.79 1.55 2.65 0.31 1 1 0.70 7.80 1.50 2.60 0.32 1 1 0.80 7.81 1.45 2.56 0.34 1 1 0.90 7.82 1.41 2.52 0.36 1 1 1.00 7.83 1'36 2.48 0.38 1 1 1.10 7.83 1'33 2.44 0'40 1 1 1.20 7.84 1.29 2.40 0.41 1 1 1.30 7.85 1.25 2.37 0.43 1 1 1.40 7,85 1.22 2.34 0.45 1 1 1.50 7.86 1.19 2.30 0.47 1 1 1.60 7.86 1.16 2.27 0.48 1 1 1.70 7.87 1.13 2.24 0.50 1 1 1.80 7.87 1.10 2.21 0.52 1 1 1.90 7.87 1.08 2.18 0.54 1 1 2.00 7.88 1.05 2.16 0.56 1 1 2.10 7.88 1.03 2.13 0.57 1 2 2.10 7.64 1.43 2.49 0.97 1 2 2.20 7.71 1.41 2.44 0.99 1 2 2.30 7.75 1.39 2.40 1.01 1 2 2.40 7.78 1.37 2.36 1.03 1 2 2.50 7.80 1.35 2.33 1.05 1 2 2.60 7.81 1.33 2.29 1.06 1 2 2'70 7.82 1.31 2.25 1.08 1 2 2.80 7.83 1.29 2.22 1.10 1 2 2.90 7.83 1.28 2.18 1.12 1 2 3.00 7.84 1.26 2.15 1.13 1 2 3.10 7.85 1.24 2.12 1.15 1 P 3.20 7.85 1.23 2.09 1.17 1 2 3.30 7.85 1.21 2.06 1.19 1 2 3.40 7.86 1.20 2.03 1.21 1 2 3.50 7.86 1.18 2'00 1.22 1 2 3.60 7.86 1'17 1.97 1.24 1 3 3.60 7.86 1.17 1.97 1.24 1 3 3.70 7.87 1.16 1.95 1.26 1 3 3.80 7.88 1.15 1.93 1'28 1 3 3.90 7.89 1.13 1.91 1.29 1 3 4.00 7.89 1.12 1.88 1.31 1 3 4.10 7.89 1.11 1.86 1.33 1 3 4.20 7.90 1.10 1.84 1.35 1 3 4.30 7.90 1.09 1.82 1.37 1 3 4.40 7.90 1.08 1.80 1.38 1 3 4.50 7.90 1.07 1.78 1.40 1 3 4.60 7.91 1.06 1.76 1.42 1 3 4.70 7.91 1.05 1.74 1.44 1 3 4.80 7.91 1.04 1.73 1.45 1 3 4.90 7.91 1.03 1.71 1.47 1 3 5'00 7.91 1.02 1.69 1.49 1 3 5.10 7.92 1.01 1.67 1.51 2 1 0.00 5.00 22.50 13'50 2.33 2 1 0.10 6.07 22.10 13.36 2.34 2 1 0.20 6.69 21.71 13.22 2.36 2 1 0.30 7.04 21.33 13.08 2.38 2 0.40 7.24 20.95 12.95 2.40 MODEL FOR 201 PROJECT FOR CROWDERS CREEK (T=260.3) Discharger Receiving Stream ---------- MODEL RESULTS : CAROLINA & SOUTHERN : CROWDERS CREEK The End D.O. is 7.32 mg/l. The End CBOD is 2.23 mg/l. The End NBOD is 1.83 mg/l. WLA WLA WLA DO Min CBOD WBOD DO Waste Flow (Mg/1) Milepoint Reach # (Mg/1) (Mg/1) (mg/1) (mgd} ______ _________ _______ ____ Segment 1 7.30 0.00 1 Reach 1 21'00 22.50 5.00 0.00000 Reach 2 0.00 0.00 0.00 0.00000 Reach 3 45.00 90.00 5.00 0.00000 Segment 2 5.00 0.00 1 Reach 1 22.50 13.50 5.00 1.50000 Reach 2 0.00 0.00 0.00 0.00000 Segment 3 6.36 3.20 2 Reach If. 0.00 0.00 0.00 0.00000 Reach 2 0.00 0.00 0.00 0.00000 Reach 3 0.00 0.00 0.00 0.00000 Reach 4 90.00 63.00 0.00 0.00000 Reach 5 0.00 0.00 0.00 0.00000 � Reach 6 0.00 0.00 0.00 0.00000 Reach 7 0.00 0.00 0.00 0'00000 Reach 8 287.00 354.00 0.00 0.00000 Reach 9 0.00 0.00 0.00 0.00000 ' . ^ ` Sepent 3 | 5.00| 6.00: 0.257 | 1.76 | 0.31 | 0.23 | 2.28 1 2.00: 0.48 | 0.30 | 0.48 | 0.30 � ^ Reach Y ' t | Flow � cfs Segment 1 Reach 1 Waste . 0.000 Headwaters! 0.200 Tributary | 0.000 * Runoff 1 0.178 Segment 1 Reach 2 Waste , Tributary | * Runoff | Segment 1 Waste Tributary * Runoff ' | CBOD 1 NBOD ! D.O. | mg/l 1 mg/l | mg/l 0.000 < 0.400 1 0.178 | 21.000 2.000 0.000 2.000 0.000 2.000 2.000 22.500 3.000 0,000 3.000 1 0.000 | | 3.000 1 1 3.000 | Reach 3 1 0'000 1 45.000 1 90.000 1 | 0.000 | 0.000 | 0.000 | 1 0.178 1 2.000 1 3.000 1 Segment 2 Reach 1 Waste | Headwaters! Tributary | * Runoff | 2.325 0.000 0.000 0.178 Segment 2 Reach 2 Waste 1 0.000 1 Tributary 1 0.600 | * Runoff 1 0.178 | Segment 3 Reach 1 Waste 1 0.000 1 Headwaters! 