ML20056D597
| ML20056D597 | |
| Person / Time | |
|---|---|
| Site: | Brunswick  |
| Issue date: | 02/06/1991 |
| From: | Bishop S, Watson P, Wright P CAROLINA POWER & LIGHT CO. |
| To: | |
| Shared Package | |
| ML20056D596 | List: |
| References | |
| 91-0039, 91-0039-R00, 91-39, 91-39-R, NUDOCS 9308170125 | |
| Download: ML20056D597 (109) | |
Text
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ENCLOSURE 2 - ! i
. BRUNSWICK STEAM ELECTRIC PLANT, UNITS 1 AND 2 l NRC DOCKET NOS. 50-325 & 50-324 ~
~ OPERATING LICENSE NOS. DPR-71 & DPR-62 .;
REQUEST FOR LICENSE' AMENDMENT [ SERVICE WATER SYSTEM ; i l l i
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EE_R 91-0039 EVALUATION OF SERVICE WATER DESIGN BASIS CAPABILITY l t i l 1 i 1 i i i i
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j t .~ .. _ t FORM 1 l EER No. H-OO39 i ENGINEERING EVAL"ATICN Rev. No. O l REPORT Page No. 1 ! I i PT 2+.6.4
- 1. Reference NCR, LER. *a/JO. etc. & $P 91006 File No. 4cGo l l
- 2. Brief description of ite:n/ activity EVAtu ATioN or seg- / Class A (Q-List) l VicE waiter DEsic-92 tuis c APA sit _ ina, C Class B-3 (FP-Q) l i C Other j
- 3. Disposition I a. Use/ acceptable as is I C b. Per=anent repair / rework 1 C c. Temporarr change; Expiration date C Temocrary repair j C Temporary condition l C JCO/STSI (O Preliminary)
- d. Other 4 . Final Resolution 5:/ a. Complies with FSAR, design, drawing, code, and qualitr requirements.
C b. Acceptable deviation frem FSAR, design, drawing, code, or quality requirements. Safety review (AI-109) required. j
- 5. Follow-up Requirements C a. Surveillance activities, responsible group (s)
C b. Action items, responsible group (s) W c. None
- 6. Review / Approval j '
Responsible Engineer
- Xm Date 2-(, 91
)
/Yes C No Technical Review
- 4t$7 Date 7 4-9/
Engineering Supervisor $ M-- 4.0 Date E/Al'It Q /
- C Yes fNo EQ Review , ,
Date VYes a No QA Review NN Date f/b/9/ l C Yes #No ONS/CNS Review Date l l l C Yes 42' No FNSC Review _f Date - j Approved Ak (( b Date Jfh/9/ i g //
- 7. Distribution:
Document Control (EER File) Other: NED BESS Section Mana5er Manager - Maintenance Supervisor - ISI Responsible Engineer
- Qualified Technical Q-List /EDES Coordinator - PEG Reviewer if Quality Operations Principal Engineer Class A and box 4b Nuclear Engineering Depart =ent (NED-Raleigh) checked Specialist - Regulatory Compliance NED EQ Group - Raleigh ;
EDC - Technical Support l QA Engineering l BSEP/Vol. XI/EbiP-12 18 Rev. 27 l
- . - . . - .~- . . . ._ -.
1 1 EER No. 91-0039 Rev. No. O ENGINEERING EVALUATION. page.No. 2 LIST OF EFFECTIVE PAGES I PAGE NO. REVISION l 1-21 0 , i t i i, 4
t i EER No. 91-0039 Rev. No. 0 ENGINEERING EVALUATION Page No. 3 TABLE OF CONTENTS ! SECTION PAGE NO. Traveler (Form 1) 1 i List of Effective Pages 2 , Table of Contents 3 I. Problem Evaluation _4 A. Problem Description 4 B. Evaluation / Disposition 5' C. Corrective Actions
- 12 .
D. Acceptance Testing
- 12 II. EER Action Item Notifications (Form 4)* 12 i III. Safety Review (per AI-109) 12 ;
i IV. EQ Impact Evaluation (per ENP-34.1, Form 3)* 12' I V. Attachments: I 1-PT-24.6.4 Data' Sheets A: i B: SP-91-006 Data Sheets I C: KYPIPE Computer Output: File "U1CALBN2" Results D: KYPIPE Computer output: "U1CALBN2" Data File E: KYPIPE Computer Output: File "UISCNRIO" Results F: KYPIPE Computer Output: "UISCNRIO" Data File
- Not Applicable l
EER No. 91-0039 Rev. No. 0 - ENGINEERING EVALUATION Page No. 4 I. PROBLEM EVALUATION - A. PROBLEM DESCRIPTION l During the Winter 1990-91 BSEP U1 Refueling Outage, several { modifications were implemented that affected the hydraulic ; characteristics of the Service Water (SW) system. Although the ; individual plant modifications included acceptance testing which ensured that those modifications individually did not impair the capability of the system to perform its design basis function, ! they did not comprehensively test the entire system. Therefore, ) as committed to the NRC, Periodic Test 1-PT-24.6.4 was run to , demonstrate the hydraulic capability of the SW system in meeting ' the design basis flow requirements to safety related components. and to measure system leakage through the cross-tie valves. Data ' resultant from 1-PT-24.6.4 would be used to calibrate the latest : BSEP U1 SW KYPIPE computer hydraulic model; this calibrated model ' would then have the worst-case accident scenarios run upon it.
~
.i Capability of the SW system would then be judged based on the.
flow shown on the output of these worst-case scenario computer l runs. However, during the performance of 1-PT-24.6.4, it was observed ! that while the two Nuclear Service Water Pumps (NSWPs) "A" and "B" were running in parallel, discharging into a common header, , the "A" pump consistently had higher flow values as measured by I the Controlotron portable ultrasonic flow meter. Since these two j pumps are essentially identical, their flow output when discharging into a common header should be close to. equal. Since there was some suspicion that the "B" pump may have experienced degradation which allowed the "A" pump to'" overpower" it when the two were running in parallel, it was decided to perform more testing to specifically investigate and compare the two pumps' flow characteristics. SP-91-006 was written and implemented to observe the two pumps' performance characteristics over a range of flows, both while the pumps were operating together and ; singly. The purpose of this Engineering Evaluation is to analyze the data provided by 1-PT-24.6.4 and SP-91-006 to find if there is a concern regarding NSWP degradation, to calibrate the latest l KYPIPE hydraulic model of the SW system, and to apply the worst-l case accident scenarios to this model to determine whether or not I the SW system is capable of meeting its design basis requirements. l
_ _ _~_ i EER No. 91-0039 Rev. No. 0- ! ENGINEERING EVALUATION Page No. 5 l B. EVALUATION / DISPOSITION > t Periodic Test 1-PT-24.6.4 took data at three different SW system line-ups; all three line-ups had both Nuclear Service Water Pumps (NSWPs) operating in parallel. Flow values for the two NSWPs as , observed during that test are shown below (the data sheets from 1-PT-24.6.4 are included in this EER as Attachment A): TABLE 1: 1-PT-24.6.4 NUCLEAR SERVICE WATER PUMP FLOW DATA i f 1-PT-24.6.4 NSWP 1A -NSWP 1B STEP NO. FLOW FLOW [ 9.3.29 5664.0 gpm 4601.25 gpm ! 9.3.33 5387.0 gpm 4668.0 gpm 4 9.3.42 5693.0 gpm 4810.0'gpm As can be seen by comparing the two pumps' flow values, the discrepancy or mismatch between the two pumps varies from i 719 to 1063 gpm. Since the two. pumps are essentially identical ( and are discharging into a common header, their flows should be identical. One of the possible explanations for this anomaly is that NSWP "B" had experienced some kind of degradation which was causing it to operate off of its established performance curve. If this was the case, then the ability of that pump to provide design-basis required flows when it was operating alone would be in question. Due to the nature of these pumps, their performance when operating alone cannot be inferred from observation of their operation in parallel. Furthermore, the data from 1-PT-24.6.4 was taken at basically the same total flow value, so it could not be determined if this flow mismatch only existed in the flow ' regime observed in that test, or if the flow mismatch would exist at all flow values. Thus, more testing was needed which would portray pump performance operating together and alone, and at a variety of flow regimes. I Special Procedure SP-91-006 was written to take pump flow as well as intake and discharge pressure data to compare and validate the , 1 previously established performance curves used in the KYPIPE SW l hydraulic model. Performance data could be compared to determine if one pump had experienced any performance degradation relative to the other pump. Results of this procedure (Data taken in l i
i r EER No. 91-0039 Rev. No. O ENGINEERING EVALUATION Page No. 6 i i i n. SP-91-006 is included in this EER as Attachment B) showed that I when one NSWP operated alone, its Developed Head (and therefore . its flow) was essentially identical to the other pump's Developed-Head when pumping into an identical system. Also, when the two pumps ran in parallel, their Developed Heads matched. Furthermore, their performance agreed with what was anticipated , from referencing the previously established pump curves. The ' discrepancies in pump flows seen in 1-PT-24.6.4 were attributed to the effects of different NSWP discharge strainer pressure + drops between the two NSWPs and inaccuracies in the permanent l' installed instrumentation and the test instrumentation. Although the Controlotron ultrasonic flow meter readings from SP-91-006 ' were found to be inaccurate (placement of these meters to achieve more accurate data will be evaluated in a future project) for the ' individual NSWP flows, the totalled NSWP flow readings were reasonable when compared to the flow received by the SW system, and tracked well with changes in the system's lineup. Since SP-91-006 showed that both NSWPs were running on their previously established performance curves, then the SW KYPIPE hydraulic model would not require alteration in NSWP curve input data, and the results obtained in 1-PT-24.6.4 could-be used to calibrate the model. The SW KYPIPE computer hydraulic model was calibrated by adjusting input data for minor losses for the various branches until the output flows closely matched the resultant flows from 1-PT-24.6.4. Since combined pump flow readings obtained from the Controlotron flow meters in SP-91-006 were found to be trustworthy, the combined pump flow readings taken in 1-PT-24.6.4 were used to adjust the SW cross-tie leakage flow parameters in the KYPIPE hydraulic model during model calibration. The hydraulic model calibration was made under the KYPIPE data file titled "U1CALEN2"; the results file and the input data file are included in this EER as Attachments C and D, respectively. A comparison of calibrated model flows versus system test flows is provided in the table on the following page.
l EER No. 91-0039 Rev. No. O ENGINEERING EVALUATION Page No. 7 l i F TABLE 2: COMPARISON OF FLOW VALUES FROM 1-PT-24.6.4 TEST AND CALIBRATED KYPIPE MODEL (All flows in gpm) I STEP 9.3.29 STEP 9.3.33 STEP 9.3.42 COMPONENT TEST MODEL TEST MODEL TEST MODEL , NSWPs 1A & 1B 10265 10723 10055 10589 10503 10808 Combined Flow SW Lube Water 131 131 124 124 127 127 DG 1 SW 1386 1341 1300 1337 1300 1321 i DG 2 SW 1422 1402 1428 1398 1392 1382 RBCCW SW 3400 3400 3300 3300 3300 3300 RHR SW A Loop 3000 3000 0 0 0 0 : RHR SWBP A M/C 67.5 67.3 0 0 0 0 RHR SWBP C M/C 66.2 67.0 0 0 0 0 RHR SW B Loop O O 3000 3000 3000 3000 RHR SWBP B M/C 0 0 66.5 58.0 65.8 56.7 RHR SWBP D M/C 0 0 63.6 64.7 63.3 57.9 RHR Pump Room 484.8 479.1 467.1 478.1 463.6 471.7 Cooler A CS Pump Room 91.2 91.4 91.2 91.2 90.6 90.0 Cooler A RHR Pump Seal 33.8 33.4 32.1 33.3 31.2 32.9 1 Coolers A & C RHR Pump Room 406.2 408.9 402.2 405.9 400.8 400.5 Cooler B CS Pump Room 66.2 66.2 62.0 65.7 61.7 64.8 Cooler B RHR Pump Seal 31.5 30.5 30.1 30.3 30.4 29.9 Coolers B & D
I l EER No. 91-0039 Rev. No. O ENGINEERING EVALUATION Page No. 8 i I I Now that the KYPIPE had been successfully calibrated, it could be ' used to have several worst-case accident scenarios run upon it to determine if the SW system could fulfill its design basis I functions. , i Several worst case O to 10 minute accident scenario files were I chosen from Calculation G0050A-12 (although this is a BSEP Unit 2 calculation, it was referenced since its listing of scenarios is j currently more complete than the comparable Unit 1 calculation). , During the first ten minutes of an accident scenario, operator , action to throttle or close valves is not considered; thus the primary concern is that the NSWPs will exceed their maximum flow ' limits. A worst case O to 10 minute accident scenario was chosen ' for each of the NSWP Intake Bay water levels of interest: Low Bay , Level (-6.0'); High Bay Level (+2. 0 ') ; Flood Bay Level (+22.0'); and Low-Low (formerly refered to as Hurricane Bay Level) Bay . Level (-8.63'). Where there was more than one worst case ; scenario for a given bay level, an alternate worst case scenario j was chosen and run as well. The scenarios chosen are copies of the system responses given in the Calculation G0050A-12 files listed in the table below: TABLE 3: WORST CASE ACCIDENT SCENARIOS: FILE NAMES BAY LEVEL ELEVATION FILE NAME & CHANGE NOs. Low -6.0' U2NOPOWR Changes 7 & 8 NOVTLHDR Changes 14 & 15 (Alt.) ! High +2.0' U2NOPOWR Changes 5 & 6 Flood +02.0' NOVTLHDR Changes 16 & 17 [ RBCCWOUT Changes 4 &5 (Alt.) ! Low-Low -8.63' RBCCWOUT Changes 2 &3 , f For each NSWP Intake Bay water level, there is a corresponding j maximum flow limit for the NSWPS. This flow limit is based upon ! ensuring that the pump is not endangered due to loss of Net ! Positive Suction Head (NPSH); that is, the flow limit ensures that available NPSH always is greater than or equal to the i required NPSH. The actual flow limits are divided by 1.05 to j account for the KYPIPE hydraulic model's 5% accuracy. Thus, the ' resultant maximum flow values that are allowable NSWP flows in ! the KYPIPE output are shown on the following table: (
)
i
l EER No. 91-0039 [ Rev. No. O ; ENGINEERING EVALUATION Page No. 9 i I TABLE 4: MAXIMUM HBWP FLOW LIMITS c. BAY WATER ACTUAL KYPIPE LEVEL ELEVATION FLOW LIMIT FLOW LIMIT Low -6.0' 9292 apm 8849 gpm High +2.0' 9552 apm 9097 gpm t Flood +22.0' 10000 gpm 9523 gpm Low-Low -8.63' 8225 gpm 7833 gpm ! The scenarios shown in Table 3 were then run on the calibrated KYPIPE SW hydraulic model under the file name U1SCNRIO (the results file and the input data file are included in this EER as Attachments E and F, respectively). The results are tabulated below. , TABLE 5: RESULTANT FLOWS FROM KYPIPE WORST CASE SCENARIOS i U1SCNRIO SCENARIO WATER KYPIPE OUTPUT > CHANGE COPIED FROM: ELEV. ALLOWABLE FLOW FROM NOs. (FILE & CH. NO.) FLOW U1SCNRIO O& 1 U2NOPOWR Ch. 7 &8 -6.O' 8849 gpm 8347 gpm 2 & 3 U2NOPOWR Ch. 5 & 6 +2.0' 9097 gpm 8496 gpm 4 & 5 NOVTLHDR Ch. 16 & 17 +22.0' 9523 gpm 8951 gpm 6 &7 RBCCWOUT Ch. 2 & 3 -8.63' 7833 gpm 7833 gpm 8 & 9 RBCCWOUT Ch. 4 & 5 +22.0' 9523 apm 8559 gpm 10 & 11 NOVTLHDR Ch. 14 & 15 -6.0' 8849 gpm 8524 gpm ; 1 As can be seen from Table 5, all the output flows from the worst case scenarios are less than or equal to the maximum allowable l j KYPIPE flow limit for the relevant water level. { As an additional check, an additional KYPIPE run was performed to simulate the worst case after 10 minute accident scenario; in l I l
. j
EER No. 91-0039 [ Rev. No. 0 ENGINEERING EVALUATION Page No. 10 ' e i this time frame, operator action to shut or throttle unnecessary i flows can be credited providing that the action is feasible in that scenario (i.e., operator action cannot be assumed to : manually close a valve during a postulated LOCA scenario that , began during operational modes 1, 2, or 3 ; likewise, operator ! action cannot be assumed to go out to the Diesel Generator l Building and throttle the DG SW valves during a postulated ! hurricane). Since operator action can be considered for i throttling or closing valves in the after 10 minute cases, ' exceeding the NSWP maximum flow is not a concern. _Instead, the ; prevailing concern is ensuring that the various heat exchangers j which require cooling during this time frame receive sufficient ; SW to allow them to meet their design basis cooling functions. ; Since the hydraulic model has a 5% accuracy of flow output data, j the flows obtained from the KYPIPE after 10 minute scenario are ' reduced by 5% before comparing to the minimum flow requirement of the particular heat exchanger. The worst case after 10 minute i scenario is a copy of the system response given in Calculation j G0050A-12, File U2NOPOWR Change No. 4. This scenario as run on i the calibrated KYPIPE model is listed in the "U1SCNRIO" file as Change No. 13; it is included in this EER as Attachments E and F for the results file and input data file, respectively. A comparison of KYPIPE heat exchanger flows to the minimum flow , values is tabulated on the following page. l 1 i i
i i t EER No. 91-0039 l Rev. No. O ; I ENGINEERING EVALUATION Page No. 11 i i I TABLE 6: COMPARISON OF AFTER 10 MINUTE HEAT EXCHANGER FLOWS: I KYPIPE WORST-CASE SCENARIO FLOWS i VERSUS MINIMUM HEAT EXCHANGER FLOWS i KYPIPE 95% OF KYPIPE HEAT EXCHANGER t HEAT EXCHANGER OUTPUT FLOW OUTPUT FLOW REQUIRED FLOW
- I SW Lube Water 113 gpm 107 gpm 95 gpm ;
DG 1 SW 1054 apm 1001 apm 350 a_u_m DG 2 SW 1102 gpm 1047 gpm 350 gpm i RHR (B Loop) 2994 gpm 2844 apm 2500 gpm** RHR SWBP B M/C 44 gpm 42 gpm 38 gpm RHR SWBP D M/C 45 gpm 43 gpm 38 gpm ; I RHR Pump Room 367 gpm 349 gpm 186 gpm Cooler A , CS Pump Room 70 gpm 66 gpm 47 gpm Cooler A ) l RHR Pump Seal 26 gpm 25 gpm 0 gpm Coolers A & C RHR Pu=p Room 311 gpm 295 gpm 186 gpm Cooler B CS Pump Room 50 gpm 48 gpm 47 gpm Cooler B RHR Pump Seal 23 gpm 22 gpm 0 gpm Coolers B & D All minimum flow requirements assume 90 F Service Water
** 2500 gpm minimum RHR SW flow requirement since this postulated scenario began during operational mode 4 or 5 As can be seen from the table, all flow outputs from the KYPIPE model worst case after 10 minute scenario were above the relevant
t i l EER No.- 91-0039- : Rev. No.- 0 : ENGINEERING EVALUATION Page No. 12 i minimum flow requirements. Thus, the SW system is capable of l meeting its design basis functions. ! C. CORRECTIVE ACTIONS f i No corrective actions are required by this EER. l I D. ACCEPTANCE TESTING No acceptance testing is required by this EER. ; II. EER ACTION ITEM NOTIFICATIONS No action items, and therefore no action item notifications, are required by this EER. l III. BAFETY REVIEW See page 13 of this EER. i IV. EO IMPACT EVALUATION See page 21 of this EER. I J e
g .. ER th. W oom ATTACHMENT 2 (Conc'd) g g O PAGE f4 o . 1~.b in l l ATTACEMENT A CP&L SATETY REVIEW Page 1 of 8 SATETY REVIEW CCVER SEEET DOCUMENT NO. E U. 91 - 00 ~5 el REv. No. O
SUMMARY
DESCRIPTICN CF TITI.E: EVALM AWBQ OF SW OfTf 4 tsA515 cap 4 fst u g
- 1. Responsible Supervisor, Assign: #
Safety Analysis Preparar: 'Ecrrz.- her e Safety Evaluator: "Rf:> m 'STrtxtt Safaty Raviawar: Pir try- k.) a. t o m
- 2. Safety Analysis Preparar: Complete PART I, SAFETY ANALYSIS
- 3. Safety Evaluator: Cc= plate Part !!, Itam Classificattc= and Routing Screen.