0.000 | Tributary 1 0.000 | * Runoff | 0.178 | Segment 3 Reach 2 Waste | 0.000 | Tributary | 0.100 | * Runoff | 0.000 | Segment 3 Reach 3 Waste | 0.000 | Tributary | 0.000 | * Runoff | 0.178 | 22.500 0.000 0.000 2.000 0.000 | 3.000 | 2.000 | 13.500 0.000 0.000 3.000 0.000 | 2.000 1 3.000 | 5.000 7.300 7.300 7.300 0.000 7.300 7.300 5.000 7.300 7.300 5.000 7.300 7.300 0.000 7.300 7.300 0.000 | 0.000 | 0.000 0.000 | 0.000 1 /.300 0.000 1 0.000 1 7.300 2.000 | 3.000 | 7.300 0.000 1 2.000 i 0.000 | 0.000 1 0.000 | 2.000 | 0.000 1 0.000 3.000 1 7.300 0.000 1 7.300 0.000 | 0.000 1 3'000 1 0.000 7.300 7.300 Segment 3 Reach 4 Waste | 0.000 | 90.000 | 63.000 Tributary | 0.0}0 1 0.000 1 0.000 | 0.000 | 7.300 2 1 0.50 7.36 20.59 12.81 2.41 2 1 0.60 7.44 20.23 12.68 2.43 2 1 0'70 7.48 19.88 12.55 2.45 2 1 0.80 7.51 19.53 12.43 2.47 2 1 0.90 7.53 19.20 12.30 2.49 2 1 1.00 7.55 18.87 12.18 2.50 2 1 1.10 7.56 18.54 12.06 2.52 2 1 1.20 7.57 18.23 11.94 2.54 2 1 1.30 7.58 17.92 11.82 2.56 2 2 1.30 7.52 15.08 9.95 3.16 2 2 1.40 7.45 14.86 9.83 3.17 2 2 1.50 7.40 14.64 9.71 3.19 2 2 1.60 7.37 14.42 9.59 3.21 2 2 1.70 7.36 14.21 9.47 3.23 2 2 1.80 7.35 14.01 9.35 3.25 2 2 1.90 7.34 13.80 9.24 3.26 3 1 0.00 7.52 9.76 6.85 4'77 3 1 0.10 7.45 9'64 6.75 4.79 3 1 0.20 7.39 9.52 6.66 4.81 3 1 0.30 7.34 9.40 6.57 4'82 3 1 0'40 7.30 9.28 6.47 4.84 3 1 0.50 7.27 9.17 6.38 4.86 3 1 0.60 7.25 9.06 6.30 4.88 3 1 0.70 7.23 8.94 6'21 4.90 3 1 0.80 7.22 8.83 6.12 4.91 3 1 0.90 7.21 8.73 6.04 4.93 3 1 1.00 7.20 8.62 5.96 4.95 3 2 1.00 7.20 8.49 5.90 5.05 3 2 1.20 7.01 8.32 5.72 5.05 3 2 1.40 6-85 8.16 5.55 5.05 3 2 1.60 6.73 8.00 5.39 5.05 3 2 1.80 6.62 7.84 5.23 5.05 3 2 2.00 6.54 7.68 5.07 5.05 3 2 2.20 6.48 7.53 4.92 5.05 3 2 2.40 6.43 7.39 4.77 5.05 3 2 2.60 6'40 7.24 4.63 5.05 3 2 2.80 6.38 7.10 4.49 5.05 3 2 3.00 6.37 6.96 4'36 5.05 3 2 3.20 6.36 6.82 4.23 5.05 3 2 3.40 6.36 6.69 4.10 5.05 3 2 3.60 6.37 6.55 3.98 5.05 3 2 3.80 6.39 6.43 3.86 5.05 3 2 4.00 6.40 6.30 3.74 5.05 3 2 4'20 6'42 6'17 3'63 5.05 3 3 4.20 6'42 6.17 3.63 5.05 3 3 4.30 6.44 6.10 3.57 5.07 3 3 4.40 6.45 6.02 3.52 5.08 3 3 4.50 6.46 5.95 3.46 5.10 3 3 4.60 6.48 5.88 3.41 5.12 3 3 4.70 6.50 5.81 3.36 5.14 3 3 4.80 6.51 5'74 3.31 5.16 3 3 4.90 6.53 5.67 3'26 5.17 3 3 5.00 6.54 5.60 3'21 5.19 3 3 5.10 6.56 5.53 3.16 5.21 3 4 5.10 6.56 5.53 3.16 5.21 3 4 5.20 6.58 5.47 3.11 5.23 3 4 5.30 6.59 5.40 3.06 5.24 3 4 5.40 6.61 5'33 3.02 5.26 3 4 5.50 6.63 5'27 2.97 5.28 3 4 5.60 6.64 5.21 2.93 5.30 3 4 5.70 6.66 5.15 2.88 5.32 3 4 5.80 6.68 5.08 2.84 5.33 3 4 5.90 6.69 5.02 2.80 5.35 3 4 6.00 6.71 4.96 2.76 5.37 3 4 6.10 6.72 4.91 2.72 5.39 1 6.20 6.74 4.85 2.68 5.41 * Runoff 1 0.178 1 2.000 1 3.000 1 7.300 Segment 3 Reach 5 Waste 1 0.000 1 0.000 | 0.000 | 0.000 Tributary 1 0.200 1 2.000 1 3'000 | 7.300 * Runoff | 0.178 | 2.000 | 3.000 | 7.300 Segment 3 Reach 6 Waste 1 0.000 | 0'000 | 0.000 | 0.000 Tributary 1 3.600 1 2.000 | 3.000 | 7.300 * Runoff | 0.178 | 2'000 | 3.000 | 7.300 Segment 3 Reach 7 Waste 1 0.000 1 0.000 | 0.000 1 0.000 Tributary | 0.850 1 10.500 | 5'000 | 7.300 * Runoff | 0.178 1 2.000 | 3.000 | 7'300 Segment 3 Reach 8 Waste 1 0.000 1287.000 1354.000 1 0.000 Tributary 1 0.000 1 0.000 | 0.000 | 7.300 * Runoff | 0.178 | 2.000 | 3'000 1 7.300 Segment 3 Reach 9 Waste | 0.000 | 0.000 | 0.000 0.000 Tributary | 0.510 1 10.000 | 29.000 7.300 * Runoff 1 0.178 1 2.000 | 3.000 | 7.300 * Runoff flow is in cfs/mile * ** MODEL.. SUMMARY DATA *** • Discharger C ROLi:Ny 1: SOUTHERN Receiving Stream . CR;OWDEF:E3 CREEK Summer 7010 . 6.4 Design Temperature: 26.. Subb i n : 030837 Stream Class: C:: Winter 7010 ;LENGTH: SLOPE; VELOCITY ; DEPTH: Kd ; Kd Ka ; Ka 1 KN 1 KN ; KNR ; KNR : 1 mile 1 ft/mi: fps : ft ;design; ;a20° :design: 20° :design1 i20° :design: P.04 Segment 1 1 2.10: 55.00: 0.118 : 0.47 : 0.96 1 0.73 :13.29 : 11.67: 0.79 : 0.50 : 0.48 : 0.30 1 Reach 1. , 1 1 , , 1 1 , , 1 , : 1 1 1 . , Segment 1 1 1.50: 34.00: 0.139 : 0.73 1 0.50 : 0.38 1 9.69 ; 8.50: 0.79 1 0.50 1 0.48 1 0.30 1 Reach 2 1 1 1 : ; ; ; 1 Segment 1 1 1,50: 34.00; 0.151 : 0.78 ; 0.51 1 0.39 :10.52 1 9.23: 0.79 : 0.50 1 0.48 1 0.30 Reach 3 1 Segment 2 1 1.30: 70.00: 0.625 1 0.51 : 1.12 1 0.85 156.97 : 50.001 0.79 1 0.50 ; 0.48 1 0.30 : Reach 1 1 1 1 1 1 1 1 1 1 1 Segment 2 ; 0.60: 28.00: 0.338 1 0.80 1 0.55 ; 0.42 119.43 1 17.05: 0.79 1 0.50 1 0.48 1 0.30 1 Reach 2 1 , 1 1 1 1 1 Segment 3 1 1.001 13.00: 0.243 1 1.15 1 0.38 1 0.29 1 6.48 1 5.681 0.46 1 0.30 1 0.48 1 0.30 : Reach 1 : 1 : : : Segment 3 1 3.20: 6.00: 0.192 : 1.32 1 0.31 ; 0.24 1 2.36 ; 2.07: 0.48 1 0.30 1 0.48 1 0.30 : Reach 2 11 1 1 1 1 1 1 Segment 3 1 0.90; 6.00; 0.192 1 1.33 1 0.31 : 0.24 1 2.36 1 2.07: 0.48 : 0.30 1 0.48 ; 0.30 : Reach 3 1 1 1 1 1 1 1 Segment 3 : 1.301 6.00: 0.193 ' 1.36 1 0.31 1 0.24 1 2.37 1 2.08: 0.48 1 0.30 1 0.48 1 0.30 : Reach 4 1 Segment 3 1 2.60: 6.00: 0.196 1 1.41 1 0.31 1 0.24 1 2.42 1 2.121 0.48 : 0.30 1 0.48 1 0.30 1 Reach .1 1 1 i • 1 1 I 1 . , 1 , 1 . 1 1 , Segment 3 1 0.30: 6.00: 0.241 1 1.64 1 0.31 : 0.23 1 2.96 : 2.60: 0.48 1 0.30 ; 0.48 1 0.30 1 Reach 6 1 : : 1 ; : Segment 3 1 0.60: 6.00: 0.249 1 1.69 1 0.31 1 0.23 1 2.21 1 1.941 0.43 1 0.30 1 0.48 1 0.30 : Reach 7 1 1 1 1 , 1 Segment 3 1 1.30: 6.00: 0.250 : 1.70 ; 0.31 ; 0.23 1 2.22 1 1.951 0.48 1 0.30 1 0.48 1 0.30 1 Se0men 3 : 5.M 6.00| 0.256 | 105 : 0.27 | 0.23 | 2.13 1 2.00| 0.38 | 0.30 | 0.30 | 0.30 � Reach Y | < | Flow CBOD | NBOD D.O. 1 cfs mg/l ( mg/l mg/l Segment 1 Reach 1 Waste 1 0.000 | 21.000 | 22.500 1 5.000 Headwaters! 0.200 | 2.000 | 3.000 1 7.040 Tributary | 0.000 | 0.000 | 0.000 1 0.000 * Runoff | 0.178 | 2.000 | 3.000 | 7.040 Segment 1 Reach 2 Waste 0.000 j 0.000 | 0'000 } 0.000 Tributary | 0.400 1 2.000 3.000 | 7.040 * Runoff | 0.178 1 2.000 | 3.000 | 7.040 Segment 1 Reach 3 Waste | 0.000 } 45.000 | 90.000 | 5.000 Tributary 1 0.000 1 0.000 | 0.000 1 0.000 * Runoff | 0.178 | 2.000 1 3.000 1 7.040 Segment 2 Reach 1 Waste | 2.325 | 22.500 1 13.500 < 5.000 Headwaters; 0.000 ( 0.000 | 0.000 | 7.040 Tributary 1 0.000 | 0.000 1 0.000 | 0.000 * Runoff | 0.178 1 2.000 < 3.000 | 7.720 Segment 2 Reach 2 Waste 1 0.000 1 0.000 1 0.000 | 0.000 Tributary | 0.600 | 3.000 | 2.000 | 7.040 * Runoff | 0.178 | 2.000 1 3.000 | 7.040 Segment 3 Reach 1 Waste 1 0.000 | 0.000 | 0.000 0.000 Headwaters; 0.000 1 0.000 | 0.000 | 7.040 Tributary 1 0.000 | 0.000 | 0.000 | 0.000 * Runoff 0.178 | 2.000 | 3.000 1 7.040 Segment 3 Reach 2 Waste 1 0.000 1 0.000 1 0.000 1 0'000 Tributary 1 0.100 1 2.000 | 3.000 1 7.040 * Runoff I 0.000 | 0.000 | 0.000 1 7.040 Segment 3 Reach 3 Waste 1 0.000 | 0.000 | 0.000 1 0,000 Tributary | 0.000 | 0.000 | 0.000 | 0.000 * Runoff ! 