- 4. Safety Evaluater: For procedura changes, Part III =ay be '
complated. If either question 1 or 2 is "yes," than Part 77 is not required; skip to n-Mer 8 of this cover sheet.
- 5. Safety Evaluator: Iatermine which DISCIPLI2mE are required for review of this item (including own) and dancte by checking the appropriata bicek balew. Pill in names of QUAI.IFIED SAFETY RIVIEWERS in space provided.
DISCIPLIIES Recuired: (Print Name) i [] Nuclear Plant Operations ' [] Nuclear Enginaaring [4 Mechanical 12cest e Sw et_ [] Electrical [] Instru=antation & Centrol [] Str.:ctural [] Metallurgy [] Chemistry /Radicchanistry [] Health Physics [] Administrative Centrols
- 6. Each person denoted in step 5 perform a first level SAFETY REVIEW and provide input into the UNREVIEWED SATETY COESTICN dater =1natien. Safety Evaluator ce= plate Part T7.
7 Each persen denoted in step 5 sign the cc= plated Part rl, indicating cc=pistion of a first level SAFETY REVIEW. B. Safety Reviewar: Perform a SAFETY REVIEW in accordance with Section 8.0. [$ The activity dcas not create an UNREVIEWED SAFETY CUESTICN. [] The activity =av create an CNREVIEWED SATETY QUESTICN. Safety Reviewer DISCIPLINE: h f"""
///,.e 4a fi/ /,/
Date 2 4 /
- 9. Responsible Supervisor: All DISCIPLII2S nacassary and important to the item have baan reviewed: WMb,JJ6 Data F-6 b~/
/
- 10. PNSC review: If required, attach a completed Part Y.
10CTR50.59 PROCPX: MANUAL RE7ISION 1 0 AI-109 Rev. 000 Page 71 of 82
EER A. 91-0039 ATTAC1DiENT'2 (Cont'd) g g, g- , EAS* N o - M l t ATTACEMENT A '! CP&L SATETY REVIEW Page 2 of 8 ( PART I: SAFETY tuuy3Is i (See instr 2ctions in Section 8.4.1)- .; (Attach additional sheets as necessary) ; DOCUMENT NO.. EER 91-00259 REv. NO. o ! 5 SCHMARY DESCRIPTICN CF TITI.Z: EVAL 4ATso,J or SW Omu tun em w-o DESCRIPTICN CF CHANGE: sa: p ar ru usr o ! I i i i ANALYSIS: sgg my m,. 3 . i i r i I i RETERENCES: srE NT r A CH Cb i I l 1 SATETY ANALYSIS PREPARER: w CATE: 2-6 91 [Aceita sw-c.de 10CTR50.59 PROGRAM MANUAL , REVISION 1 O AI-109 Rev. 000 Page 72 of 82 1
EER Mo. 91-0031 Rev . No. O : Pay _. N o . 15 l ATTACHMENT A Page 3 of 8 i CP&L SAFETY REVIEW PART I: SAFETY ANALYSIS (Cont'd.) l FOR i EER 91-0039 L I l DESCRIPTION: This EER serves to analyze and evaluate Service Water system test data taken in Periodic Test 1-PT-24.6.4 and Special Procedure SP-91-006. The data was analyzed by I several means to ensure its reliability, then it was used to i ) calibrate the existing Service Water KYPIPE hydraulic ' computer model, including a calibration of the system crosstie leakage. Once the computer model was successfully calibrated, it was used to run several worst case accident i scenarios. The resultant flows from these scenarios were ' compared to the allowable limits for the SW system (the NSWP ; flows for the 0-10 minute scenarios to ensure pump runout or l NPSH problems do not exist, and the heat exchanger flows for , the after 10 minute scenarios to ensure these heat exchanger ' receive sufficient Service Water to perform their design ] basis functions). The comparison of flows resultant from ! the computer scenarios to the limiting SW flows showed that i the system remains capable of fulfilling its design basis purposes. l i ANALYSIS: This analysis is for the mechanical discipline. This i EER merely serves to analyze data already taken under l previously approved procedures (1-PT-24.6.4 and SP-91-006). This EER does not physically change any portion of the l i Service Water or any other system. The EER shows the SW l system to be capable of performing it design basis duties ! during an accident / transient coincident with a single { failure. No document revisions are required resultant from 1 this EER. No action items are result 2nt from this EER. I l
REFERENCES:
(1) TS 3/4.7.1.2 j (2) TSI 90-03, Rev. 0 ' (3) BSEP FSAR Chapters 9 & 15 (4) Calculations G0050A-10 & -12 (5) SW Syster Hydraulic Analysis Report (6) 1-PT-24.6.4 l (7) SP-91-006 i
o I EER No. att-co39 ! !. ATTACHMENT 2 (Cont'd) 2.e v. No. O' i Page No. 16 l
^
]
ATTACEMENT A CP&L SAFETY REVIEW Page 4 cf Q FART II; ITEM C' "SIFICATICN AND ROUTING SCREEN
\
OOCOMENT NO. EER 91-00 %9 REV. NO. O f I Yes No -
- 1. Does this itam reprasant a change to the facility or procedures as described in the [] g ,
t SAFETY ANALYSIS REPCRT, or a test or experimant not described in the SAFETY ' ANALYSIS REPORT?
- 2. Ooas this itam involve a change to the individual plant operating License or to its [] g i
Technical Specifications?
- 3. Does this item require a revision to the FSAR?
- 4. Ooes this item involve a change to the Offsite [] M Dosa Calculation Manual? [] M
- 5. Ooss this item ccnstituta a change to the Process Centrol Program? [] 3
- 6. Does this itam involva-a major change to a Radwaste Traat= ant System? [] 3 :
7 Does this item involve a change to the , Technical Specification Equipment I.ist [] g Program?
- 8. Ooes this item constituta an unreviewed enviren=antal questien defined in the SENPP [] M l Environ = ental Protecticn Plan or a significant environmental i= pact (Brunswick and E.B.
Robinson NPDES Permits)?
- 9. Ocas this item involve a change to a !
j previously accepted:
- a. Quality Assurance Program
- b. Security Plan (including Training, [] M- t Qualification, and Contingancy Plans)? [] M t
- c. Emergancy Plan?
- d. Independant Spant Fuel Storaga [] M !
Installation licensa? (If yes, refer to [] M - appropriate site procedure for 10CTR72.48 requirements.) IF TEE ANSWER TO ANY CF THE ABOVE QUESTIONS IS "YES", THEN IDENTITY THE EASIS DOCOMENT AND SECTICN(S) INVOLVED. SEE SECTICN B.4.2 FOR INSTRUCTIONS FOR EACE "YES" ANSWER.
REFERENCES:
75AR Cunrrra.s 9 &, 15 *, TS i
~3 /4 .
- 7. f. L TS T 90 03
/
DISCIPLII'E SIGNATURE o / DATE We Safety Evaluator se ce. ou. 8Z 7*h / 7-C * 'l l V 10CrR50.59 PROCRAM MANUAL - 56 - REVISICN 1 0 AI-109 Rev. 000 Page 73 of 82
r - , EEE Wo. 91-0039 ATTACHMENT 2 (Cont'd) ~Q w , gg , g Ea.3e No, {~T ATTACEMENT A CPEL SAFETY REVIEW Page 1 of 8 FART !!!: CHANGES TO PLANT PROCEDLTES l 1 DOCCMENT NO. EER 91-O 0101 REV. NO. G Yes No _
- 1. Does this itam represent a change to [] g proceduras for which a 10CTR50.59 EVALUATION
{ is required and is the rhange fully addressed by another e g isted UNREVIEWED SAFETT QUESTICN datar=s. nation? (See Sectics 7.2.2.5) i RETERENCE DOCUMENT: REV.
- 2. Is the change a non-intent change rhich does [] }g no more than: (See Section 7.2.2.3) !
- a. Correct typographical errors which do not altar '
the meaning or intent of the procedure; c r,
- b. Add steps for clarificatica (provided they are consistant with the original purpose or applicability of the procedure); o r,
- c. Change the title of an organirational position: l or, '
- d. Change names, addresses, or telephone nu=bers .
of persons; cr, {
- e. Change the designation of an itam of equip = ant l where the equip = ant is the same as the original {
equip. ant or is an authorized replacement; or,
- f. Change a specified tool or instru=ent to an equivalent substitute: or,
- g. Change the for=at of a procedure without altering the maanang, intent, or contant: or
- h. Oslata a part or all of a procedura, the deleted portions of which are wholly covered by approved plant procedures? l If the answer to either Questien 1 or Question 2 in PART !!! is "Yes," then PART IV need not he co=pleted. !
DISCIPLINE 3IGNATUEZ _ / DATE Safety Evaluator: Me w uscAt_ h hl MMr, / 2.C,. % 1 l 10CTR50.59 PROGPJ.M MANUAL REVISICN 1 0 AI-109 Rev. 000 Page 74 of 82 l
I EER Mo. cli-0039 ATTACHMENT 2 (Cont'd) R e v. N o. - O l 7acye. No. 10 i l L ATTACEMENT A CP&L SATETT REVIEW Page L of 8 FART IV: UNREVIEhTD SATETY OUESTICN DETERMINATION DOCUMENT NO. EER 91-OA*M4 REV. NO. O l Using the SATETY ANALYSIS developed for the change, test or experiment, as well as other required references (LICENSING EASIS DOCUMENTATICN, Oasign Drawings, Design Basis Documents, codes, etc.), the preparer of the SATETY E7ALUATICN must directly answer each of the fc11cwing seven questicas and make a deter =1 nation of whether an UNREVIEh'ID SATETY CUESTICN exists .
- A WRITTEN BASIS IS REQUIRID TCR EACE ANSWER Yes No
- 1. May the preposed activity increase the [] M probability of occurrence of an accident '
evaluated previously in the SAFETY ANALYSIS REPORT? HEE ATTAcidD
- l l 2. May the proposed activity increase the consequences of an accident evaluated
[] M ! l previously in the SATITY ANALYSIS REPORT? SEE ATTAcurs t
- 3. May the proposed activity increase the [] pg probability of occurrence of a =alfuncticn of equip =ent i=po rtant to safety evaluated-previously in the SATETY ANALYSIS REPORT?
.sFt: AT%mED l
4 May the proposed activity increase the [] M consequence of a =alfunction of equipment important to safety evaluated previously in the SATETY ANALYSIS REPORT? M ATrACHEb i
- 5. May the preposed activity create the [] R possibility of an accident of a different type
[ than any evaluated previously in the SATETY l ANALYSIS RI; PORT? SEM' ATfACHEn i 10CFR50.59 PROGRAM MANUAL - 58 REVISION 1 l 0 AI-109 Rev. 000 Page 75 of 82
EER. No. 91-C0391 ! Re.v. Wo. O ! ATTACHMENT 2 (Cont'd) hg Wo, loj ; , il p : ATTACEMENT A CPEL SAFETY REVIEW Page 7 ef 8 ras g 7
- 6. May the proposed activity create the possibility of a malfunction of aquipment [] g i=portant to safety of a diffarant type than any evaluated previcusly in the SAFETT -
ANALYSIS REPORT? N A r ra euG !
- 7. Does the proposed activity reduce the margin b of safety as defined in the basis of any [] g !
Technical Specification? , SFE AM f H C9 ' Based en the answers to questiens 1 - 7, does this [] itam result in an UNPr/IEWED SAFETT CUESTICN? If
)(
the answer to any of the questions 1-7 is "Yes", ; than the itam is considered to constitute an UNPf/IEWED SAFETY QUESTICN. If, in answering questien 1 or 3, it was determined that the prebability did in fact increase, but the increase was small relative to the uncertainties or, in answering question 2 or 4, i it was determi=ad that the consequences increased, but the i i consequences vara still less than the NRC ACCEPTANCE LIMIT; cr, in answering questien 7, a paramatar would be closer to the NRC I ACCEPTANCE LIMIT, but the and result was still vs. thin the NRC , 4 ACCEPTANCE LIMIT than PNSC review is requirad. j l PNSC REVIEW REQUIRED FOR ABOVE REASCN(S) ? [] j{ { RETERENCES: T5 3.4.~7.1 'Z ; TsT 90 -03 ew. O . FSKit. Nr u +s 9 & W : hr e Cn o o s oA - io Xe -12 'Sw R4 n u t .c_ Am ri s vzveer: I PT ?4 A A " ?T ~24. C 4; SP 41 - 0 0 6 " l DISCIPLINE SIGNATUPJ _ / DATE Safety Evaluater: prtx N a h, -iz2 A Miph /249e Cther QUALITIED (/ '
/ l SAFETI REVIEWERS (as appropriata) / I
/ }
Additicnal Sheets Attached? Yes No 10CTR50.59 PROGRAM MANUAL REVISICN 1 0 AI-109 Rev. 000 Page M of M
i EER T4o. 91-0039 l
'Rev. No. o Page kJ o. 20 ATTACEMENT A Page 8 of 8 ;
CP&L BAFETY REVIEW PART IV: UNREVIEWED SAFETY QUESTION DETERMINATION (Cont'd.) FOR EER 91-0039 i
- 1. The data analysis and system evaluation performed by l EER 91-0039 will not increase the probability of occurrence '
of a previously evaluated accident in the FSAR. The EER only serves to evaluate the Service Water system's capability to perform its design basis duties during an accident; no physical work, documentation changes, or action items result from this EER. Thus, this EER has no impact on any previously analyzed accident occurrence probability. '
- 2. This EER does not increase the consequences of a previously FSAR-evaluated accident. As stated above, this EER only analyzes data taken during the performance of previously approved procedures, and has no bearing whatsoever on ,
presiously analyzed accident consequences. -
- 3. The probability of occurrence of a previously evaluated malfunction of safety-related equipment does not change 1 because of this EER. This EER only evaluates an existing i system for its design basis capability; equipment malfunctions are not affected.
- 4. The consequences of safety-related equipment malfunction will not change from that which has been already analyzed.
This EER only analyzed system capability; it has no impact upon previously performed equipment malfunction studies.
- 5. No new accident scenario is being introduced by this EER.
Previously analyzed accident scenarios were re-analyzed I under this EER for the existing system which had undergone modification during the recent cutage; no concerns were raised from these analysis results, and no new accident scenarios were discovered in this EER.
- 6. No new safety-related equipment malfunction possibility is raised by this EER. This EER re-evaluates the previously l analyzed accidents and equipment failures, but does not !
introduce any new equipment failures beyond those previously studied.
- 7. This EER does not reduce the margins of safety given in the i
Technical Specifications: on the contrary, it affirms that l the existing margins of safety still apply. This EER ) analyzed the recently-modified SW system using the existing accident scenarios coincident with the previously studied equipment single failures and found that the system remains capable of performing its design basis functions. 1 I l i
EER No. 91-co7A i Ro. tao . o ! Ag A. 21 l -e ., EER No. 91-00 39 Rev. No. O FORM 3 ENGINEERING EVALUATION REPORT ENVIRONMENTAL QUALIFICATION IMPACT FORM (EER-EQ1F) [ Will the evaluation, on either a temporary or permanent basis: {
- 1. Justify the deletion of equipment / common components from the BSEP EQ progam? ,
O re= 9 No !
- 2. Justify the addition of (already existing) equipment / common components to the ESEP EQ program?
O res 8 No
- 3. Authorize the repair of EQ equipment / common components with other than qualified like-in-kind equipment / component parts?
O res E so i 4 Affect the existing installation or interface (of EQ equipment / common , component applications) as may be designated in EDBS and/or in the ' qualification data package (including changing the type of interf ace / ! l installation)? O re= E so l S. Justify the (quality class) upgrade of equipment /co= mon components or - l l component parts which could be utilized in EQ applications? Yes @ No l 6. (Re) Define qualification parameters (e.g., normal or LOCA/EELB environ-mental conditions, postaccident operating time requirements, essential passive / active postaccident operating requirements, qualified life l assumptions /results, etc.) for specific EQ equipment? C Yes @ No
- 7. Provide an EQ-related justification for continued operation (as required l per PLP-02, Section 4.4.3.3 or 4.4.4)?
i l O res E no l l 8. Provide the resolution of a qualification problem (as required per l PLP-02, Section 4.4.4)? j l [_] Yes I l @ No l NOTES: 1. If all no, then no further EQ consideration is required. Mark
- the EER Traveler accordingly as required by ENP-12 and include l this completed EER-EQlf within the EER package. An EQ l Technical Review is not required.
- 2. If any yes, an EQ impact assessment (per Section 5.3) must be performed during the evaluation process. Mark the EER Traveler l accordingly and include this completed EER-EQIF within the EER i package. An EQ technical review is required.
l ! BSEP/Vol. II/ENP-34.1 20 Rev. 4 i
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DATA SIIEET 3 DIESEL. GENERATORS SERVICE WATER FLOWS DIESEL DIESEL GENERATOR #1 GiNERATOR #2 STEP NO. JACKET WATER JACKET WATER COOLER SW COOLER SW Ft.0W FI.0W , 9.3.29 _ 131 % 14'27__ 9.3.33 h00 1426 ' 9.3.42 130 0 1:sq 2. , a> Td smW
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_ . . _._ . ._, .. - _ . , _ . __ m . i.' Ilt!'T 1 1-PT-24.6.4 . DATA SilEET 4 SEltVICE WATER DUII.DillG P.SW NSW NSW HSW CONV NilC Pi1P N N N l'flP D l'f tP A NSW - llDR llDR PRESS PflP A
' DISCII DISCil DISCII DISCII NC 1U b7 N 4 PUMP I.Ne T Utd ' LUBE PRESS TEST -PRESS PBESS SIRN STRH 3
STEP *lA if WATER TEST PI- PI- AP AP T ' NO. Fl.0W P d FL0W t4" CAUCE CAUCE
#2 144 145 PDIC l'DIC '.
*3 6" U3 E2
#1 -138 -140
' I'M # IS' 57 9b 1.5 2.0 Go 94 kp64.o 4bOl.2f] J2&i'r' 57.4- Gl Z -
l 9.3.29 9.3.33 1567.0 4640 124,o $b.(o 59. 4 59 % l . 4- 20 60 .M W$0 AfllU.o I27.0 *l0.h_ $b.O $k % l.& 2. 2 2/ bo 9.3.42 Mr
'h @-l4:M - /1548 Test Cauge il Data:
0-I b pst instatica Ei.: M M-0" CP&L Ho, b b f I 'I N Range: # CalDate*j'2' Cal. Duc Date: l /2b / h[ Teat Cauge #2 Data:
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} c. t.4 9.3.42 il1fl. Y ll. Q [( Ig. n? C 6. 0 VJJ Y5 lY 'l l o f, / O R 0 l, ll i l Test'Cauge #3 Data:
CP&L No. 5 ~/7I Range: O'2_00 Installed El.: 1 Cal Date: /7;/27 !# 7C Cal. Due Date: //2/ /7/ Test Gauge #4 Data: > CP&L No. S ~/77 Range: O'200 Installed El.: 'Il f' . y Cal Date: /// v/~r/ Cal. Due Date: 2 /# / S' $kZJ Oj0 y 2 W -t n o, e W
>V n 1-PT-24.6.4 Rev. O Page 79 of 80
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EER No. 91-0039 'I Rev. No. O ! ATTACHMENT C: UICALEN2 RESULTS FILE Page No. 1 . f l- ! L i t FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIC IE THE DARCY WEISBACH HEAD LOSS EQUATION IS USED, THE KINEMATIC VIS. = .0000070 THE SPECIFIC GRAVITY OF THIS LIQUID = 1.03 a l' A SUCCESSFUL CE0 METRIC VERIFICATION HAS BEEN COMPLETED f 4 OUTPUT SELECTION: THE FOLLOWING RESULTS ARE OUTPUT ', RESULTS ARE OUTPUT FOR.ALL PIPES WITH PUMPS - CLOSED PIPES ARE NOTED l l RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 1 4 16 31- 34 38 41'.47' 50 57 _62- : 72 73 74 79 88 92- 97 101 105 . I RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 109 116 120 128 134 146 152 166 1741179 185 i 197 198 205 213 218 224 233 234 235 " RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 501 503 600 '! RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES : 1 2 14 15 16 27' 28 36 37 i 49 50 66 70 74 75 ' RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES . 90 91 100 101 109 110 143 144'156 j 157 18 23 i l THIS SYSTEM HAS 243 PIPES _WITH 212 JUNCTIONS , 27 LOOPS AND 5 FCNS ; 1 I THE RESULTS ARE OBTAINED AFTER 5 TRIALS WITH AN ACCURACY = .00242 l UICALEN2 CHANGE 0:MODEL ATTEMPTS TO MIMIC 1-PT-24.6.4 STEP 9.3.29; INCLUDES PIPE 'i ROUGHNESS &_ID CHANGES FROM PM 82-222A AND NEW l.EAKAGE LINE ML (ASSUMES 448 GPM'
@ 34.2- PSID BETWEEN CSWH & NSWH)
PIPE NO. NODE NOS. 4 FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 l 1 0 1 5392.54 .02 154.04 .00 7.96- 19.69 ! 4 0 4 5330.81'
.02 155.10 .00 7.87' 19.24 16 12 13 131.00 .51 .28 4.29 l 31
.00. 44.90 27 28 66.16 .04 -. 00 45.02 5.02 -42.22' 34 304 305 505.56 .82 .001 2.61 38 14.15 169.80 36 37 103.14 .10 .00 32.34 7.83 99.14:
41 38 39 101.48 .10- .00 31.31 7.70 47 42
.96.08- 1 41 103.09 .10 .00 32.31 7.82 99.04 50 43 44 101.15 .10 .00 31.10 7.68 57 49
. 95.47 50 14.34 .20 .00 12.55 6.36- 200.64 62 53 54 . 16.20 .25 .00 6.40 7.18 253.51' 72 59 62- 1151.04 .00 .00 1.63 2.20 73 60
.93 63 1117.30 .00 .00 1.54 2.13 .88
-74 61 64 1131.66 .00 .00 1.58 2.16 LINE 79 IS CLOSED
.90 88 74 75 118.78 .13 .00 15.14 9.01 130.32 I
-1
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. . _ _ - . ._- _. . _ _ ~!
1 EER No. 41-0039 Rev. No. O ATTACHMENT C: UICALEN2 RESULTS FILE Page No. 2 i 92 76 77 120.51 .13 .00 15.58 9.15 97 134.01 81 82 122.02 .14 .00 15.98 9.26 137.28 101 83 84 117.78 .13 .00 14.89 8.94 128.19 105 88 68 603.88 1.81 .00 7.24 6.69 22.54 109 90 91 16.73 .27 .00 .85 7.42 116 269.84 96 97 16.69 .27 .00 2.55 7.40 268.70 120 100 101 91.36 .08 .00 2.99 6.93 128 78.44 109 110 1402.42 .04 .00 14.65 10.24 39.87 134 115 116 1340.97 .04 .00 2.98 9.79 36.54 LINE 146 IS CLOSED LINE 152 IS CLOSED LINE 166 IS CLOSED LINE 174 IS CLOSED LINE 179 IS CLOSED LINE 185 IS CLOSED 197 170 171 .00 .00 .00 .00 .00 198 302
.00 165 .00 .00 .00 .00 .00 .00 205 177 178 1498.63 .03 749.29 .00 9.61 213 185 32.61 186 1501.37 .03 749.19 .00 9.63 32.73 218 189 190 66.98 9.68 .00 5.11 13.96 572.79 224 195 196 67.29 9.48 .00 5.16 14.02 233 577.99 203 204 3000.00 .01 .00 .00 3.27 4.69 LINE 234 IS CLOSED 235 70 205 3400.00 .00 .00 .27 5.97 501 5.96 86 301 479.10 .03 .00 65.70 5.31 14.44 503 46 303 408.86 .06 .00 68.03 4.53 600 10.66 17 0 205.26 .00 .00 16.12 .24 .02 JUNCTICS NUMEER DEMAND GRADE LINE ELEVATICN PRESSURE 1 .00 176.02 43.10 59.33 2 .00 171.81 42.40 57.76 14 .00 169.82 26.50 63.97 15 .00 171.20 26.50 64.59 16 .00 171.20 26.50 64.59 18 .00 167.18 36.30 38.42 23 .00 158.24 12.50 65.05 27 .00 144.83 11.00 59.73 28 .00 99.77 10.80 39.71 36 .00 155.27 17.50 61.49 37 .00 122.83 17.50 47.01 49 .00 147.76 8.30 62.24 50 .00 135.01 8.30 56.55 66 3400.00 161.12 77.20 37.45 70 -3400.00 42.67 74.10 14.03 74 .00 148.97 17.50 58.68 75 .00 133.70 17.50 51.86 90 .00 137.53 31.60 47.28 91 .00 136.40 31.60 46.78 100 .00 130.10 11.40 52.98 101 .00 127.03 28.50 43.98 109 .00 100.43 44.40 25.01 110 .00 85.75 44.40 18.45 143 .00 166.84 72.80 41.97 144 156
.00
.00 40.40 166.81 74.20 72.80
-15.09 41.96 I
'i l
.b EER No. 01-0039 -!
Rev. No.- 0 , ATTACHMENT C: UICALEN2 RESULTS FILE Page No. 3 i i
.i
.00 40.40 157 74.20 -15.09 .
THE NET. SYSTEM DEMAND.= 131.00
SUMMARY
OF-INFLOWS (+).AND OUTFLOWS (-) FROM FIXED CRADE NODES i
.i PIPE NUMBER FLOWRATE '
I 1 5392.54 i 4 5330.81 158 -2743.39 ! 161 -7643.71 ! 600 -205.26 , i THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 10723.36 ' THE NET FLOW OUT OF THE SYSTEM INTO FIXED CRADE NODES = -10592.36 l f 1 e
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EER No. 01-0039 j Rev. No. 0 , ATTACHMENT C: UICALBN2 RESULTS FILE Page No. 4 : j i A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS i THE FOLLOWING SPECIFIC DEMAND CHANCES ARE MADE : ! JUNCTION NUMBER DEMAND ! 13 124.00 -! 66 3300.00 70 -3300.00 204 .00 ! 205 .00 i 302 3000.00 165 -3000.00 LINE 166 IS OPEN LINE 174 IS OPEN LINE 179 IS OPEN _* LINE 185 IS OPEN LINE 198 IS CLOSED LINE 205 IS CLOSED ; LINE 213 IS CLOSED , LINE 218 IS CLOSED LINE 224 IS CLOSED LINE 234 IS OPEN , THE FOLLOWING CHANCES IN PIPE DATA ARE SPECIFIED : FOR PIPE NUMBER 1 THE VALUE OF THE FIXED CRADE IS CHANGED TO 19.8 FOR PIPE NUMBER 4 THE VALUE OF THE FIXED CRADE IS CHANCED TO 19.8 i FOR PIPE NUMBER 600 THE VALUE OF THE FIXED CRADE IS CHANCED TO 153.3 l PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED CRADE .i 2 1 2 9.7 16.6 5.0 3.97 .00 ! 5 4 5 9.7 16.6 5.0 5.40 .00 ! THE RESULTS ARE OBTAINED AFTER 5 TRIALS WITH AN ACCURACY = .00353 i UICALBN2 CHANGE 1:FT-24.6.4 STEP 9.3.33 : I
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PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 .* I O 1 5329.08 .02 .155.13 .00 7.87 19.23 l 4 0 4 5259.77 .02 156.30 .00 7.77 18.73 i 16 12 13 124.00 .45 .00 . .25 4.06 40.25 i 31 27 28 65.68 .04 .00 44.36 4.98 41.63 ; 34 304 305 501.85 .80 .00 2.57. 14.05 167.36 ; 38 36 37 102.38 .10 .00 31.87 7.77 97.74 i 41 38 39 100.74 .09 .00 30.85 7.65 94.73 ! 47 41' 42 102.33. .10 .00 31.84 7.77 97.64
- 30 43 44 100.40 09. .00 30.65 7.62 94.12 i 57 49 50 14.24 .20 .00 12.36 6.31 197.82 !
62: 53 54 16.08 .25 .00 6.31 7.13 249.94 , i
EER No. 91-0039 ATTACHMENT C: UICALBN2 RESULTS FILE Rev. No. O Page~No. S 72 59 62 1117.18 .00 .00 1.54 73 2.13 .88 60 63 1084.43= .00 .00 1.45 2.07 .83 74 61 64 1098.39 .00 .00- 1.49 LINE 2.10 .85-79 IS CLOSED 88 74 75 118.53 .13 .00 15.08 9.00 92 129.77 76 77 120.25 .13 .00 15.52 9.13 133.45 97 81 82 121.75 .14 .00 15.91 101 9.24 136.71 83 84 117.53 . 13 .00 14.82 8.92 127.66 105 88 68 602.57 1.80 .00 7.21 6.68. 22.44 109 90 91 16.69 .27 .00 .85 7.40 116 268.72 96 97 16.66 .27 .00 -2.54 7.38 267.58 120 100 101 91.16 .08 .00 2 97 6.92 128 1398.26 78.12 109 110 .04 .00 14.56 10.21 39.64 134 115 116 1336.99 .04 .00 2.96 9.76 36.33 LINE 146 IS CLOSED LINE 152 IS CLOSED 166 143 144 1501.69 .03 749.18 .00 174 9.63' 32.74 156 157 1498.31 .03 749.30 .00 9.61 32.60 179 148 149 64.74 9.22 .00 4.78 .13.49 185 160 58.01 535.94 161 7.44 .00 3.84 12.09 432.69 197 170 171 3000.00 .02 .00 .21 5.27 4.69 LINE 198 IS CLOSED LINE 205 IS CL0cnD LINE 213 IS CLOSED LINE 218 IS CLOSED LINE 224 IS CLOSED . 233 203 204 .00 .00 '!
.00 .00 .00 .00 234- 204 205 .00 .00 .00 .00 l 235
.00 .00 1 70 205 3300.00 .00 .00 .25 5.80 5.63 501 86 301 478.06 .03 .00 65.42 5.30 14.38 503 46 303 405.86 .06 .00 67.03 4.50 10.51-600 17 0 202.43 .00 .00 15.68 .24 i
.02 '
JUNCTION NUMBER DEMAND CRADE LINE ELEVATION FRESSURE 1 .00 174.91 43.10- 58.83 2 .00 170.90 42.40 -57.36 14 .00 168.96 26.50 63.58 15 .00 168.96 26.50- 63.58 16 .00 168.96 26.50 63.58 18 .00 166.39 36.30 58.07 23 .00 157.54 12.50 64.73 27 .00 144.31 11.00 59.50 28- .00 99.91 10.80 39.77 36 .00 154.60 17.50 61.19 37 .00 122.64 17.50 46.93 49 .00 147 20 8.30 62.00 50 .00 134.64 8.30 56.39 66 3300.00 160.67 77.20 37.26 70 -3300.00 41.16 74.10 -14.70 74 .00 -148.30 17.50 58.38 75 .00 133.09 17.50 51.59 90 .00 136.90 31.60 47.00 91 .00 135.79 31.60 46.50 100 .00 129.50 11.40 52.71 101 .00 126.45 28.50 43.72
. . . _ _ . . ~...
e o a l~ ! q EER No. 91-0039 ATTACHMENT C: UICALEN2 RESULTS FILE Rev. No. 0 Page No. 6 .! i. I 1 109 . 00 100.01 44.40 24.82 ! 110 . 00 85.41 44.40' 18.30- ; 143 . 00 165.26 72.80- 41.27 144 . 00 914.41 74.20 375.01 r 156 .00 165.24 72.80 41.26 ' 157 . 00 914.50 7.4 20 375.06 l THE NET SYSTEM DEMAND = 124.00
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES I PIPE NUMBER FLOWRATE L 1 5329.08 l' 4 5259.77 '; 158 -2735.26 l 161 -7527.18 600 -202.43 i THE NET FLOW INTO THE SYSTEM FROM FIXED CRADE NODES = 10588.86 ! l .THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -10464.86 l i
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I i i I EER No. 91-0039- i Rev. No. 0 ATTACHMENT C: UICALEN2 RESULTS FILE Page No. 7 f 1 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS , i THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : JUNCTION NUMBER DEMAND 1 66 3300.00 '; 70 -3300.00 ' 13 127.00 302 3000.00 165 -3000.00 l 204 .00 ' 205 .00 THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED I FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANCED TO 18.7 FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANGED TO 18.7 f FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 79.8 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE l 2 1 2 9.7 16.6 5.0 3.84 .00 ! 5 4 5 9.7 16.6 5.0 5.67 .00 l [ THE RESULTS ARE OBTAINED AFTER 3 TRIALS WITH AN ACCURACY = .00092 i t UICALEN2 CHANGE 2:PT-24.6.4 STEP 9.3.42 ' i l PIPE NO. NODE NOS. ~ FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 l 1 0 1 5449.34 .02 153.06 .00 8.05 20.10 : 4 0 4 5358.71 .02 154.62 .00 7.91 19.44 ! 16 12 13 127.00 .48 .00 .27 4.16 42.21 l 31 27 28 64.81 .04 .00 43,19 4.92 40.58 ; 34 304 305 495.20 .78 .00 2.51 13.86 163.05 l 38 36 37 101.03 .10 .00 31.03 7.67- 95.26 ! 41 38 39 99.40 .09 .00 30.04 7.54- 92.32 ' 47 41 42 100.98 .10 .00 31.00 7.66 95.16 50 43 44 99.07 .09 .00 29.84 7.52 91.73 ; 57 49 50 14.05 .19 .00 12.04 6.23 192.82 62 53 54 15.86 .24 .00 6.14 7.03 243.59 i 72 59 62 1117.18 .00 .00 1.54 2.13 .88 .i 73 60 63 1084.43 .00 .00 1.45 2.07 .83 i 74 61 64 1098.39 .00 .00 1.49 2.10 .85 ! LINE 79 IS CLOSED i 88 74 75 116.96 .13 .00 14.68 8.88 126.47 i 92 76 77 118.66 .13 .00 15.11 9.01 130.05 ! 97 81 82 120.15 .13 .00 15.49 9.12 133.23 i 101 83 84 115.98 .12 .00 14.43 8.80 124.41 105 88 68 594.61 1.75 .00 7.02 6.59 21.88 109 90 91 16.47 .26 .00 .83 7.30 261.90 - P 1 l
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-t EER No.. 91-0039 ATTACHMENT C: UICALBN2 RESULTS FILE Rev. No.