0.178 | 2.000 | 3.000 } 7.040 Segment 3 Reach 4 Waste 1 0.000 1 90.000 1 63.000 1 0.000 Tributary | 0.000 | 0.000 | 0.000 1 0.000 * Runoff 0.178 1 2.000 1 3.000 1 7.040 2 p 1.50 7.86 14.94 9.86 2 2 1.60 7.85 14.74 9.75 ^ 2 2 1.70 7.85 14.54 9.65 2 2 1.80 7.85 14.34 9.55 2 2 1.90 7.85 14.15 9.45 3 1 0.00 8.00 10.40 7.30 3 1 0.10 7.93 10.28 7.22 3 1 0.20 7.88 10.16 7.13 3 1 0'30 7.84 10.05 7.05 3 1 0.40 7.80 9.93 6.97 3 1 0.50 7.77 9.82 6.89 3 1 0.60 7.75 9.71 6.81 3 1 0.70 7.73 9.60 6.73 3 1 0.80 7'72 9.49 6.65 3 1 0.90 7.70 9.39 6'57 3 1 1.00 7.70 9.28 6.50 3 2 1.00 7.68 9.13 6.43 3 2 1.20 7.51 8.98 6.27 3 2 1.40 7.37 8.82 6.12 3 2 1.60 7.25 8.67 5.98 3 2 1.80 7.15 8.52 5.84 3 2 2.00 7.07 8.37 5.70 3 2 2.20 7.01 8.23 5.56 3 2 2.40 6.96 8.09 5.43 3 2 2.60 6.92 7.95 5.30 3 2 2.80 6.90 7.81 5.17 3 2 3.00 6.88 7.68 5.05 3 2 3.20 6.87 7.55 4.93 3 2 3.40 6.86 7'42 4.81 3 2 3.60 6.86 7.29 4.70 3 2 3.80 6.87 7.16 4.59 3 2 4.00 6.87 7.04 4.48 3 2 4.20 6.89 6.92 4.37 3 3 4.20 6.89 6.92 4.37 3 3 4'30 6.89 6.84 4.31 3 3 4.40 6.90 6.76 4.26 3 3 4.50 6.91 6.69 4.20 3 3 4.60 6.92 6.61 4.15 3 3 4.70 6.93 6.54 4.09 3 3 4.80 6.94 6.47 4.04 3 3 4.90 6.95 6.40 3.99 3 3 5.00 6.97 6'33 3.94 3 3 5.10 6.98 6.26 3.89 3 4 5'10 6.98 6.26 3.89 3 4 5.20 6.99 6.19 3.84 3 4 5.30 7.00 6.12 3.79 3 4 5'40 7.01 6.05 3.74 3 4 5.50 7.03 5.99 3.69 3 4 5.60 7.04 5'92 3.65 3 4 5.70 7.05 5.86 3.60 3 4 5.80 7.07 5.79 3.56 3 4 5.90 7.08 5.73 3.51 3 4 6.00 7.09 5.67 3.47 3 4 6.10 7.11 5.60 3.42 3 4 6.20 7.12 5.54 3.38 3 4 6.30 7.14 5.48 3.34 3 4 6.40 7.15 5.43 3.30 3 5 6.40 7.15 5.30 3.29 3 5 6.60 7.1S 5'19 3.21 3 5 6.80 7.21 5.08 3.13 3 5 7'00 7.24 4.98 3.06 3 5 7.20 7.27 4.87 2.99 3 5 7.40 7.30 4.77 2.92 3 5 7.60 7.33 4.68 2.85 3 5 7.80 7.36 4.58 2.79 3 5 8.00 7.38 4.49 2.72 3.15, 3.21 3.23 3.25 3'26 4.59 4.61 4.63 4.65 4.66 4.68 4.70 4.72 4.74 4.75 4.77 4'87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.87 4.89 4.91 4.92 4.94 4.96 4.98 5.00 5.O1 5.03 5.03 5.05 5.07 5.08 5.10 5.12 5.14 5.16 5.17 5.19 5'21 5.23 5.24 5.26 5'46 5.50 5.53 5'57 5.61 5.64 5.68 5.71 5.75 Segment 3 Reach 5 Waste | 0.000 1 0.000 1 0.000 | 0.000 Tributary 0.200 | 2.000 | 3.000 | 7.040 * Runoff | 0.178 1 2.000 | 3.000 | 7.040 Segment 3 Reach 6 Waste 1 0.000 0.000 1 0.000 1 0.000 Tributary | 3.600 | 2.000 1 3.000 | 7.040 * Runoff 1 0.178 | 2.000 1 3.000 | 7.040 Segment 3 Reach 7 Waste | 0.000 | 0.000 1 0.000 | 0.000 Tributary | 0.850 | 10.500 1 5.000 | 7.040 * Runoff | 0.178 1 2.000 1 3.000 1 7.040 Segment 3 Reach 8 Waste 1 0.000 1287.000 1354.000 1 0.000 Tributary | 0.000 | 0.000 1 0.000 | 7.040 * Runoff | 0.178 | 2.000 | 3.000 | 7.040 Segment 3 Reach 9 ° Waste | 0.000 | 0.000 | 0.000 1 0.000 Tributary | 0.510 | 10.000 1 29.000 1 7.040 * Runoff | 0'178 | 2.000 | 3.000 | 7.040 * Runoff flow is in cfs/mile 3 , 3 . 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 tSag #| = � 9 9 9 9 9 9 9 9 9 9 9 9 9 9 Reach 8.20 8.40 8.60 8.8O 9.00 9.00 9.10 9'20 9.30 9.30 9.40 9.50 9.60 9.70 9.80 9.90 9.90 10.00 10.10 10'20 10.30 10.40 10.50 10.60 10.70 10.80 10.90 11.00 11.10 11.20 11.20 11.40 11.60 11.80 12.00 12.20 12.40 12.60 12.80 13.00 13.20 13.40 13.60 13.80 14.00 14.20 14.40 14.60 14.80 15.00 15.20 15.40 15'60 15.80 16.00 16.20 # | Sag Mi | 7.41 7.44 7.46 7.48 7.51 7.33 7.37 7.41 7.44 7.41 7.42 7.42 7.43 7.44 7'45 7.46 7.46 7.47 7.47 7.48 7.49 7.50 7.51 7.51 7.52 7.53 7.54 7.55 7.55 7.56 7.54 7.53 7.53 7.53 7.53 7.54 7.54 7.55 7.55 7.56 7.57 7.58 7.59 7.59 7.60 7.62 7.63 7.64 7.65 7.66 7.67 7.68 7.69 7.70 7.72 7.73 4.40 4.31 4'22 4.14 4.06 3.28 3.25 3.23 3.21 3.80 3.77 3.75 3.72 3.69 3.66 3.64 3.64 3.61 3.58 3.56 3.53 3.51 3.48 3.46 3.43 3'41 3.38 3.36 3.33 3.31 3.61 3.56 3.51 3.46 3.41 3'37 3.32 3.27 3.23 3.18 3.14 3.10 3.05 3.01 2.97 2.93 2.89 2.85 2.81 2.77 2'74 2.70 2.66 2.63 2.59 2.56 CBOD 2.66 2.60 2.54 2.48 2'43 2.65 2.62 2.60 2.57 2.77 2.74 2.72 2.70 2.67 2.65 2.62 2.62 2.60 2'58 2.55 2.53 2.51 2.49 2.46 2.44 2.42 2.40 2.38 2.36 2.34 3.54 3.48 3.41 3.35 3.29 3.23 3.17 3.11 3.06 3.00 2.95 2.90 2.85 2.80 2.75 2.70 2.65 2.60 2.56 2.51 2.47 2.43 2.39 2.35 2.31 2.27 | NBOD 5.78 5.82 5'85 5.89 5.93 9'53 9.54 9.56 9.58 10.43 10.45 10.46 10.48 10.50 10.52 10.54 10.54 10.55 10.57 10.59 10.61 10.62 10.64 10.66 10.68 10'70 10.71 10.73 10.75 10.77 11.28 11.31 11.35 11.38 11.42 11'45 11.49 11.53 11.56 11.60 11.63 11.67 11.70 11.74 11.78 11.81 11.85 11.88 11.92 11.95 11.99 12.02 12.06 12.10 12.13 12.17 Flow | Discharger Receiving Stream ---------- MODEL RESULTS : CAROLINA & SOUTHERN : CROWDERS CREEK The End D.O. is 7.73 mg/l. The End CBOD is 2.56 mg/l. The End NBOD is 2.27 mg/l. SUMMER MODEL FOR 201 PROJECT FOR CROWDERS CREEK BASIN (nyp`Z9^mC 0 zof°.It) WLA WLA WLA DO Min CBOD NBOD DO Waste Flow (mg/1) Milepoint Reach # (mg/1) (mg/l> (mg/1) (mgd) ______ _________ _______ ____ ____ __ ------------- Segment 1 7.04 0.00 1 Reach 1 21.00 22.50 5.00 0.00000 Reach 2 0.00 0.00 0.00 0.00000 Reach 3 45.00 90.00 5.00 0.00000 Segment 2 5.00 0.00 It. Reach 1 22.50 13.50 5.00 1.50000 Reach 2 0.00 0.00 0.00 0.00000 Segment 3 6.86 3.40 2 Reach 1 0.00 0.00 0.00 0.00000 Reach 2 0.00 0.00 0.00 0.00000 Reach 3 0.00 0.00 0.00 0.00000 Reach 4 90.00 63.00 0.00 0.00000 Reach 5 0.00 0.00 0.00 0.00000 Reach 6 0.00 0.00 0.00 0.00000 Reach 7 0.00 0.00 0.00 0.00000 Reach 8 287'00 354.00 0.00 0.00000 Reach 9 0.00 0.00 0.00 0.00000 3 7 9.90 7.23 3.29 2.26 10.71 3 8 9.90 7.23 3.29 2.26 10.71 3 8 10.00 7.23 3.27 2.23 10.73 3 8 10.10 7.23 3.24 2.21 10.75 3 8 10.20 7.22 3.22 2.18 10.77 3 8 10.30 7.22 3.19 2.16 10.78 3 8 10.40 7.22 3.16 2.13 10.80 3 8 10.50 7.22 3.14 2.11 10.82 3 8 10.60 7.22 3.11 2.09 10.84 3 8 10.70 7.22 3.09 2.07 10.86 3 8 10.80 7.22 3.06 2.04 10'87 | 3 8 10.90 7.23 3.04 2.02 10.8 u°s�"�' 3 8 11.00 7.23 3'01 2.00 10.1. 3 8 11'10 7.23 2.99 1.98 10.93 3 8 11.20 7.23 2.97 1.96 10.94 | 3 9 11'20 7.24 3'28 3.16 11.45 3 9 11.40 7.21 3.23 3.09 11.49 3 9 11.60 7.20 3.18 3.02 11.53 3 9 11.80 7.18 3.13 2.95 11.56 3 9 12.00 7.17 3.08 2.89 11.60 3 9 12.20 7.17 3.03 2.82 11.63 3 9 12.40 7'16 2.98 2.76 11.67 3 9 12.60 7.16 2.94 2.70 11.7O 3 9 12.80 7.16 2.89 2.64 11.74 3 9 13.00 7.16 2.85 2.58 11.78 3 9 13.20 7.17 2'80 2.52 11.81 3 9 13.40 7.17 2.76 2.47 11.85 3 9 13.60 7.18 2.72 2.41 11.88 3 9 13.80 7.19 2.68 2.36 11.92 3 9 14.00 7.20 2.64 2.31 11.95 3 9 14.20 7.20 2'60 2.26 11.99 3 9 14'40 7.21 2.56 2.21 12,02 3 9 14.60 7.22 2.52 2.17 12.06 3 9 14,80 7.24 2.48 2.12 12.10 3 9 15.00 7.25 2.44 2.07 12.13 3 9 15.20 7'26 2.41 2.03 12.17 3 9 15.40 7.27 2'37 1.99 12.20 3 9 15.60 7.28 2.33 1'95 12.24 3 9 15.80 7.29 2.30 1.91 12.27 9 16,00 7.31 2.26 1.87 12.31 3 9 16.20 7.32 2.23 1.83 12'35 1 Seg # 1 Reach # 1 Seg Mi | DM. CBOD NBOD Flow ---------- MODEL RESULTS ---------- Discharger : CAROLINA & SOUTHERN Receiving Stream : CROWDERS CREEK ------------------------ The End D.O. is 5.64 mg/l. The End CBOD is 7.76 mg/l. The End NBOD is 6.83 mg/l. Segment 1 Reach 1 Reach 2 Reach 3 Segment 2 Reach 1 Reach 2 DO Min (mg/1) Milepoint Reach # ______ _________ _______ 5.26 0.00 1 5.00 0.00 Segment 3 5.20 13.00 Reach 1 Reach 2 Reach 3 Reach 4 Reach 5 Reach 6 Reach 7 Reach 8 Reach 9 ^ 9 WLA WLA WLA CBOD NBOD