Page No. 0 8-l ( { 116 96 97 16.44 . 26 .00 2.47 '7.29 260.79
.120 100 101 89.96 .08 .00 2.89 6.83 76.14 -
128 109 110 1381.51 . 04 .00 14.21 10.09 38.72 ! 134 115 116 1320.97 . 04 .00 2.89 9.64 35.49 LINE 146 IS CLOSED : LINE 152 IS CLOSED .; 166 143 144 1501.70 .03 749.18 .00 9.63 32.74 l 174 156 157 1498.30 ;03 749.30 .00 9.61 32.60 -i 179 148 149 57.88 7.41 .00 3.82 12.06 430.68 ! 185 160 161 56.73 7.12 .00 3.67 11.82 414.24. ! 197 170 171 3000.00 .02 .00 .21 -5.27 4.69' i LINE 198 IS CLOSED : LINE 205 IS CLOSED LINE 213 IS CLOSED LINE 218 IS CLOSED l LINE 224 IS CLOSED ' 233 203 204 .00 . 00 .00 .00 .00 .00- ! 234 204 205 .00 .00 .00 .00 .00 .00 J 235 70 205 3300.00 . 00 .00 25 5.80 5.63 501 86 301 471.75 . 03 .00 63.70' 5.23 14.02 ; 503 46 303 400.48 . 06 .00 65.27 4.44 10.24 ; 600 17 0 474.16 . 00 .00 86 03 .56 .09 JUNCTION NUMBER DEMAND CRADE LINE ELEVATION PRESSURE 1 .00 171.74 43.10 57.41 l j 2 .00 167.68 42.40 55.92 14 .00 165.64 26.50 62.10 15 .00 165.83 } 26.50 62.19 i 16 00 165.83 26.50 62.19 l 18 .00 163.10 36.30 56.60 l 23 .00 154.48 12.50 63.37 ,j 27 .00 141.59 11.00 58.29 .i 28 .00 98.37 10.80 39.08 36 .00 151.62 17.50 59.86 37 .00 120.49 17.50 45.97 49 .00 144.41 8.30 60.75 50 .00. 132.18 8.30 55.29 66 3300.00 157.38 77.20 35.79 70 -3300.00 41.16 74.10 -14.70 74 .00 145.48 17.50 57.12 75 .00 130.67 17.50 50.51 90 .00 134.38 31.60 45.87 91 .00 133.29 31.60 45.39-100 .00- 127.17 11.40 51.67 101 .00 124.20 28.50 '42.71 109 .00 98.32 44.40 24.07 110 .00 84.07 44.40 17.70 143 .00 161.97 72.80 39.80 144 .00 911.12 74.20 373.55 156 .00 161.95: 72.80 39.79 157 .00 911.22 74.20 373.59 THE NET SYSTEM DEMAND = 127.00
SUMMARY
0F INFLOWS (+) AND OUTFLOWS (-) FROM FIXED CRADE NODES
i h N EER No. 91-0039 ; Rev. No. 0 ATTACHMENT C: UICALEN2'RESULTS FILE Page No. 9 i PIPE NUMBER FLOWRATE ! 1 5449.34 !
.4 5358.71 -
158 -2702.48 161 -7504.42 , 600 -474.16 t THE NET FLOW INTO THE SYSTEM FROM FIXED CRADE NODES = 10808.05 . THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -10681.05 I i i t i f k i i l -i i 6
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l .. i l-1. i EER No. 91-0039 ! Rev. No. O ;
. ATTACHMENT D: UICALEN2 INPUT DATA FILE Page No. 1
( L i I i 4 FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIG i A
SUMMARY
OF THE ORIGINAL DATA FOLLOWS l THE DARCY WEISEACH HEAD LOSS EQUATION IS USED. THE KINEMATIC VIS. = .0000070 THE SPECIFIC GRAVITY OF THIS LIQUID = 1.03 [ PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE '! l (FEET) (INCHES) : 1 0 1 1.0 16.6 5.0 .00 22.00 , LINE 1 PUMP DATA (HEAD-FLOW): 200.0 .0 135.0 6400.0 90.0 8300.0 i 2 1 2 9.7 16.6 5.0 4.08 3 2 3 15.9 18.6 5.0 2.91 4 0 4 1.0 16.6 5.0 . ,00 22.00 , LINE 4 PUMP DATA (HEAD-FLOW): 200.0 .0 135.0 6400.0 90.0 8300.0 ' 5 4 5 9.7 16.6 5.0 5.34 ! ! 6 5 6 15.9 18.6 5.0 2.91 l- 7 3 6 6.0 28.5- 5.0 .06 ; 8 6 7 6.0 28.5 5.0 .06 , 9 7 8 308.8 28.5 5.0 .48 ! 10 8 18 371.0 28.5 5.0 .84 11 8 9 2.7 16.6 5.0 .33 l
- i. 12 9 10 63.7 17.3 .2 .60 >
l 13 10 103 124.3 16.6 5.0 .52
^
14 7 11 1.4 3.5 5.0 .71 15 11 12 3.8 3.5 5.0 3.69 { 16 12- 13 11.3 3.5 5.0 .99 !
-17 14 3 7.0 28.5 5.0 .06 :
18 15 14 6.1 28.5 5.0 .06 > 19 16 15 7. 0 28.5 5.0 .06 i 20 17 16 2.3 28.5 .5.0 .00 t 21 306 19 2.3 29.3 .2 .07 ! 22 19 21 9.1 22.5 5.0 .79 l 23 19 20 11.4 29.3 .2 1.49 e 24 20 55 24.1 19.3 .2 .68 25 18 22 28.1 6.1 .2 l 2.76 .t 26 22 23 15.5- 6.1 .2 30 .l 27 23 24 6.5- 6.1 .2 .18 t 28 24 25 111.6 6.1 .2 2.63 ! 29 25 26 67.3 3.8- .2 .22 I 30 26 27 40.8 1.7 .2 3.46 ' 31 27 28 1.0 2.3 .2 115.00 32 28 29' 31.5 1.7 .2 33.18 33 29 30 1.2 3.8 .2 17.02 34 304 305 4.8 3.8 .2 .84
- l. 35 23 32 13.1 6.1 .2 .81
m: ! I i j EER No. 91-0039 Rev. No. O i 1. ATTACHMENT D: UICALEN2 INPUT DATA FII.E Page No.' 2 36- 33 34 1.3 3.0 .2 .54 37 34 36 8.2 2.3 .2 .74 ! 38 36 37 1.0 2.3 .2 34.00 j 39 37 40 7.0 2.3 .2 1.13 + 40 34 38 7.2 2.3 .2 1.17 38 1.0 2.3-41 39 .2 34.00 1 42 39 40 7.1 2.3 .2 2.03 . 43 40 '45 5.0 3.0 .2 .69 ! 44 32 33 5.0 6.1 .2 .48 ' 45 33 35 2.8 3.0 .2 .79 46 35 41 9.2 2.3 .2 . .74 t 47 41 42 1.0 2.3 .2 34.00 48 l 42 45 7.0 2.3 .2 2.06 ' 49 35 43 7.9 2.3 .2 1.76 , 50 43 44 1.0 2.3 .2 34.00 31 44 46 8.0 2.3 .2 2.60 : 52 45 46 1.5 6.1 .2 .22 53 303 47 20.8 6.1 .2 .93 ' 54 47 30 200.0 6.1 .2 3.33 55 24 48 3.5 1.4 .2 .85 ' 56 48 49 11.0 1.0 .2 11.64 : 57 49 50 1.0 1.0 .2 20.00 1 58 50 51 17.2 1.0 .2 125.00 ! 59 51 52 1.1 1.4 .2 .,90 ! 60 52 47 2.9 1.4 .2 1.73 1 61 48 53 19.0 1.0 .2 12.94 ; 62 53 54 1.0 1.0 .2 8.00 : 63 54 51 9.0 1.0 .2 100.00 ' 64 31 139 47.4 18.6 5.0 .08 65 22 71 125.1 6.1 .2- 3.02 66 55 56 104.2 18.6 5.0 12.71 - 67 56 57 14.9 18.6 5.0 .60 ; 68 57 58 5.0 18.6 5.0 30 69 57 59 16.1 14.6 5.0 .67 - 70 58' 60 16.1 12.6 5.0 .47 71 58 61 18.3 14.6 5.0 1.02 72 59 62 1.0 14.6 .2 21.80 73 -60 63 1.0 14.6 .2 21.80
- 74. 61 64 1.0 14.6 .2 21.80 ,
75- 62 65 12.5 15.3 .2 .51 76 10.9 13.3 l 63 65 .2 .37
- 77. 64 66 13.3 15.3 .2 .87 t 78 65 66 5.7 15.3 .2 .08 ;
79 66 70 29.5 15.3 .2 17.59 : l- LINE 79 IS CLOSED ! l .80 205 69 9.3 15.3 .2 .62 ' i 81 69 68 30.2 28.5 5.0 1.82 ! 82 68 137 36.9 28.5 5.0 .04' , 83 71 98 51.2 6.1 .2 2.85 : 84 98 67. 2.9 6.1 .2 .63 ' 85 71 72- 8.2 6.1 .2 .36 86 72 300 37.1 6.1 .2 1.17- l 87 73 74 9.8 2.3 .2 1.35 i 88 74 75 1.0 2.3 .2 12.00 ' 89 75 78 7.2- 2.3 .2 1.76 90 73 79 .9 6.1 .2 .12 91- 79 76 8.5 2.3 .2 1.08 i
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I ! 5 EER No. 91-0039 . Rev. No. 0 : ATTACIIMENT D: UICALEN2 INPUT DATA FILE P&ge No. 3 R i k 92 76 77 1.0 2.3 .2 12.00 i 93 77 78 8.6 2.3 .2 1.51 i 94 78 85 4.7 3.0 .2 .57 ! 95 79 80 1.2 3.0 .2 1.13 i 96 80 81 9.1 2.3 .2 1.01 : 97 81 82 1.0 2.3 .2 -12.00
- 98 82- 85 7.5 2.3 .2 .81- ;
99 85 86 4.2 6.1 .2 .42 : 100 80 83 9.2 2.3 .2 1.35 ! 101 83 84 1.0 2.3 .2 12.00 i 102 84 86 8.4 2.3 .2 1.62 i 103 301 87 27.5 6.1 .2 1.17 ; 104 87 88 606.1 6.1 ,2 4.82 105 88 68 80.2 6.1 .2 10.40 106 72 102 12.5 1.7 .2 .60 l 107 102 89 2.9 1.4 .2 .73 ' 108 89 90 13.0 1.0 .2 12.28 109 90 91 1.0 1.0 .2 1.00 110 91 92 24.0 1.0 .2 75.00 111 92 93 .9 1.4 .2 .22 112 93 94 2.9 1.4 .2 1.35 ! 113 94 95 18.7 1.7 .2 1.20 114 95 87 .9 1.7 .2 1.67 115 89 96 20.3 1.0 .2 12.46 ' 116 96 97 1.0 1.0 .2 3.00 117 97 92 11.2 1.0
.2 75.00 !
118 98 99 101.9 3.8 ,2 1.46 119 99 100 35.0 1.7 .2 3.57 ' 120 100 101 1.0 2.3 .2 4.00 121 101 88 34.5 2.3 .2 100.00 ! 122 120 104 31.0 16.6 5.0 .89- ! 123 104 105 5.4 16.6 5.0 .89 . 124 105 106 .8 16.6 5.0 .00 > 125~ 104 107 56.3 5.6 5.0 4.01 ! 126 107 108 12.7 5.6 5.0 .73 127 108 109 1.9 7.5 5.0' .76 128 109 110 1.0 7.5 .2 9.00 , 129 110 111 1.9 75 5.0 .98 130 111 112 79.0- 5.6 5.0 3.28 ; 131 105 113 79.8 5.6 5.0 4.34 ) 132 113 114 12.0 5.6 5.0 ,73 I 133 114 115 1.9 7.5 5.0- .76 ! 134 115 116 1.0 7.5 .2 2.00- t 135 116 117 1.9 7.5 5.0 .98 I 136 11'7 118 100.4 5.6 5.0 3.61 ; 137 119 118 .8 16.6 5.0 .00 1 138 118 112 .8 16.6 5.0 .07- l 139 112 136 26.8 16.6 5.0 .45 140 103 120 18.9 16.6 5.0 35.41 141 103 12.0 16.6 l 121 5.0 35.41. i 142 121 122 3.1 5.6 5.0 .00 ! 143 120 123 58.0 5.6' 5.0 4.00 144 123 124 13.7 5.6- 5.0 .73 1 145 124 125 1.7 7.5 5.0 .76 146- 125 126 1.0 8.0 { 2 9.00 LINE- 146 IS CLOSED 147 126 1.27 l.9 7.5 5.0 1.48
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EER No. 91-0030 Rev. No. O ATTACHMENT D: UICALEN2 INPUT DATA FILE Page No. 4 148 127 128 74.8 5.6 5.0 2.68 149 121 129 54.5 5.6 5.0 4.01 150 -129 130 16.3 5.6 5.0 .91 151 130 131 1.7 7.5 5.0 .50 152 131 132 1.0 8.0 .2 9.00 LINE 152 IS CLOSED 153 132 133 1.9 '7.5 5.0 .98 154 133 134 75.7 5.6 5.0 3.28 155 135 134 2.3 16.6 5.0 .00-156 134 128 30.8 16.6 5.0 .07 157 128 136 4.3 16.6 5.0 .45 . 158 136 0 414.1 16.6 5.0 .96 28.90 159 137 138 16.4 28.5 5.0 .92 160 139 138 126.7 18.6 5.0 .64 161 138 0 286.2 34.5 5.0 1.13 40.00 162- 21 140 27.2 22.5 5.0 .20 163 140 141 6.5 12.6 5.0 .34 164 141 142 4.3 12.6 5.0 .12 165 142 143 4.3 8.0 .2 .32 166 143 144 1.0 8.0 .2 .00-LINE 166 PUMP DATA (HEAD-FLOW): 775.0 .0 580.0 4000.0 500.0 4725.0 LINE 166 IS CLOSED 167 144 145 9.9 12.0 .2 3.76 168 145 146 16.7 12.0 .2 .93 169 140 153 16.0 22.5 5.0 .06 170 153 173 21.5 22.5 5.0 .30 171 153 154 6.5 12.6 -5.0 .44 172 154 155 4.3 12.6 5.0 .12 173 155 156 4.3 8.0 .2 .32 174 156 157 1.0 8.0 .2 .00 LINE 174 PUMP DATA (HEAD-FLOW): 775.0 .0 580.0 4000.0 500.0 4725.0 LINE 174 IS CLOSED , 175 157 158 9.8 12.0 .2 3.76 176 158 146 31.4 12.0 .2- 1.07.