DO Waste Flow (mg/1) (mg/1) (mg/1) (mgd) __ __________ 21.00 0.00 45.00 22.50 0.00 22.50 0.00 90.00 13.50 0.00 0.00 0.00 0.00 0.00 0.00 0.00 90.00 63.00 0.00 0.00 0.00 0.00 0.00 0.00 287.00 354.00 0.00 0.00 It, xR* Ww 5.00 .00000 0.00 0.00000 5.00 r~-& 08^7�^ ��� 5.00 111.50000 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00000 0.00000 0.00000 ,40.14800 / 0.00000 0.00000 0.00000 0.21300 0.00O00 *** MODEL SUMMARY DATA 4 ** 1w Disc1'rar ner : C .ROLINA SOUTHERN Receiving Stream CRO'JDERS CREEK Summer 7010 6.4 Design Temperature: 26. Subbas i n . 030837 Stream Class: C Winter 7010 ;LENGTH; SLOPE; VELOOCITY ; DEPTH: Kd Kd 1 Ka 1 Ka ; KN ; KM ; KNR ; KNR ; mile 1 ftlmi; fps ; ft ;design; 320° ;design; 320° 'design; 320° ;design; 320° : Segment 1 1 2.101 55.001 0.394 ; 0.57 ; 0.96 ; 0.73 144.50 1 39.05: 0.79 ; 0.50 1 0.48 ; 0.30 Reach 1 Segment 1 ; 0.50: 34.001 0.269 1 0.80 1 0.50 ; 0.38 :18.79 ; 16.49: 0.79 ; 0.50 1 0.48 1 0.30 Reach 2 ; Segment 1 1 1.50: 34.001 0.276 ; 0.83 1 0.51 1 0.39 ;19.27 ; 16.911 0.79 1 0.50 0.48 1 0.30 Reach 3 1 1 Segment 2 1 1.301 70.001 0.625 ; 0.51 ; 1.12 1 0.85 :56.97 ; 50.001 0.79 ; 0.50 ; 0.48 : 0.30 Reach 1 1 : 1 I 1 1 Segment 2 ; 0.60; 28.001 0.338 ; 0.80 1 0.55 ; 0.42 119.43 1 17.051 0.79 ; 0.50 : 0.48 ; 0.30 ; Reach 2 1 Segment 3 1 1.0C; 13.081 0.306 ; 1.18 ; 0.38 1 0.29 1 8.16 ; 7.161 0.48 1 0.30 1 0.48 1 0.30 ; Reach . Segment 3 1 3.201 6.00: 0.239 1 1.35 1 0.31 1 0.24 1 2.94 1 2.581 0.48 1 0.30 ; 0.48 1 0.30 1 Reach 2; 1 1 1 1 1 ; I 1 1 3 3 Segment 3 1 0.901 6.00; 0.239 1 1.36 1 0.31 : 0.24 ; 2.94 ; 2.58; 0.48 1 0.30 1 0.48 ; 0.30 1 Reach 3 ; ; Segment 3 : 1.301 6.00; 0.243 1 1.39 1 0.31 1 0.24 1 3.00 ; 2.631 0.48 1 0.30 1 0.48 1 0.30 1 Reach 4 Segment 3 ; 2.601 6.00; 0.243 1 1.44 ; 0.31 ; 0.24 ; 2.99 ; 2.63: 0.48 1 0.30 ; 0.48 1 0.30 1 Reach 5 1 Segment 3 1 0.301 6.001 0.276 1 1.67 1 0.31 ; 0.23 ; 2.45 1 2.151 0.48 0.30 1 0.48 1 0.30 1 Reach 6 1 1 / 1 , . , , 3 i 1 , 1 Segment 3 1 0.601 6.00: 0.282 1 1.71 0.31 1 0.23 1 2.50 1 2.201 0.48 1 0.30 1 0.48 ; 0.30 1 React. 7 1 1 ; 1 1 ; 1 , Segment 3 ; 1.301 6.001 0.287 1 1.73 ; 0.31 1 0.23 1 2.55 1 2.241 0.48 1 0.30 1 0.48 1 0.30 1 Reach 8 1 1 ; ; 1 Segment 3 1 5.00| 6.0V| 0.292 : 1.78 0.3\ | 0.23 | 2.0 | 2.281 V.48 ! 0.3O | V,48 | 030 | Reach 9 � Flow | cfs Segment 1 Reach 1 Waste | 1'550 Headwaters! 0.200 Tributary 1 0.000 * Runoff | 0.178 CBOD mg/l ! 21.000 | 2.000 | 0.000 | 2.000 Segment 1 Reach 2 Waste | 0.000 | Tributary 1 0.400 | * Runoff | 0.178 | Segment 1 Reach 3 Waste 1 0.130 1 Tributary | 0.000 | * Runoff | 0.178 | Segment 2 Reach 1 Waste | 2.325 1 Headwaters! 0.000 | Tributary | 0.000 1 * Runoff | 0.178 | Segment 2 Reach 2 Waste 1 0.000 | Tributary | 0.600 1 * Runoff | 0'178 1 Segment 3 Reach 1 Waste | 0.000 | Headwaters! 0.000 | Tributary 1 0.000 | * Runoff | 0.178 | Segment 3 Reach 2 Waste 1 0.000 | Tributary | 0.100 1 * Runoff 1 0.000 | Segment 3 Reach 3 Waste 1 0.000 | Tributary | 0.000 1 * Runoff | 0.178 | NBOD mg/l 1 22.500 | 3.000 1 0.000 | 3.000 0.000 | 2.000 | 2.000 1 45.000 0.000 2.000 0.000 | 3.000 | 3.000 | 1 90.000 | | 0.000 < | 3.000 1 22.500 | 0.000 1 0.000 | 2.000 | 13.500 1 0.000 | 0.000 | 3.000 | 0.000 | 0.000 | 3.000 1 2.000 1 2.000 1 3.000 ( D.O. mg/l 5.000 7'300 O.000 7.300 0.000 7.300 7.300 5.000 0.000 7.300 5.000 0.000 0.000 7.300 0.000 7.300 7.300 0.000 | 0.000 | 0.000 0.000 1 0.000 1 0.000 0.000 1 0.000 1 0.000 2.000 | 3.000 1 7.300 0.000 1 2.000 1 0.000 | 0,000 1 0.000 1 2.000 1 0.000 1 3.000 < 0.000 1 0.000 | 0.000 / 3.000 1 0.000 7.300 0.000 0.000 0.000 7.300 Segment 3 Reach 4 Waste | 0.229 � Tributary | 0.000 1 * Runoff 1 0.178 1 90.000 | 63.000 | 0.000 1 0.000 1 2.000 | 3.000 1 0.000 0.000 7.300 Segment 3 Reach 5 � Waste 1 0.000 | 0.000 | 0.000 | 0 00O _ Tributary | 0.200 1 2'000 | 3.000 1 7.300 � * Runoff | 0'178 1 2.000 | 3.000 | 7.300 =" �_�� " ° Segment 3 Reach 6 Waste | 0.000 ( 0.000 | 0.000 | 0.000 Tributary | 3.600 1 2.000 | 3.000 | 7.300 * Runoff 1 0.178 | 2.000 | 3.000 1 7.300 Segment 3 Reach 7 Waste . 0.000 1 0.000 | 0.000 1 0.000 Tributary | 0.850 | 10.500 1 5.000 | 7.080 * Runoff ! 0.178 1 2.000 | 3.000 1 7.300 Segment 3 Reach 8 Waste t 0.330 1287.000 1354.000 1 0.000 Tributary 1 0.000 | 0.000 | 0.000 | 0.000 * Runoff 1 0.178 | 2.000 | 3.000 | 7'300 Segment 3 Reach 9 Waste | 0.000 1 0.000 | 0.000 | 0.000 Tributary 1 0.510 1 10.000 1 29.000 | 5.070 * Runoff | 0.178 | 2.000 | 3.000 | 7.300 * Runoff flow is in cfs/mile � SUMMER � m~ | Seg # | Reach # | Seg Mi 1 D.O. 1 1 0.00 5.26 1 1 0.10 6.31 ° 1 1 0.20 6.84 1 1 0.30 7.11 1 1 0,40 7.26 1 1 0.50 7.33 1 1 0.60 7.38 1 1 0.70 7.41 1 1 0.8O 7.43 1 1 0.90 7.44 1 1 1'00 7.46 1 1 1.10 7.47 1 1 1.20 7.48 1 1 1.30 7.50 1 1 1.40 7.51 1 1 1.50 7.52 1 1 1.60 7'53 1 1 1.70 7.54 1 1 1.80 7.55 1 1 1.90 7.56 1 1 2.00 7.57 1 1 2.10 7.58 1 2 2.10 7.54 1 2 2.20 7.45 1 2 2.30 7.41 1 2 2.40 7.38 1 2 2.50 7.37 1 2 2.60 7'36 1 3 2.60 7.25 1 3 2.70 7.23 1 3 2.80 7.22 1 3 2.90 7.22 1 3 3.00 7.22 1 3 3.10 7.23 1 3 3.20 7.24 1 3 3.30 7.25 1 3 3.40 7.26 1 3 3.50 7.27 1 3 3.60 7.29 1 3 3.70 7.30 1 3 3.80 7.31 1 3 3.90 7.32 1 3 4.00 7.33 1 3 4.10 7~35 2 1 0.00 5.00 2 1 0.10 6.07 2 1 0.20 6.69 2 1 0.30 7.04 2 1 0.40 7.24 2 1 0.50 7.36 2 1 0.60 7.44 2 1 0.70 7.48 2 1 0.80 7.51 2 1 0.90 7.53 2 1 1.00 7.55 2 1 1.10 7.56 2 1 1.20 7,57 2 1 1.30 7.58 2 2 1.30 7.52 2 2 1.40 7'45 | CBOD NBOD Flow | 18.83 20.27 1.75 18.38 19.95 1.77 17.95 19.64 1.79 17.53 19.33 1.80 17.12 19.03 1.82 16'72 18.73 1.84 16.33 12.45 1.86 15.96 18.17 1.87 15.59 17.89 1.89 15.24 17.62 1.91 14.89 17.36 1.93 14.55 17.10 1'95 14.22 16.85 1.96 13.90 16.60 1.98 13.59 16.36 2'00 13.29 16.12 2.02 13.00 15'89 2.03 12.71 15.66 2.05 12.43 15.44 2.07 12.16 15.22 2.09 11.89 15.00 2'11 11.64 14.79 2.12 10.11 12.92 2.52 9.94 12.72 2.54 9.77 12.51 2'56 9.61 12.31 2.58 9.45 12.12 2.59 9.29 11.93 2.61 10.99 15.63 2.74 10.81 15.39 2.76 10.63 15.15 2.78 10.46 14.91 2.80 10.29 14.68 2.81 10.12 14.46 2.83 9.96 14.23 2.85 9.80 14.02 2.87 9.64 13'80 2.89 9'49 13.59 2'90 9.34 13.39 2.92 9.19 13.18 2.94 9.04 12.98 2.96 8.90 12.79 2.97 8.76 12.60 2.99 8.63 12.41 3.01 22.50 13.50 2'33 22.10 13'36 2'34 21.71 13.22 2.36 21.33 13.08 2.38 20.95 12'95 2.40 20.59 12.81 2.41 20.23 12.68 2.43 19.88 12.55 2.45 19.53 12.43 2.47 19.20 12.30 2.49 18.87 12.18 2.50 18.54 12.06 2.52 18.23 11.94 2.54 17.92 11.82 2.56 15.08 9.95 3.16 14.86 9.83 3.17 2 2 f -.50�;7 -.40 14.64 9.71 3.19 2 2 1.60 7.37 14.42 9.59 3.21 2 2 1.70 7.36 14'21 9.47 3.23 & � 2 2 1.80 7.35 14.01 9.35 3.25 | � 2 2 1.90 7.34 13.80 9.24 3.26 | 3 1 0'00 7.34 11.32 10.76 6.27 / � 3 1 0.10 7.29 11.21 10.64 6.29 3 1 0.20 7'24 11.10 10.51 6.31 � 3 1 0'30 7.20 10.99 10'39 6.33 3 1 0.40 7.17 10.88 10.28 6.34 3 1 0.50 7.15 10.77 10.16 6.36 3 1 0.60 7'13 10.67 10.04 6.38 3 1 0.70 7.12 10.56 