-177 141 147 .8 1.7' .2 .20 178 147 148 .5 1.7 .2 .07 179 148 149 17.2 1.4 2 1.69 LINE- 179 IS CLOSED 180 149 150 .7 1.7 .2 26.27
- 81 150 151 2.2 1.4 .2 27.12 182 151 152 19.9 1.4 .2 2.42 183 154 159 .8 1.7 5.0 .69 184 159 160 .5 1.7 .2 .07 185 160 161 17m2 1 -. 4 .2 1.69 LINE 185 IS CLOSED
-186 161 162 1.0 1.7 .2 26.57 187 162 163 2.7 1.4 .2 28.70 188 163 164 19.9 14 .2 2.21 189 193 164 21.2 3.0 .2 .32 190 164 152 16.7 3. 0 .2 .54 191 -152 165 117.8 3.0 .2 4.45 192 146 166 156.0 16.0 .2 1.15 193 166 167 18.7 16.0 .2 .44 194 167 168 10.5 15.3 .2 .14 195 168 169- 2.5 15.3 .2 .00 196 169 170 1.0 19.3 .2 11.50 197 170 171 5.0 15.3 .2 .48
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-k EER No. 01-0039- l Rev. No. O i ATTACHMENT D: UICALEN2 INPUT DATA FILE- Page No. 5 i I
198 302 165 205.0 15.3 .2 410.00 199 165 172 7.5 19.3 .2 .00 ; 200 172 31 31.0 18.6 5.0 .07 - 201 173 174 1.0 12.6 5.0 .00 i 202' 174 175 4.7 13.3 .2 .10 , 203 175 176 4.3 13.3 .2 .12 ' 204 176 177 42 8.0 .2 .32 , 205 177 178 1.0 8.0 .2 .00 - LINE 205 PLMP DATA (HEAD-FLOW): 775.0 .0 580.0 4000.0 500.0 4725.0 l 206 178 179 9.8 12.0 .2 3.76 ; 207 179 180 27.9 12.0 .2 .46 , 208 173 181 16.0 22.5 5.0 .12 209 181 182 .4 12.6 5.0 .00 210 13.3 .2 182 183 4.8 .00 ! 211 183 184 4.4 13.3 .2 .12 212 184 185 4.2 S.0 .2 .32 213 185 186 1.0 8.0 .2 .00 LINE 213 PLHP DATA (HEAD-FLOW): 775.0 .0 580.0 4000.0 500.0 4725.0 i 214 186 187 10.4 12.0 .2 3.76 i 215 187 180 17.4 12.0 .2 .29 1' 216 175 188 1.0 1.7 .2 .49 i 217 188 189 .3 1.4 .2 .07 , 218 189 190 16.9 1.4 .2 1.69 i 219 190 191 1.0 1.7 .2 25.00 l 220 191 192 2.3 1.4 .2 15.00 221 192 193 19.5 1.4 .2 2.44 ; 222 183 194 .4 1.7 .2 .49 223 194 195 .7 1.4 .2 .07 224 195 196 16.4 1.4 .2 1.69 : 225 196 197 1.0 1.7 .2 10.00 - 226 197 198 2.9 1.4 .2 15.00 l 227 198 193 39.2 1.4 .2 5.21 i 228 180 199 212.5 15.3 .2 1.33 1 229 199 200 2.5 15.3 .2 .25 1 230 200 201 2.5 19.3 .2 .00. ; 231 201 202 1.0 19.3 .2 11.50 ) 232 202 203 2.5 19.3 .2 .19 i 233 203 204 2.5 15.3 .2 .00 ! 234 204 205 235.1 15.3 .2 4.09 1 LINE 234 IS CLOSED . 1 235 70 205 .7 15.3 .2 .48 e 500 300 73 . 4.8 6.1 .2 .76 501 86 301 2.3 6.1 .2 150.00 j 502 171 302 4 15.3 .2 .00- 1 503 46 303 5.8 6.1 .2 213.26 l 504 30 304 1.5' 3.8 .2 .00 l 505 305 31 32.9 5.6 5.0 1.94 ! 506 18~ 306 103.8. 28.5 5.0 .08 !
-600 17 0 1.0 18.6 5.0 17794.00 155.08 j A SUCCESSFUL GEOMETRIC VERIFICATION HAS BEEN COMPLETED I l
JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES 1 .00 43.10 1 2 2 .00 42.40 2 3 3 .00 26.50 3 7 17 1
EER No. 01-0039 , Rev. No. 0- , ATTACIDENT D: UICALEN2 INPUT DATA FILE- Page No. 6 i i i 4 .00 43.10 4 5 ~ 42.40 5 .00 5 6 6 .00 26.50 6 7 8 4 7 .00 26.50 8 9 14 8 .00 26.50 9 10 11 ; 9 .00 29.20 11 12 10 .00 31.80 12 13 l 11 .00 24.60 14 15 12 .00 24.60 15 16 13 131.00 24.60 16 14 .00 26.50 17 18 l 15 .00 26.50 18 19 ; 16 .00 26.50 19 20 t 17 .00 26.50 20 600 ! 18 .00 36.30 10 25 506 19 .00 81.50 21 22 23 ? 20 .00 81.50 23 24 l 21 .00 81.50 22 162 j 22 .00 19.10 25 26 65 r 23 .00 12.50 26 27 35 24 .00 12-.50 27 28 55 ) 25 .00 33.80 28 29 ; 26 .00 34.50 29 30 : 27 .00 11.00 30 31 ! 28 .00 10.80 31 32 - 29 .C0 32.30 32 33 ! 30 .00 - 23.20 13 54 504 31 . C:0 35.50 t. 4 200 505 l 32 .00 12.50 35 44 i 33 .00 12.50 36 44 45 i 34 .00 12.50 36 37 14 0 !
.00 12.50 35 45 46 36 .00 17.50 37 38 37 .00 -17.50 38' 39 -
38 .00 17.50 40 41 39 .00 17.50 41 '42 40 .00 14.20 39 42 43 1 41 .00 17-.40 46 47 t 42 .00 17.4' 47 48 43 .00 17.40 49 50 1 44 .00 17.40 =50 51 ! 45 .00 14.20 43 52 1 46 .00 14.20 51 52 503 47 .00 10.80 53 34 60-48 .00 12.50 55 56 61 49 .00 8.30 56 57 50 .00 8.30 57 58 51 .00 10.80 58 59 63 52 .00 10.80 59 60 53 .00 8.30 61 62 54 .00 8.30 62 63 55 .00 81.50 24- 66 56 .00 81.50 66. 67
.57 .00 79.00 67 68 69 58 .00 79.00 68 70 71 59 .00 74.80 69 72 60 .00 74.80 70 73 l l
1 i
EER No. 01-0039 ' Rev. No, 0 ATTACIDENT D: UICALEN2 INPUT DATA FILE Page No.' 7 i 61- .00 74.80 71 74 i 62 .00 74.80 72 75 l 63 .00 74.80 73 76 i 64 .00 74.80 74 77 65 .00 77.20 75 76- 78 66 3400.00 77.20 77 78 79 67 .00' 16.80 84 ; 68 .00 35.50 81 82 105 . 69 .00 65.80 80 81- l' 70 -3400.00 74.10 79 235 71 .00 .10 65 83 85 72 .00 .10 85 86 106- ? 73 .00 16.10 87 90 500 ! 74 .00 17.50 87 88 75 .00- 17.50 88 89 i 76 .00 17.50 91 92 i 77 .00 17.50 92 93 : 78 .00 14.20 89 93 94 : 79 .00 16.10 90 91 95 ! 80 .00 16.10 95 96 100 : 81 .00 17.40 96- 97 ! 82 .00 17.60 97 98 l 83 .00 17.40 100 101 84 .00 17.60 101 102 85 .00 14.20 94 98 99 86 .00 14.20 99 102 301 i 87 .00- 20.90 103 104 114 : 88 .00 33.20 104 105 121 ; 89 .00 14.20 107 .108 115 ! 90 .00 31.60 108 109 i 91 .00 31.60 109 110 l 92 .00 12.10 110 111 117 i 93 .00 12.10 111 112 94 .00 23.00 112 113- > 95 .00 21.00 113 114 i 96 .00 8.30 115 116 ; 97 .00 8.30 116 117 '! 98 .00 16.80 83 84 118 99 .00 34.50 118 119 i 100 .00 11.40 119 120 , 101 .00 28.50 120 121 :
- 102 .00 14.20 106' 107 :
103 .00 34.50 13 140 141 ! 104 .00 34.50 122 123 125 ' 105 .00 34.50 123 124 131 ; 106 .00 34.50 124 k 107 .00 43.80 125 126 i 108 .00 42.90 126 127 '!
= 109 .00 44.40 '127 128 110 .00 44.40 128 129 ;
111 .00 ~ 44.50 129 '130 i 112 .00 34.50 130 138 139 ' 113 .00 43.80 131 132 ! 114 .00 42.90- 132 133 ! 115 .00 44.40 133 134 ! 116 .00 44.40 134 135 117 .00 44.30 135 136 l
i I' I EER No. 91-0039 , Rev. No. 0 l ATTACHMENT D: UICALEN2 INPUT DATA FILE Page No. 8 118 .00 34.50 136 137 138 ; 119 .00 34.50 137 '. 120 .00 34.50 122 140 143 l 121 .00 34.50 141 142 149 , 122 .00 34.50 142 123 .00 47.30 143 144 124 .00 43.80 144 145 125 .00 44.40 145 146 126 .00 44.40 146 147 127 .00 43.80 147 148 128 .00 34.50 148 156 157 129 .00 43.80 149 150 < 130 .00 43.80 150 151 l 131 .00 44.40 151 152 ! 132 .00 44.40 152 153 133 .00 43.80 153 154 ! 134 .00 34.50 154 155 156 135 .00 34.50 155 l 136 .00 34.50 139 157 158 l 137 .00 19.30 82 159 138 .00 19.30 159 160 161 ; 139 .00 19.30 64 160 i 140 .00 81.50 162 163 169 141 .00 75.00 163 164 177 , i 142 .00 72.80 164 165 l 143 .00 72.80 165 166 + 144 .00 74.20 166 167 l 145 .00 77.50 167 168 146 .00 81.20 168 176 192 - 147 .00 75.00 177 178 148 .00 75.00 178 179 I 149 .00 73.80 179 180 i 150 .00 73.90 180 181 + 151 .00 74.30 181 182 . 152 .00 63.50 182 190 191 ' 153 .00 81.50 169 170 171 154 .00 75.00 171 172 183 , 155 .00 72.80 172 173 ! 156 .00 72.80 173 174 157 .00- 74.20 174 175 : 158 .00 7 7 . 5', 175 176 159 .00 75.00 183 184 ! 160 .00 75.00 184 185 , 161 .00 73.80 185 186 : 162 .00 73.90 186 187 .i 163 .00 74.30 187 188 - 164 .00 63.50 188 189' 190 , 165 .00 58.80 191 198 199 ; 166 .00 46.80 192 193 167 .00 34.20 193 194 i 168 .00 34.20 194 195 t 169 .00 34.20 195 196 ! 170 .00 34.20 196 197
- 171 .00 34.20 197 502 172 .00 51.00 199 200 173 .00 81.50 170 201 208 i
i 174 .00 79.60 201 202 ' l
EER No. 91-0039 Rev. No. O
~ ATTACHMENT D: UICALEN2 INPUT DATA FILE Page No. 9 175 .00 75.00 202 203 -216 176 .00 72.80 203 204 177 .00 72.80 204 205 178 .00 74.10 205 206 179- .00 77.50 206 207 180 .00 77.50 207 215 228 181 .00 81.50 208 209 182 .00 79.80 209 210 183 .00 75.00 210 211 222 184 .00 72.80 211 212 185 .00 72.80 212 213 186 .00 74.10 213 214 187 .00 77.50 214 215 188 .00 75.00 216 217 189 .00 75.00 217 218 190 .00 73.40 218 219 191 .00 73.40 219 220 192 .00 74.30 220 221 193 .00 63.50 189 221 227 194 .00 75.00 222 223 195 .00 75.00 223 224 196 .00 73.40 224 225 197 .00 73.40 225 226 198 .00 74.08 226 227 199 .00 33.10 228 229 200 .00 33.10 229 230 201 .00 33.10 230 231 202 .00 33.10 231 232 203 .00 33.10 232 233 204 3000.00 33.10 233 234 205 -3000.00 71.90 80 234 235 300 .00 16.00 86 500 301 .00 14.20 103 501 302 .00 34.20 198 502 303 .00 12.50 53 503 304 .00 33.20 34 504-305 .00 33.20 34 505 306 .00 81.50 21 506 OUTPUT SELECTION: THE FOLLOWING RESULTS ARE OUTPUT RESULTS ARE OUTPUT FOR ALL PIPES WITH PUMPS - CLOSED PIPES ARE NOTED -RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 1 4 16 31 34 38 41 47 50 57 62 72 73 74 79 88 92 97 101 105 RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES': 109 116 120 128 134 146 152 166 174 179 185-197 198 205 213 218 224 233 234 235 RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 501 503 600 RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES : 1 2 14 15 16 27 28 36 37 49 50 66 70 74 75 RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES : 90 91 100 101 109 110.143 144 156 157 18 23 -
THIS SYSTEM HAS 243 PIPES WITH 212 JUNCTIONS , 27 LOOPS AND 5 FGNS
[ I EER No. .,,91-0039 .[ Rev. No. O ATTACHMENT D: UICALEN2 INPUT DATA FILE Page No. 10 i [ t TERMINATION DUE EITHER TO THE DETECTION OF AN ERROR OR USER INSTRUCTIONS .. c A
SUMMARY
OF CONDITICNS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS' THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : JUNCTION KLHBER DEMAND 13 124.00 4 66 3300.00 ' 70 -3300.00 f 204 .00 t 205 .00 ' 302 3000.00 165 -3000.00 LINE 166 IS OPEN ! LINE 174 IS OPEN LINE 179 IS OPEN 'i' LINE 185 IS OPEN LINE 198 IS CLOSED LINE 205 IS CLOSED 5 LINE 213 IS CLOSED LINE 218 IS CLOSED LINE 224 IS CLOSED l LINE 234 IS OPEN l THE FOLLOWING CHANCES IN PIPE DATA ARE SPECIFIED . FOR PIPE NUMBER 1 THE VALUE OF THE FIXED CRADE IS CHANCED TO 19..8 l l FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANCED TO 19.8 1 FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 153.3
-l PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 2 1 2 9.7 16.6 5.0 3.97 .00 5 4 5 9.7 16.6 5.0 5.40 .00 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS
~THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE :
JUNCTION NUMBER DEMAND 66 3300.00 70 -3300.00 13 127.00 302 3000.00 165 -3000.00 204 .00
i i i r i EER No. 91-0039
.Rev. No. O AITACHMENT D: UICALEN2 INPUT DATA FILE Page No. I1 .!
t i 205 .00 [ THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED i FOR. PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANCED TO 18.7 ' FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANCED TO 18.7 I FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANCED TO 79.8 - PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 2 1 2 9.7 16.6 5.0 3.84 .00
.5 4 5 9.7 16.6 5.0 5.67 .00.
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i f 1 I EER No. 91-0039 .! Rev.. No. 0 , ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. I j l l i FLOWRATE IS EXPRESSED IN GPM AND PRESSURE IN PSIG THE DARCY WEISBACH HEAD LOSS EQUATION IS USED. THE RINEMATIC VIS. = .0000070 ' THE SPECIFIC GRAVITY OF THIS LIQUID = 1.03 i A SUCCESSFUL GEOMETRIC VERIFICATION HAS BEEN COMPLETED OUTPUT SELECTION: THE FOLLOWING RESULTS ARE OUTPUT ! RESULTS ARE OUTPUT FOR ALL PIPES WITH PUMPS - CLOSED PIPES ARE NOTED ' RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 1 4 16 31 34 38 41 47 50 57 72 73 74 79 88 92 97 101 105 .; RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 109 116 120 128 134 146 152 166 174 179 185' ! 197'198 205 213 218 224 233 234 235 ~ RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 501 503 600 RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES : 1 2 14 15 16 27 28_ 36 37 49 50 66 70 74 75 RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES 90 91 100 101 109 110 143 144'156 157 18 23 204 205 302 1 RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES : 165 . THIS SYSTEM HAS 243 PIPES WITH 212 JUNCTIONS , 27 LOOPS AND 5 FCNS r THE RESULTS ARE OBTAINED AFTER S TRIALS WITH AN ACCURACY = .00356 ! U1SCNRIO CHANGE 0: WORST CASE MAX FLOW SCENARIO FOR NORMAL LOW BAY WATER LEVEL. \
'(-6.0 FT); COPY OF U2NOPOWR CHANGE 7 -SCENARIO RUN ON MODEL SET UP AS UICALEN2;FOR i SYSTEM LINEUP DETAILS OF U2NOPOWR CHANGE 7 SEE CALC C0050A-12 ATT'3 !
PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 ' LINE 1 IS CLOSED - ~i 4 0 4 7478.34 .04 110.92 .00 11.05 37-.82 16 12 13 118.00 .41 . 00 - .23 3.87 36.46 LINE 31 IS CLOSED 34 304 305 348.87 .40 .00 1.24 9.77 82.36 38 36 37 81.89 .06 .00 20.39 6.21 63.55 41 38 39 80.58 .06 .00 19.74 6.11 61.60
-47 41 42 81.85 .06 .00 20.37 6.21 63.49 50 43 44 80.31 .06 .00 19.61 6.09 61.21 57 49 50 11.38 .13 .00 7.90 5.04 128.95-62 53 54 12.85 .16 .00 4.03 5.70 162.66 72 59 62 1354.17 .00 .00 2.26 2.58 1.27 73 60 63 1314.53 .00 .00 2.13 2.51 1.20 74 61 64 1331.30 .00 .00 2.18 2.54 LINE 1.23 79 IS CLOSED
L i l-i EER No. 01-0039 + Rev. No. O ATTACIIMENT E: U1SCNRIO RESULTS FILE Page No. 2 > i
+
4 LINE 88 IS CLOSED LINE 92 IS CLOSED '( LINE 97 IS CLOSED i LINE .101 IS CLOSED 105 88 68 .00 .00 .00 .00 .00 .00 LINE 109 IS CLOSED LINE 116 IS CLOSED l LINE 120 IS CLOSED , LINE 128 IS CLOSED ' LINE 134 IS CLOSED ' LINE 146 IS CLOSED LINE 152 IS CLOSED ' 166 143 144 1401.60 .03 752.61 .00 8.99 28.63 f 174 156 157 1398.40 .03 752.71' .00 8.97 28.51 179 148 149 45.11 4.56 .00 2.32 9.40 265.29 185 160 161 44.22 4.39 .00 2.23 9.21 255.19 . 197 170 171 2800.00 .02 .00 .18 4.92 4.10 l' LINE 198 IS CLOSED LINE 205 IS CLOSED LINE 213 IS CLOSED LINE 218 IS CLOSED LINE 224 IS CLOSED 233 203 204 .00 .00 .00 .00 .00 .00 234 204 205 .00 .00 .00 .00 .00 .00 235 70 205 4000.00 .01 .00 .37 7.03 8.16 ; l 501 86 301 .00 .00 .00 .00 .00 .00 503 46 303 324.63 .04 .00 42.89 3.60 6.87. ; 600 17 0 122.16 .00 .00 1.54 .14' .01 JUNCTION NUMBER DEMAND CRADE LINE ELEVATION PRESSURE ; 1 .00 117.23 43.10 33.09 2 .00 117.23 42.40 33.40 14 .00 117.23 26.50 l ' 40.49 i 15 .00 117.64 26.50 40.68 ! 16 .00 117.64 26.50 40.68 . 18 .00 115.51 36.30 35.36
.00 23 114.46 12.50 45.51 27 .00 114.46 11.00. 46.18 1
28 .00 44.48 10.80 15.03 i 36 .00 112.57 17.50 42.43 i 37 00 92.13. 17.50 33.31 . 49 .00 107.82~ 8.30 44.42- !' 50 .00 99.80 8.30 40.84 66 4000.00 107.18 77.20 -13.38 . 70 -4000.00 41.48 ' 74.10 -14.56 74 .00 114.66 17.50 43.36
- l 75 .00 40.42 17.50 10.23 '
90 .00 114.66 31.60 37.07 ! 91 .00 40.42 31.60 3.94 100 .00 114.66 11.40 46.09 101 .00 40.42 28.50 5.32 109 .00 116.46 44.40 32:.16 l 110 .00 28.90 44.40 -6.92 143 .00 114.48 72.80 18.60 i 144 .00 .867.06 74.20 353.88 i l 156 .00 114.45 72.80 18.59 '! 1 . .
i l i EER No. 01-0039 : Rev. Nc. O ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 3 s 157 .00 867.14 74.20 353.91 l 165 -2800.00 41.29 58.80 -7.82 , 1 204 .00 41.11 33.10 3.57 i 205 .00 41.11 71.90 .-13.74 ' l 302 2800.00 862.75 34 20 369.81 l THE NET SYSTEM DEMAND = 118.00-
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GdADE NODES l PIPE NUMBER FLOWRATE 4 7478.34 ' 158 .00 161 -7238.19 ' 600 122.16 THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 7478.34
- THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -7360.36 J
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I I I- ! EER No. 01-0039 r i Rev. No. O L- ATTACIDENT E: U1SCNRIO RESULTS FILE Page'No. 4 i i i A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS i THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE - JUNCT'7N NUMBER DEMAND ' 13 110.00 1 66 .00 i i 70 .00 : 165 .00 ! 302 .00 4 LINE 31 IS OPEN LINE 79 IS OPEN ; LINE 88 IS OPEN LINE 92 IS OPEN LINE 97 IS OPEN t LINE 101 IS OPEN LINE 109 IS OPEN LINE 116 IS OPEN LINE 120 IS OPEN LINE 128 IS OPEN ( LINE 134 IS OPEN LINE 198 IS OPEN ; THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED ' FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANCED TO 26.5 i PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 2 1 2 9.7 16.6 5.0 1.59 .00 5 4 5 9.7 16.6 5.0 1.59 00' 24 20 55 24.1 19.3 .2 420.08 .00 79 66 70 29.5 15.3 .2 85.93 .00 ' 198 302 165 205.0 15.3 .2 2192.66 .00 THE RESULTS ARE ')BTAINED AFTER 10 TRI ALS WITH AN ACCURACY = ' .00199 ! U1SCNRIO CHANGE 1:U2NOPOWR CHANGE 8 SCENARIO (CALC C0050A-12 ATT 3) RUli GN MODEL - SET UP AS UICALEN2 NOTE: U2NOPOWR UNNECESSARILY ASSUMES 4 DCs;THIS RUN CHANGED TO STANDARD 2 DGs ! PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 LINE 1 IS CLOSED THE PUMP IN LINE 4 IS OPERATING OUT OF RANGE 4 0 4 8347.16 .05 88.74 .00 12.33 47.101 16 12 13 110.00 .36 .00 .20 3.61 31.71 ! 31 27 28 42.01 .02 .00 18.15 3.19 17.82 34 304 305 321.17 .34 .00 1.05 8.99 70.14 38 36- 37 65.53 .04 .00 13.05 4.97 41.45 41 38 39 64.48 .04 .00 12.64 4.89 40.19 47 41 42 65.50 .04 .00 13.04 4.97 41.42 50 43 44 64.27 .04 .00 12.56 4.88 39.94' 57 49 50 9.10 .08 .00 5.06 4.03 84.36 62 53 54 10.28 .11 .00 2.58 4.56 106.22 72 59 62 687.25 .00 .00 .58 1.31 .36
4
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EER No. 01-0039' Rev. No. 0 ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 5 i f i
)
73 60 63 666.99 .00 .00 .55 1.27 .34 { 74 61 64 675.82 .00 .00 .56 1.29 .35 : 79 66 70 2030.05 .07 .00 16.96 3.57 2.22 i 88 74 75 75.89 .05 .00 6.18 5.76 54.91 i 92 76 77 76.99 .06 .00 6.36 5.84 56.44 97 81 82 77.97 .06 .00 6.52 5.92 57.84 , 101 83 84 75.27 .05 .00 6.08 5.71 54.05 l 105 88 68 388.63 .78 .00 3.00 4.31 9.67 ! 109 90 91 11.91 .14 .00 .43 5.28 140.71 - 116 96 97 11.95 .14 .00 ' 1.31 5.30 141.50 120 100 101 58.65 .03 .00 1.23 4.45 33.54 128 109 110 950.21 .02 .00 6.72 6.94 18.74 ! 134 115 116 908.J' .02 .00 1.37 6.63 17.19 ! LINE 146 IS CLOSED LINE 152 IS CLOSED + 166 143 144 1380.3o .03 753.30 .00 8.85 27.50 :i" 174 156 157 1377.12 .03 753.40 .00 8.83 27.68 179 148 149 37.42 3.18 .00 1.60 -7.80 184.81 185 160 161 36.tB 3.06 .00 1.53 7.64 177.78 197 170 171 2757.53- .02 .00 .17 4.84 3.99 , 198 302 165 2757.58 .82 .00 798.61 4.84 3.99 - LINE 205 IS CLOSED LINE 213 IS CLOSED LINE 218 IS CLOSED l LINE 224 IS CLOSED ! 233 203 204 .00 .00 .00 .00 .00 .00 ? 234 204 205 .00 .00 .00 .00 .00 .00 .! 235 70 205 2030.05 .00 .00 .09 3.57 2.22 i 501 86 301 306.12 .01 .00 26.82 3.39 6.14 503 46 303 259.78 .03 .00 27.46 2.88- 4.50 ! 600 17 0 806.89 .00 .00 67.21 .95 .25 ' JUNCTION NUMBER DE.W D CRADE LINE ELEVATION PRESSURE 1 .00 93.71 43.10 22.59 . 2 .00 93.71 42.40- 22.90 l 14 .00 93.71 26.50 30.00 15 .00 93.71 26.50 30.00 16 .00 93.71 26.50 30.00 18 .00 92.34 36.30 25.01 23 .00 88.66 12.50 33.99 ; 27 .00 83.19 11.00 32.22 28 .00 65.03 10.80 24.20 : 36 .00 87.44 17.50 31.22 'l 37 .00 74.35 17.50 25.37 ( 49 .00 84.39 8.30 33.96 ; 50 .00 79.25 8.30 31.67 66 .00 57.53 77.20 -8.78 , 70 .00 40.50 74.10 -15.00 ; 74 .00 84.80 17.50 30.04 l 4 75 .00 78.57 17.50 27.26 i 90 .00 87.70 31.60 25.04 91 .00 87.13 31.60 24.78 100 .00 77.18 11.40 29.36 101 .00 75.91 28.50 21.16 109 .00 61.76 44.40 7.75 110 .00 35.02 44.40 4.74
t
^EER No. 91-0039 !
Rev. No.
-0 ATTACHMENT E: U1SCNRIO RESULTS FILE Page'No. 6 'i 143 .00 91.45 72.80 8.32 .;
144 .00 844.72 74.20 343.91 + 156 .00 91.42 72.80 8.31 ! 157 .00 844.80 74.20 343.94 ! 165 .00 41.11 58.80 -7.90 204 .00 40.41 33.10 3.26 205 .00 40.41 71.90 -14.06 302 .00 840.53 34.20 359.89 THE NET SYSTEM DEMAND = 110.00 ,
SUMMARY
OF INFLOWS {+) AND OUTFLOWS (-) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE I 4 8347.16 158 -1858.73 161 -5571.54 600 -806.89 i THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 8347.16 ' THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -8237.16 , i i l
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r L I ? l l l EER No. 91-0039 ! l Rev. No. O AITACHMENT E: UlSCNRIO RESULTS FILE Page No. 7 . l A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS i L THE FOLLOWING SPECIFIC DEMAND CHANCES ARE FADE : i l JUNCTION NUMBER
- DEMAND 66 4000.00 '
70 -4000.00 302 2800.00 165 -2800.00 13 124.00 LINE 31 IS CLOSED i LINE 79 IS CLOSED LINE 88 IS CLOSED l LINE 92 IS CLOSED - LINE 97 IS CLOSED LINE 101 IS CLOSED , LINE 109 IS CLOSED LINE 116 IS CLOSED LINE 120 IS CLOSED LINE 128 IS CLOSED -; LINE 134 IS CLOSED - LINE 198 IS CLOSED , THE FOLLOWING CHANCES IN PIPE DATA ARE SPECIFIED , FOR PIPE NUMBER 1 THE VALUE OF THE FIXED CRADE IS CHANGED TO 22.0
- FOR PIPE NUMBER 4 THE VALUE OF THE FIXED CRADE IS CHANGED TO- 22.0 3
FOR PIPE NUMBER 600 THE VALUE OF THE FIXED CRADE IS CHANGED TO 116.1 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED CRADE 2 1 2 9.7 16.6 5.0 1.78 00 , 5 4 5 9.7 16.6 5.0 1.78 .00 24 20 55 24.1 19.3 .2 .68 .00 l l THE RESULTS ARE OBTAINED AFTER 3 TRIALS WITH AN ACCURACY = .00159 U1SCNRIO CHANGE 2: WORST CASE MAX FLOW SCENARIO FOR NORMAL HICH BAY WATER LEVEL (+2.0 FT); COPY OF U2NOPOWR CHANGE 5 SCENARIO RUN ON MODEL SET UP AS UICALEN2;FOR I SYSTEM LINEUP DETAILS OF U2NOPOWR CHANGE 5 SEE CALC C0050A-12 ATT 3 , l PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 LINE 1 IS CLOSED l 4 0 4 7611.95 .04 107.67 .00 11.24 39.18 l 16 12 13 124.00 .45 .00 .25 4.06 40.25 1 i l LINE 31 IS CLOSED t l 34 304 305 359.40 .42 .00 1.32 10.06 87.26 38 36 37 84.36 .07 .00 21.64 6.40 67.29 i 41 38 39 83.01 .07 .00 20.95 6.30 65.23 , l 47 41 42 84.32 .07 .00 21.62 6.40 67.23 ! 50 43 44 82.74 .06 .00 20.81 6.28 64.82 l l 57 49 50 11.73 .14 .00 8.39 5.20 136.50 l 62 53 54 13.24 .17 .00 4.28 5.87 172.22 1 l t'
P 1 EER No. 01-0030- ,. Rev. No. 0
- ATTACIDfENT E: U1SCNRIO RESULTS FILE Page No. 8 72 59 62 1354.17 .00 .00 2.26 2.58 1.27 '
73 60 63 1314.53 .00 .00 2.13 2.51 1.20 6 74 61 64 1331.30 .00 .00 2.18 2.54 1.23 LINE 79 IS CLOSED , i LINE 88 IS CLOSED i LII'E 92 IS CLOSED LINE 97 IS CLOSED ! LIhT 101 IS CLOSED
- 105 88 68 .00 .00 .00 .00 .00 .00 !
LINE 109 IS CLOSED ' LINE 116 IS CLOSED LINE 120 IS CLOSED I LINE 128 IS CLOSED LINE 134 IS CLOSED : LINE 146 IS CLCSED i LINE 152 IS CLOSED 166 143 144 1401.60 .03 752.61 .00 8.99 23.63 174 156 157 1398.40 .03 752 71 .00 8.97 28.51 > 179 148 149 46.49 4.84 .00 2.46 9.69 281.24 .! 185 160 161 45.57 4.65 .00 2.37 9.50 270.53 ! 197 170 171 2800.00 .02 .00 .18 4.92' 4.10 LINE 198 IS CLOSED i~ LINE 205 IS CLOSED ! LINE 213 IS CLOSED LINE 218 IS CLOSED : LINE 224 IS CLOSED ; t 233 203 204 .00 .00 .00 .00 .00 .00 ' 234 204 205 .00 .00 .00 .00 .00 .00 < 235 70 205 4000.00 .01 .00 .37 7.03 8.16 ' 501 86 301 .00 .00 . 00 .00 .00 .00 503 46 303 334.44 .04 .00 45.32 3.71 7.27 600 17 0 236.55 .00 .00 5.78 .28 .02 l j JUNCTION NUMBER DEMAND CRADE LINE ELEVATION PRESSURE ! 1 .00 121.79 43.10 35.12 4 2 .00 121.79 42.40 35.44 1 14 .00 121.79 26.50 42.53 ! 15 .00 121.88 26.50 42.57 16- .00 121.88 26.50 42.57 18 .00 120.08 36.30 37.39 23 .00 118.96 12.50 47.52 1 27 .00 118.96 11.00 48.19 28 .00 44.69 10.80 15.12 36 .00 116.96 17.50 44.39 37 .00 95.25 17.50 34.70 49 .00 111.92 8.30 46.25 50 .00 103.40 8.30 42.44 66 4000.00 111.73 77.20 15.41 70 -4000.00 41.48 74 10 -14.56 74 .00 I?9.16 17.50 45.38 75 .00 0.42 17.50 10.23 90 .00 7.9.16- 31.60 39.08 91 .00 40.42 31.60 3.94 100 .00 .19.16 11.40 48.10 ) 101 .00 40.42 28.50 5.32 i 109 .00 121.02 44.40 34.20
L il i o g EER No. 91-0039 i- Rev. No. O I
- l. ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 0 110 .00 28.90 44.40 -6.92 I 143 .00 119.04 72.80 20.64 i 144 .00 871.62 74.20 355.92 '
156 .00 119.02 72.80 20.63 : 157 .00- 871.70 74.20 355.95~
-2800.00 165 41.30 58.80 .-7.81 '
204 .00 41.11 33.10 3.57 f 205 .00 41.11 71.90 -13.74 , 302 2800.00 867.31 34.20 371.84 1 i THE NET SYSTEM DEMAND = 124.00 i
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES $ PIPE NUMBER FLOWRATE 4 7611.95 - 158 .00 161 -7251.46 li 600 -236.55 THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 7611.95 ' THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -7488.01 'i l t 4 1 i
'I 3
i i l l-l
-i EER No. 01-0039 i Rev. No. O !
ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 10 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : JUNCTION NUMBER DEMAND A 66 00 70 .00 302 .00 165 .00 i 13 110.00 t LINE 31 IS OPEN LINE 88 IS OPEN LINE 92 IS OPEN ! LINE 97 IS OPEN LINE 101 IS OPEN LINE 109 IS OPEN : LINE 116 IS OPEN ' LINE 120 IS OPEN LINE 128 IS OPEN LINE 134 IS OPEN
- LINE 79 IS OPEN !
LINE 198 IS OPEN ' THE FOLLOWING CHANCES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 26.5 f PIFE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE .; 2 1 2 9.7 16.6 5.0 1.56 .00 ' 5 4 5 9.7 16.6 5.0 1.56 .00 ' 24 20 55 24.1 19.3 .2 420 08 ,00 79 66 70 '29.5 15.3 .2 91.88 .00 205.0 198 302 165 15.3 .2 2204 74 .00 i THE RESULTS ARE OBTAINED AFTER 10 TRIALS WITH AN ACCURACY = .00205 i I U1SCNRIO CHANGE 3:U2NOPOWR CHANGE 6 SCENARIO (CALC G0050A-12. ATI 3) RUN ON MODEL SET UP AS UICALEN2 , NOTE:U2NOPOWR UNNECESSARILY ASSUMES 4 DGs;THIS RUN CHANCED TO STANDARD 2 DGs- l l PIPE NO NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000. LINE 1 IS CLOSED . i THE PUMP IN LINE 4 IS. OPERATING OUT OF-RANGE l 4 0 4 8496.48 .05 84.73 .00 12.55 48.80 16 12 13 110.00 .36 .00 .20 3.61 31.71 J 31 27 28 43.48 .02 .00 19.44 3,30 19.01 { 34 304 305 332.52 .36 .00 1.13 9.31 75.03 38 36 37 67.85 .04 .00 14.00 5.15 44.31' .! 41 38 39 66.76 .04 .00 13.55 5.07 42.96 I 47 41 42 67.82 .04 .00 13.98 5.15 44.27 i
.50 43 44 66.55 04 .00 13.46 . 5. 05- 42.69 57 49 50 9.43 .09 .00 5.42 4.18 90.12-62 53 54 10.64 .11 .00 2.76 4.72 113.50 72 59 62 703.32 .00 .00 .61 1.34 .37 i
j
I s i EER No. 01-0039 Rev. No. O I ATTACIIMENT E: U1SCNRIO RESULTS FILE Page No. 11 i i 73 60 63 682.60 .00 .00 .57 1.30 .35 k 74 61 64 691.62 .00 .00 .59 1.32 .36 i 79 66 70 2077.53 .07 .00 18.99 3.65 2.32 88 74 75 78.55 .06 .00 6.62 5.96 58.67 i 92 76 77 79.69 .06 .00- 6.81 6.05 60.31 ' 97 81 82 80.71 .06 .00 6.99 6.13 61.80 ; l 101 83 84 77.91 .06 .00 6.51 5.91 57.75 : 1 105 88 68 402.23 .83 .00 3.21 4.46 10.33 r 1 109 90 91 12.32 .15 .00 .46 5.46 149.99 -i 116 96 97 12.36 .15 .00 1.40 5.48 150.89 120 ! 100 101 60.68 .04 .00 1.32 4.60 35.79 128 109 110 977.42 .02 .00 7.12 7.14- 19.79 1 134 115 116 934.54 .02 .00 1.45 6.82 18.15 LINE 146 IS CLOSED ! LINE 152 IS CLOSED 166 143 144 1379.77 .03 753.32 .00 8.85 27.78 174 156 157 1376.62 .03 753.42 .00 8.83 27.65 , 179 148 149 38.77 3.40 .00 1.71 8.08' 197 84 ! 185 160 161 38.03 3.28 .00 1.65 7.92 190.60 l 197 170 171 2756.39 .02 .00 .17 4.84 3.98 i 198 302 165 2756.39 .82 .00 802.32 4.84 3.98 LINE 205 IS CLOSED l LINE 213 IS CLOSED LINE 218 IS CLOSED ' LINE 224 IS CLOSED 233 203 204 .00 .00 .00 .00 .00 .00 234 204 205 .00 .00 .00 .00 .00 .00 235 70 205 2077.53 .00 .00 .10 3.65 2.32 501 86 301 316.87 .02 .00 28.74 3.51 6.56 503 46 303 268.98 .03 .00 29.44 2.98 4.81 600 17 0 829.05 .00 .00 70.95 .98 .26 JUNCTION NLHBER DEMAND GRADE LINE ELEVATION PRESSURE-1 .00 97.45 43.10 24.26 ! 2 .00 97.45 42.40 24.57 14 .00 97.45 26.50 31.67 15 .00 97.45 26.50 31.67 16 .00 97.45 26.50 31.67 18 .00 96.04 36.30 26.66 23 .00 92.10 12.50 35.53 27 .00 86.20 11.00 33.56 I 28 .00 66.74 10.80 24.97 36 .00 90.79 17.50 32.71 37 .00 76.76 17.50 26.45 49 .00 87.52 8.30 35.36 50 .00 82.01 8.30 32.90 i 66 .00 59.58 77.20 -7.86 70 .00 40.52 74.10 -14.99 74 .00 87.97 17.50 31.45 75 .00 81.29 17.50 28.47 90 .00 90.98 31.60 26.50 91 .00 90.36 31.60 26.23 100 .00 79 79 11.40 30.52 101 .00 78.43 28.50 22.29 109 .00 63.67 44.40 B.60 110 .00 56.53 44.40 5.41 P- ** 1 mv Sr
EER No. 91-0039 Rev. No. O ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 12 1 143 .00 95.14 72.80 9.97 ) l 144 .00 848.44 74.20 345.57 1 156 .00 95.12 72.80 9.96 l- 157 .00 848.52 74.20 345.60
.00 41.12 165 58.80 -7.89 ;
204 .00 40.42 33.10 3.27
.00 40.42 205 71.90 -14.05 !
302 .00 844.26 34.20 361.55 -j THE NET SYSTEM DEMAND = 110.00 l
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES ( PIPE NUMBER FLOWRATE 4 8496.48
- 158 -1911.96 161 -5645.47 ,
I 600 -829.05 , THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 8496.48 THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -8386.49
)
'i e
i. l l l l l l I 1
EER No. 91-0039 Rev. No'. O ATTACIDfENT E: U1SCNRIO RESULTS FILE Page No. 13 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS THE FOLLOWING SPECIFIC DEMAND CHANGES ARE-MADE : JUNCTION NUMBER DEMAND 13 168.00 66 4000.00 70 -4000.00 302 2800.00 165 -2800.00 LINE 31 IS CLOSED LINE 38 IS CLOSED LINE 41 IS CLOSED LINE 47 IS CLOSED LINE 50 IS CLOSED LINE 57 IS CLOSED LINE 62 IS CLOSED LINE 79 IS CLOSED LINE 88 IS CLOSED LINE 92 IS CLOSED LINE 97 IS CLOSED LINE 101 IS CLOSED LINE 109 IS CLOSED LINE 116 IS CLOSED LINE 120 IS CLOSED LINE 128 IS CLOSED LINE 134 IS CLOSED LINE 198 IS CLOSED THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANGED TO 42.0 FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANCED TO 42.0 FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 116.1 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 2 1 2 9.7 16.6 5.0 1.79 .00 5 4 5 9.7 16.6 5.0 1.79 .00 I 24 20 55 24.1 19.3 .2 .68 .00 1 THE RESULTS ARE OBTAINED AFTER 2 TRIALS WITH AN ACCURACY = .00334 U1SCNRIO CHANGE 4: WORST CASE MAX FLOW SCENARIO FOR FLOOD BAY WATER LEVEL (+22.0 FT): COPY OF NOVTLHDR CHANGE 16 SCENARIO RUN ON MODEL SET UP AS UICALEN2; FOR SYSTEM LINEUP DETAILS OF NOVTLHDR CHANGE 16 SEE CALC C0050A-12 ATT 17 PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 LINE 1 IS CLOSED 4 0 4 7581.47 . 04 108.42 .00 11.20 38.87 16 12 13 168.00 .83 .00 .47 5.51 73.72-LINE 31 IS CLOSED 34 304 305 .00 .00 .00 .00 .00 .00
L S EER No. 01-0039 .; Rev.. No. O ~, ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 14 1 L LINE 38 IS CLOSED LINE 41 IS CLOSED l LINE 47 IS CLOSED LINE 50 IS CLOSED ! LINE 57 IS CLOSED
- LINE . 62 IS CLOSED '[
72 59 62 1354.17 .00 .00 2.26 2
. 58 1.27 !
l 73 60 63- 1314.53 .00 .00 2.13 2.51 1.20 E 74 61 64 1331.30 .00 .00 2.18 2.54- 1.23 LINE 79 IS CLOSED
- LINE 88 IS CLOSED LINE 92 IS CLOSED LINE 97 IS CLOSED '
LINE 101 IS CLOSED 105 88 68 .00 .00 .00 .00 .00 .00 ' LINE 109 IS CLOSED ' LINE 116 IS CLOSED I LINE 120 IS CLOSED LINE 128 IS CLOSED , LINE 134 IS CLOSED
.LINE 146 IS CLOSED LINE 152 IS CLOSED i 166 143 144 1401.60 .03 752.61 .00 8.99 28.63 1398.40 .03 174 156 157 752.71 .00 8.97 28.51 179 185 148 160 149 161 52.48 31.44 6.12 5.89
-. 00
.00 3.14 3.02 10.94 10.72 355.89. .;
342.32 197 170 171 2800.00 .02 .00- .18 4.92 4.10 - LINE 198 IS CLOSED ! LINE 205 IS CLOSED ' LINE 213 IS CLOSED I LINE 218 IS CLOSED LINE 224 IS CLOSED 233 203 204 .00 .00 .00 .00 .00- .00-234 204 205 .00 .00 .00 .00 .00 .00- ' 235 70 205 4000.00 .01 .00 .37 7.03 8.16 , 501 86 301 .00 .00 .00 .00 .00 .00 ! 503 46 303 .00 .00 .00 .00 .00 .00 600 17 0 509.56 .00 .00 26.80 .60 .10 l~ JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE i 1 .00 142.59 43.10 44.40 ' 2 .00 142.59 42.40 44.72 < 14 .00 142.59 26.50 51.81 I 15 .00 142.90 26.50 51.95 i 16 .00 142.90 26.50 51.95 - l 18 .00 141.03 36.30 46.74 23 .00 141.03 12.50 57.37- ' 27 .00 141.03 11.00 58.04 , 28 .00 40.98 10.80 13.47 ! 36 .00 141.03 17.50 55.13 I 37 .00 40.98 17.50 10.48 49 .00 141.03 8.30 59.24 50 .00 40.98 8.30 14.58 66 4000.00 132.69 77.20 24.77 70 -4000.00 41.45 74.10 -14.57 74 .00 141 03 17.50. 55.14
EER No. 91-0039 Rev. No. O ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 15 75 .00 40.39 17.50 10.22 90 .00 141.03 31.60 48.84 91 .00 40.39 31.60 3.92 100 .00 141.03 11.40 57.86 101 .00 40.39 28.50 5.31 109 .00 141.89 44.40 43.51 110 .00 28.90 44.40 -6.92 143 .00 139.99 72.80 29.99 144 .00 892.57 74.20 365.26 156 .00 139.96 72.80 29.98 157 .00 892.65 74.20 365.30 165 -2800.00 41.10 58.80 -7.90 204 .00 41.08 33.10 3.56 205 .00 41.08 71.90 -13.76 302 2800.00 888.26 34.20 381.20 THE NET SYSTEM DEMAND = 168.00
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE 4 7581.47 158 .00 161 6903.91 600 -509.56 THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 7581.47 THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = 7413.47
EER No. 41-0039 , Rev. No. O ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 16 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS i i THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : , JUNCTION NUMBER DEMAND ' 13 110.00 66 .00 ' 70 .00 ; 302 .00 t 165 .00 j LINE 79 IS OPEN LINE 128 IS OPEN LINE 134 IS OPEN ; LINE 198 IS OPEN THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 26.5 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE i 2 1 2 9.7 16.6 5.0 1.47 .00 ! 5 4 5 9.7 16.6 5.0 1.47 .00 79 66 70 29 5 15.3 .2 119.25 .00 ; 198 302 165 205.0 15.3 .2 2261.08 .00 { THE RESULTS ARE OBTAINED AFTER 7 TRIALS WITH AN ACCURACY = .00346 ! U1SCNRIO CHANGE 5:NOVTLHDR CHANGE 17 SCENARIO (CALC G0050A-12 ATT 17) RUN ON MODEL SET UP AS UICALEN2 NOTE:NOVTLHDR UNNECESSARILY ASSUMES 4 DCs:THIS RUN CHANGED TO STANDARD 2 DGs PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 LINE 1 IS CLOSED THE-PUMP IN LINE 4 IS OPERATING OUT OF RANCE 4 0 4 8951.20 .05 72.53 .00 13.22 54.15 I 16 12 13 110.00 .36 .00 .20 3.61 31.71 i LINE. 31 IS CLOSED 1 34 304 305 .00 .00 .00 .00 .00 .00 LINE 38 IS CLOSED LINE 41 IS CLOSED LINE 47 IS CLOSED LINE 50 IS CLOSED LINE 57 IS CLOSED ! LINE 62 IS CLOSED ' 72- 59 62 1065.90 .00 .00 1.40 2.03 .81 ) 73 60 63 1034.64 .00 .00 1.32 1.97 .76 1 74 61 64 1047.99 .00 .00 1.35' 2.00 .78 ) 79 66 70 3148.53 .15- .00 56.62 5.53 5.14 LINE 88 IS CLOSED -)' LINE 92 IS CLOSED-LINE 97 IS CLOSED LINE 101 IS CLOSED 105 88 68 .00 .00 .00 .00 .00 .00 LINE 109 IS CLOSED I
I EER No. 91-0039-' ! Rev. No. 0 , ATTACIDENT E: U1SCNRIO RESULTS FILE Page No. I7 LINE 116 IS CLOSED l LINE 120 IS CLOSED I 128 109 110 1026.29 .02 .00 7.84 7.49 21.75 i 134 115 116 981 28 .02 .00 1.59 7.16 19.94 i LINE 146 IS CLOSED ! LINE 152 IS CLOSED ! 166 143 144 1368.77 .03 753.68 .00 8.78 27.35 i 174 156 157 1365.65 .03 753.78 .00 8.76 27.23- ' 179 148 149 41.18 3.82 .00 1.93 8.58 222.34 ! 185 160 161 40.36 3.68 .00 1.86 8.41 213.88 ' 197 170 171 2734.42 .02 .00 .17 4.80 3.92 ; 198 302 165 2734.42 .80 .00 809.75 4.80 3.92 i LINE 205 IS CLOSED - LINE 213 IS CLOSED LINE 218 IS CLOSED ! LINE 224 IS CLOSED : 233 203 204 .00 .00 .00 .00 .00 .00 i 234 204 205 .00 .00 .00 .00 .00 .00 235 70 205 3148.53 .00 .00 .23 5.53 5.14 l 501 86 301 .00 .00 .00 .00 .00 .00 503 46 303 .00 .00 .00 .00 .00 .00 ; 600 17 0 869.15 00 .00 77.98 1.02- .29 JUNCTION NUMBER DEMAND CRADE LINE ELEVATION PRESSURE 1 .00 104.48 43.10 27.40 2 .00 104.48 42.40 27.71 14 .00 104.48 26.50 34.80 15 .00 104.48 26.50 34.80 16 .00 104.48 26.50 34.80 ; 18 .00 102.91 36.30 29.73 l 23 .00 102.91 12.50 40.35 ! 27 .00 102.91 11.00 41.02 28 .00 40.86 10.80 13.42 36 .00 102.91 17.50 38.12 37 .00 40.86 17.50 10.43 49 .00 102.91 8.30 42.23 50 .00 40.86 8.30 14.53 66 .00 97.71 77.20 9.15 70 .00 40.94 74.10 -14.80 74 .00 102.91 17.50 33.12 75 .00 40.28 17 50 10.17 90 .00 102.91 31.60 31.83 91 .00 40.28 31.60 3.87 1 100 .00 102.91 11.40 40.84 l 101 .00 40.28 28.50 5.26 ! 109 .00 67.23 44.40 10.19 110 .00 59.36 44.40 6.68 143 .00 101.97 72.80 13.02 144 .00 855.62 74.20 348.77 i 156 .00 101.95 72.80 13.01 157 .00 855.70 74.20 348.81 165 .00 40.97 58.80 -7.96 204 .00 40.71 33.10 3.39 205 .00 40.71 71.90 -13.92 l 302 .00 851.53 34.20 364.80 l l l \ . . .
I "' SER No. 91-0039' : Rev. No 0 ATTACHMENT E: U1SCNRIO RESULTS FILE Page No.' 18 i THE NET SYSTEM DEMAND = 110.00 i I l-
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE ; 4 8951.20 158 -2007.57 , 161 -5964.48 ; 600 -869.15 ; THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES =. 8951.20 j
~
t THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -8841.20. 1 l
.I I
l e 1 1 l o
I l EER No 0030 't
-Rev. No. 0 . ATTACHMENT E: U1SCNRIO RESULTS FILE- Page No. 19 !
t l L A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS f i j THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : JUNCTION NUMBER DEMAND 13 179.00 -* 66 .00 'i 70 .00 302 4100.00 ! 165 -4100.00 + LINE 38 IS OPEN : LINE 41 IS OPEN ! LINE 47 IS OPEN 1 LINE 50 IS OPEN ' l LINE 57 IS OPEN LINE 62 IS OPEN LINE 72 IS CLOSED LINE 73 IS CLOSED ! LINE 74 IS CLOSED 'i LINE 128'IS CLOSED LINE 134 IS CLOSED i LINE 198 IS CLOSED THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANCED TO 11.4 i FOR PIPE NUMBER 4 THE VALUE CF THE FIXED GRADE IS CHANCED TO 11.4 FOR PIPE NUMBER 600 THE VALUE.0F THE FIXED GRADE IS CHANCED TO 116.1 i
! I PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE I 2 1 2 9.7 .16.6 5.0 '2.77 .00 5 4 5 9.7 16.6 5.0 2.77 .00 THE RESULTS ARE OBTAINED AFTER 7 TRIALS WITH AN ACCURACY = .00307-U1SCNRIO CHANGE 6: WORST CASE MAX FLOW SCENARIO FOR LOLO BAY WATER LEVEL (-8.63 FT); COPY OF RBCCWOUT CHANGE 2 SCENARIO RUN ON MODEL SET UP.AS UICALEN2: FOR SYSTEM LINEUP DETAILS OF RBCCWOUT CHANGE 2 SEE CALC C0050A-12 ATT 19-PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 LINE 1 IS CLOSED
'4 0 4 5476.34 .02 152.58 .00 8.09 20.30 16 12 13 179.00 .95 .00 .53 5.87 83.66 LINE 31 IS CLOSED 34 304 305 441.78 .63 .00 1.99 12.37 130.46 38 36 37 102.36 .10 .00 31.85. 7.77 97.69 41 38 39 100.71 .09 .00 30.84 7.64 94.68 l 47 41 42 102.31 .10 .00 31.82 7.76 97.59 50 43 44 100.38 .09 .00 30.63 7.62 94.07 1 57 49 50 17.38 .29 .00 18.43 7.70 290.47 62 53 54 18.64 .33 .00 8.48 8.26 332.43 i LINE 72 IS CLOSED l
J l
i
}
EER No. 41-0039 ! Rev. No. O ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 20 i l t 'LINE 73 IS CLOSED 5 LINE 74 IS CLOSED 79 66 70 .00 .00 .00 .00 .00 .00 '[ LINE 88 IS CLOSED L LINE 92 IS CLOSED LINE 97 IS CLOSED ! LINE 101 IS CLOSED .i 105 88 68 .00 .00 .00 .00 .00 .00 ' LINE 109 IS CLOSED LINE 116 IS CLOSED > LINE 120 IS CLOSED - LINE 128 IS CLOSED LINE 134 IS CLOSED I LINE 146 IS CLOSED LIhT - 152 IS CLOSED - 166 143 144 2052.25 .06 725.81 .00 13.16 60.20 2047.75 174 156 157 .06 726.03 .00 13.14 59.95 ' 179 148 149 56.50 7.07 .00 3.64 11.78 410.99 185 160 161 55.38 6.80 .00 3.49 11.54 395.21 -l 197 170 171 4100.00 .04 .00 .39 7.20 '8.56 ' LIhT 198 IS CLOSED LINE 205 IS CLOSED LINE 213 IS CLOSED LINE 218 IS CLOSED I LINE 224 IS CLOSED 233 203 204 .00 .00 .00 .00- .00 .00 ' 234 204 205 .00 .00 .00 .00 .00 .00 235 70 205 .00 .00 .00 .00 .00 .00 ! 501 86 301 .00 .00- .00 .00 .00 .00 503 46 303 405.74 .06 .00 66.99 4.50 10.50 600 17 0 643.69 .00 .00 42.77 .76 16 JUNCTION NUMBER DEMAND CRADE LINE ELEVATION PRESSURE ! 1 .00 158.87 -43.10 51.67 2 .00 158.87 42.40 51.98 14 .00 158.87 26.50 59.08 15 .00 158.87 26.50 59.08 16 .00 158.87 26.50 59.08 18 .00 158.16 36.30 54.39 23 .00 156.48 12.50 64.26 ' 27 .00 156.50 11.00 64.94 i 28 .00 47.17 10.80 16.23 i 36 .00 153.55 17.50 60,72 ! 37 .00 121.62 17-.50 46.47 , 49 .00 141.21 8.30 59.32 50 .00 174.05 8.30 73.98 66 .00 40.14 77.20 -16.54 70 .00 40.14- 74.10 -15.16 " 74 .00 156.79 17.50 62.17 -! 75 .00 40.14 17.50 10.10 , 90 .00 156.79 31.60 55.88
.00 40.14 91 31.60 3.81 l 100 .00 156.79 11.40 64.89 .