9.93 6.40 3 1 0.80 7.11 10.46 9.81 6.42 3 1 0.90 7.10 10.36 9.70 6.43 3 1 1.00 7.09 10.25 9.59 6.45 3 2 1.00 7.10 10.13 9.49 6.55 3 2 1.20 6.88 9.97 9.26 6.55 3 2 1.40 6.70 9.81 9.04 6.55 3 2 1.60 6.55 9.66 8.82 6.55 3 2 1.80 6.43 9.50 8.61 6.55 3 2 2.00 6.33 9.35 8.41 6.55 3 2 2.20 6.26 9.20 8'20 6.55 3 2 2'40 6.20 9.06 8.01 6.55 3 2 2,60 6.15 8.92 7.81 6.55 3 2 2.80 6.12 8.77 7.63 6.55 3 2 3.00 6.10 8.64 7.44 6.55 3 2 3.20 6.09 8.50 7.26 6.55 3 2 3.40 6.08 8.36 7.09 6.55 3 2 3.60 6.09 8.23 6.92 6.55 3 2 3.80 6.09 8.10 6.75 6.55 3 2 4.00 6.10 7.97 6.59 6.55 3 2 4.20 6.12 7.85 6.43 6.55 3 3 4.20 6.12 7.85 6.43 6.55 3 3 4.30 6.13 7.77 6.35 6.57 3 3 4.40 6.15 7.69 6.26 6.59 3 3 4.50 6.16 7.62 6.18 6.60 3 3 4.60 6.17 7.54 6.09 6.62 3 3 4.70 6.19 7.47 6.01 6,64 3 3 4.80 6.20 7.39 5.93 6'66 3 3 4.90 6.22 7.32 5.85 6.68 3 3 5.00 6.23 7.25 5.77 6.69 3 3 5.10 6'25 7.17 5.69 6.71 3 4 5.10 6.04 9.91 7.59 6.94 3 4 5.20 6.03 9'81 7.49 6.96 3 4 5.30 6.03 9.72 7.39 6.98 3 4 5.40 6.02 9.62 7.29 6.99 3 4 5.50 6.02 9.53 7.19 7.01 3 4 5.60 6.02 9'43 7.09 7.03 3 4 5'70 6.02 9.34 7.00 7.05 3 4 5.80 6.03 9.25 6.91 7.07 3 4 5.90 6.03 9.16 6.81 7.08 3 4 6.00 6.04 9.07 6.72 7.10 3 4 6.10 6.05 8.98 6.64 7.12 3 4 6.20 6.06 8.89 6.55 7.14 3 4 6.30 6.07 8.81 6.46 7'15 3 4 6.40 6.08 8.72 6.38 7.17 3 5 6.40 6.11 8.54 6.28 7.37 3 5 6'60 6.13 8.37 6.12 7.41 3 5 6.80 6.16 8.21 5.96 7.44 3 5 7.00 6.19 8.06 5.81 7.48 3 5 7.20 6.22 7.90 5.66 7.51 3 5 7.40 6.25 7.75 5.51 7.55 3 5 7.60 6.28 7.61 5.37 7.59 3 5 7.80 6.31 7.46 5.23 7.62 � _ 3 5 __8.00 6.35 7.32 5.10 7.66 � 3 5 8.20 6.38 7.18 4.97 7.69 ". 3 5 8.40 6.41 7.05 4.84 7.73 3 5 8 '60 6.44 6.91 4.72 7.76 o & - _ -u_- 'uo u 9 oo �'51 6.66 4.48 7.83 �''' - -- - -� N� 3 6 9.00 6.76 5.19 4.02 11.43 ~~ 3 6 9.10 6.76 5.15 3.97 11.45 -~ 3 6 9.20 6.75 5.11 3.93 11.47 � 3 6 9'30 6.75 5.07 3.89 11.49 3 7 9.30 6.78 5.45 3.96 12.34 3 7 9.40 6.77 5.40 3.92 12.36 3 7 9.50 6.77 5.36 3.88 12.37 3 7 9.60 6.77 5.32 3.84 12.39 3 7 9.70 6.77 5.28 3.80 12.41 3 7 9.80 6.77 5.24 3.76 12.43 3 7 9.90 6.77 5.21 3.72 12.45 3 8 9.90 6.59 12.49 12.77 12.78 3 8 10.00 6.47 12.39 12.63 12.79 3 8 10'10 6.36 12.30 12'49 12.81 3 8 10.20 6.25 12.20 12.35 12.83 3 B 10.30 6.15 12.11 12.21 12.85 3 8 10.40 6.06 12.02 12.08 12.86 3 8 10.50 5.98 11.92 11.9+ 12.88 3 8 10.60 5.90 11.83 11.81 12.90 3 8 10.70 5.83 11.74 11.68 12.92 3 8 10.80 5.76 11.65 11.55 12.94 3 8 10.90 5.70 11.56 11.42 12.95 3 8 11.00 5.64 11.48 11.29 12.97 3 8 11.10 5.59 11.39 11.17 12'99 3 8 11.20 5.55 11.30 11.05 13.01 3 9 11.20 5.53 11.25 11.72 13.52 3 9 11.40 5.44 11.09 11.47 13.55 3 9 11.60 5.38 10.92 11.22 13.59 3 9 11.80 5.32 10.76 10.98 13.62 3 9 12.00 5.28 10.60 10.74 13.66 3 9 12.20 5.25 10.44 10.51 13.69 3 9 12.40 5.22 10.29 10.28 13.73 3 9 12.60 5.21 10.13 10.06 13.77 3 9 12.80 5.20 9.98 9.85 13.80 3 9 13.00 5.20 9.84 9.64 13.84 3 9 13.20 5.21 9.69 9.43 13.87 3 9 13.40 5.22 9.55 9.23 13.91 3 9 13.60 5.23 9.41 9'03 13.94 3 9 13.80 5.25 9.27 8'84 13.98 3 9 14.00 5.28 9,13 8.65 14.02 3 9 14.20 5.30 9.00 8.46 14.05 3 9 14.40 5.33 8.86 8.28 14.09 3 9 14.60 5.36 8.73 8.11 14.12 3 9 14.80 5.39 8.61 7.93 14.16 3 9 15.00 5.42 8.48 7.76 14.19 3 9 15.20 5.45 8.36 7.60 14.23 3 9 15.40 5.49 8.23 7.44 14.26 3 9 15.60 5.53 8.11 7.28 14.30 3 9 15.80 5.56 7.99 7.13 14.34 3 9 16.00 5.60 7.88 6.98 14.37 3 9 16.20 5.64 7.76 6.83 14.41 | Seg # 1 Reach # 1 Seg Mi 1 D.O. CBOD NBOD Flow ^