101 .00 40.14 28.50 5.19 l 109 .00 158.55 44.40 50.95 l 110 .00- 28.90 44.40 6.92 r l 5
i EER No. 01-0039 ' Rev. No. O ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 21 143 .00 156.35 72.80 37.29 144 .00 882.10 74.20 360.59 ! 156 .00 156.30 72.80 37.27 ; 157 .00 882.27 74.20 360.67 ' 165 -4100.00 42.13 58.80 -7.44 204 .00 40.14 33.10 3.14 205 .00 40.14 71.90 -14.18 302 4100.00 872.89 34.20 374.34 > THE NET SYSTEM IEMAND = 179.00
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED CRADE NODES ' PIPE NUMBER FLOWRATE 4 5476.34 1 158 .00 161 -4653.66 600 -643.69 THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 5476.34
-THE NET FLOW OUT OF THE SYSTEM INTO FIXED CRADE NODES = -5297.35 l
1 i l l
1 R l' :: j i EER No. 91-0039 -{ i Rev. No. O l . ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 22 ! A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS
- lC THE FOLLOWING SPECIFIC DEMAND CHANCES ARE MADE : !
JUNCTION NUMBER DEMAND l 13 110.00 '! 66 .00 ! 70 .00 165 .00 I 302 .00 i LINE 31 IS OPEN LINE 88 IS OPEN' LINE 92 IS OPEN LINE 97 IS OPEN LINE 101 IS OPEN LINE 109 IS OPEN f I LINE 116 IS OPEN i LINE 120 IS OPEN ' LINE 128 IS OPEN ' LINE 134 IS OPEN LINE 198 IS OPEN i i THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED I FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANCED TO 26.5 PIPE NO NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED CRADE ! 2 1 2 9.7 16.6 5.0 1.82 .00 ! 5 4 5 9.7 16.6 5.0 1.82 .00 l 198 302 165 205.0 15.3 .2 1035.00 .00 i THE RESULTS ARE OBTAINED AFTER 9 TRIALS WITH AN ACCURACY = .00285 . i U1SCNRIO CHANCE 7:RBCCWOUT CHANGE 3 SCENARIO (CALC C0050A-12 ATT 19) RUN ON ! MODEL SET UP AS UICALEN2 ' NOTE:RBCCWOUT DID NOT THROTTLE RHRSW TO 4100 CPM AS PER C0050A-12 p77;THIS DOES -i PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 LINE 1 IS CLOSED 4 0 4 7833.14 .04 102.16: .00~ 11.57 41.49 '! 16 12 13 110.00 .36 .00 .20 3.61 31.71 ! 31 27 28 49.67 .02 .00 25.37 3.77 24.46- - 34 304 305 356.99 .41 .00 1.30 9.99 86.13
- 38 36 37 72.14 .05 .00 15.82 5.47 49.82 41 ~ 38 39 70.98 .05 .00 15.32 5.39 48.30 47 41 42 72.11 .05 .00 15.81 5.47- 49.78 i 50 43 44 70.75 .05 .00 15.22 5.37 48.00 i 57 49 50 10.02 .10 .00 6.13 4.44 101.26 62 53 54 11.32 .13 .00 3.13 5.02 127.59 ,
LINE 72 IS CLOSED i LINE 73 IS CLOSED LINE 74 IS CLOSED l 79 66 70 .00 .00 .00 .00 .00 00 ' 88 84.19 74 75 .07 .00 7.61 6.39 67.02 > 1
l t i EER No. 91-0039- t Rev No. 'O i ATTACIDENT E: U1SCNRIO RESULTS FILE Page No. 23 .; 92 76 77 85.41 .07 .00 7.83 6.48 68.91 97 81 82 86.50 .07 .00 8.03 6.56 70.60 i 101 83 84 83.50 .07 .00 7.48 6.34 65.97 - 105 88 68 428.29 .93 .00 3.64 4.75 11.65 l 109 90 91 11.84 .14 .00 .43 5.25 139.14 116 96 97 11.82 .14 .00 1.28 5.24 138.64 120 100 101 65.02 .04 .00 1.51 4.93 40.84 ! 128 109 110 1032.23 .02 .00 7.94 7.54 21.99 134 115 116 986.96 .02 .00 1.61 7.21 20.17 : LINE 146 IS CLOSED ' LINE 152 IS CLOSED ! 166 143 144 1984.44 .06 729-.10 .00 12.73 56.38' ! 174 156 157 1980.09 .06 729.31 .00 12.70 56.14 : 179 148 149 41.17 3.82 .00 1.93 8.58 222.25 185 160 161 40.34 3.68 .00 1.85 8.41 213.70 ' 197 170 171 3964.53 .04 .00 .36 6.96 8.02 198 302 165 3964.53 1.64 .00 779.17 6.96 8.02 . LINE 205 IS CLOSED ' LINE 213 IS CLOSED LINE 218 IS CLOSED ! LINE 224 IS CLOSED , 233 203 204 .00 .00 .00 .00 ,00 .00 . 234 204 205 .00 .00 .00 .00 .00 .00 235 70 205 .00 .00 .00 .00 .00 .00 + 501 86 301 339.60 .02 .00 33.01 3.76 7.48 503 46 303 285.98 .03 -. 00 33.28 3.17 5.40 ; 600 17 0 872.63 .00 .00 78.60 1.03 .29 ' JUNCTION NUMBER DEMAND CRADE LINE ELEVATION PRESSURE 1 .00 105.10 43.10 27.67 2 .00 105.10 42.40 27.99 14 .00 105.10 26.50 35.08 1 15 .00 105.10 26.50 35.08 + 16 .00 105.10 26.50 35.08 18 .00 104.00 36.30 30.22 23 .00 99.50 12.50 38.83 ! 27 .00 100.19 11.00 39.81 28 .00 74.79 10.80 28.56 i 36 .00 98.02 17.50 35.94 ! 37 .00 82.17 17.50 28.86 49 .00 94.33 8.30 38.40 50 .00 88.11 8.30 35.62 i 66 .00 40.15 77.20 -16.54 i 70 .00 40.15 74.10 -15.15 ; 74 .00 94.78 17.50 34.49 : 75 .00 87.10 17.50 31.07 ! 90 .00 89.04 31.60 25.64 -l 91 .00 88.47 31.60 25.38 ; 100 .00 85.49 11.40 33.07 .; 101 .00 83.94 28.50 24.74 ; 109 .00 67.67 44.40 10.39 i 110 .00 59.71 44.40 6.83 ' 143 .00 102.31 72.80 13.17 144 .00 831.36 74.20 337.94 ! 156 .00 102.26 72.80 13.15 ! 157 .00 831.52 74.20 338.02 .i i
-)
EER No. 41-0039 .! Rev. No. O { j -ATIACHMENT E: U1SCNRIO RESULTS FILE Page No. 24 : l -a l l l i 165 .00. 41.94 58.80 -7.53 204 .00 40.15 33.10 3.15 ., 205 .00 40.15 71.90 -14.17 ! 302 .00 822.75 34.20 351.95 r 1
-I l
l THE NET SYSTEM DEMAND = 110.00 ! l
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES 1 PIPE NUMBER FLOWRATE I l 4 7833.14 1 158 -2019.19 ; 161 -4831.33 , 600 -872.63 t THE NET FLOW INTO THE SYSTEM FROM FIXED CRADE NODES = 7833.14 THE NET FLOW OUT OF THE SYSTDi INTO FIXED GRADE NODES = -7723.14 ,
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e 1 i l h EER No. 91-0039 Rev. No. O ; l ATIACHMENT E: U1SCNRIO RESULTS FILE Page No. 25 ; 1 i A SUte!ARY OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS ; L t l THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : ~' JUNCTION NUMBER DEMAND 13 167.00 i 66 .00 ! 70 .00 ! 302 4600.00 ' 165 -4600.00 i LINE 31 IS CLOSED
- LINE 88 IS CLOSED LINE 92 IS CLOSED LINE 97 IS CLOSED LINE 101 IS CLOSED LINE 109 IS CLOSED
- LINE 116 IS CLOSED '
LINE 120 IS CLOSED > LIhT 128 IS CLOSED LINE 134 IS CLOSED , LINE 198-IS CLOSED THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED i i FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANGED TO 42.0 , FOR PIPE NUMSER 4 THE VALUE OF THE FIXED GRADE IS CHANGED TO 42.0 ; FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GPADE IS CHANCED TO 116.1 FIPE NO. NODE NOS. LENGTH DIAMETER ROUCHNESS MINOR LOSS K FIXED GRADE l 2 1 2 9.7 16.6 5.0 2.41 .00 _; 5 4 5 9.7 16.6 5.0 2.41 .00 l l l 157 .00 829.57 74.20 337.15 4 ! 165 .00 42.40 58.80 -7.32 , 204 00 40.18 33.10 3.16 205 .00 40.18 71.90 14.16 302 .00 818.63 34.20 350.12 l THE NET SYSTEM DEMAND = 110.00 '
^
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED CRADE NODES PIPE NUMBER FLOWRATE 4 8559.35 : 158 -2154.27 161 -5365.61 600 -929.46 ' i l THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 8559.35 l THE NET FLOW OUT OF THE SYSTEM INTO FIXED CRADE NODES = -8449.34
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L ! l' i l j t l-EER No. 01-0039 ATIACHMENT E: U1SCNRIO RESULTS' FILE Rev. No. 0-Page No. 31 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : JUNCTION NUMBER DEMAND 13 128.00 66 4000.00- ! 70 -4000.00 302 2800.00 165 -2800.00 LINE 31 IS CLOSED LINE -38 IS CLOSED i LINE 41 IS CLOSED I LINE 47 IS CLOSED ! LINE 50 IS CLOSED LINE 57 IS CLOSED ! l' LINE 62 IS CLOSED I LINE 72 IS OPEN ' LINE 73 IS OPEN i LINE 74-IS OPEN LINE .79 IS CLOSED l LINE 88-IS CLOSED I LINE LINE 92 IS CLOSED 97 IS CLOSED j LINE 101 IS CLOSED LINE- 109 IS CLOSED { l LINE 116 IS CLOSED , LINE 120 IS CLOSED LINE 128 IS CLOSED ., LINE 134 IS CLOSED p LINE 198 IS CLOSED 3 THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANGED TO 14.0 j! FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANGED TO 14.0 i i FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANCED'TO~ 116.1 - PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED CRADE
'2 1 2 9.7 16-6
. 5.0 1.89 .00 5 4 5 9.7 16.6 5.0~ 1.89 .00 l
24 20 55 24.I 19.3 . -2 .68- .00 THE RESULTS ARE OBTAINED AFTER 3 TRIALS WITH AN ACCURACY = .00464 U1SCNRIO CHANGE 10: ALT WORST CASE MAX FLOW SCENARIO FOR NORMAL LOW BAY WATER LVL ( 6 FT); COPY OF NOVTLHDR CHANGE 14 SCENARIO RUN ON MODEL SET UP AS UICALBN2; FOR l SYSTEM LINEUP DETAILS OF NOVTLHDat CHANGE 14 SEE CALC G0050A-12 ATT 17 PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 LINE 1 IS CLOSED 4 0 4 7271.87 .04 115.83 .00 10.74 35.76 l l l l l
p , r EER No. 01-0039 Rev. No. O ! ATTACIDIENT E: U1SCNRIO RESULTS FILE Page No. 32 } l 1 i i 16 12 13 128.00 .48 .00 .27 4.20 42.88 LINE 31 IS CLOSED 34 304 305 .00 .00 .00 .00 .00 LINE .00 ;
'38 IS CLOSED LINE 41 IS CLOSED LINE 4? IS CLOSED LINE 50 IS CLOSED !
LINE 57 IS CLOSED : LINE ; 62 IS CLOSED 72 59 62 1353.84 .00 .00 2.26 2.58 1.27 73' 60 63 1315.29 .00 .00 2.13 2.51- 1.20 i 74 61 64 1330.87 .00 .00 2.18 2.54 LINE 79 IS CLOSED 1.23- . LINE 88 IS CLOSED - LINE 92 ~.S CLOSED ' LINE 97 IS CLOSED ' LINE 101 IS CLOSED 105 88 68 .00 .00 .00 .00 .00 .00 LINE 109 IS CLOSED LINE 116 IS CLOSED , LINE 120 IS CLOSED LINE I28 IS CLOSED LINE 134 IS CLOSED ' LINE 146 IS CLOSED LINE 152 IS CLOSED 166 143 144 1401.60 .03 752.61 .00 8.99 174 28.63 ! 156 157 1398.40 .03 752.71 .00 8.97 28.51 179 148 149 46.79 4.90 .00 2.50 9.75 284.83 185 160 161 45.87 4.71 .00 2.40- 9.56 273.98 e 197 170 171 2800.00 .02 -. 00 .18 '4.92 4.10 LINE 198 IS CLOSED LINE 205 IS CLOSED 'i' LINE 213 IS CLOSED LINE 218 IS CLOSED ! LINE 224 IS CLOSED 233 203 204 .00 .00 .00 .00 .00. .00 l 234 204 205 .00 .00 .00 .00 .00 .00 70 l 235 205 4000.00 .01 .00 .37 7.03 8.16-501 86 301 .00 .00 .00 .00 .00 .00 503 46 303 .00 .00 .00 .00 .00 .00 600 17 0 251.22 .00 .00 6.51 .30 .03 JUNCTION NUMBER DEMAND CRADE LINE ELEVATION PRESSURE f 1 .00 122.44 43.10 35.41 2 .00 122.44 42.40 35.73- ! 14 .00 122.44 26.50 42.82 ' 15 .00 122.61 26.50 42.90 i 16 .00 122.61 26.50 42.90 i 18 .00 120.89 36.30 37.76 ' 23 .00 120.89- 12.50 48.38 ; 27 .00 120.89 11.00 49.05' ! 28 .00 40.97 10.80 13.47 1 36 .00 120.89 17.50 46.15 37 .00 40.97 17.50 10.48 49 .00 120.89 8.30 50.25 .i 50 .00 40.97 8.30 14.58 !
l l 1 l l l EER No. 01-0039 f'
' ATTACHMENT E: U1SCNRIO RESULTS FILE Rev.-No. 0 Page No. 33 i i
1 66 4000.00 112.55 77.20 15.78 '! 70 -4000.00 41.45 74.10 14.57 : 74 .00 120.89 17.50 46.15 t 75 .00 40.39 17.50 10.22 i 90 .00 120.89 31.60 39.85 i 91 .00 40.39 31.60 3.92 ! 100 .00 120.89 11.40 48.87 I 101 .00 40.39 28.50 5.31 i 109 .00 121.75 44.40 34.52 : 110 .00 28.90 44.40 -6.92 '
.00 143 119.85 72.80 21.00 ,
144 .00 872.43 74.20 356.28 ' 156 .00 119.83 72.80 20.99 ' 157 .00 872.51 74.20 356.31 ; 165 -2800.00 41.09 58.80 -7.91 - 204 .00 41.07 33.10 3.56 205 .00 41.07 71.90 -13.76 $ 302 2800.00 S68.12 34.20 372.21 l THE NET SYSTEM DEMAND = 128.00
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES PIPE NUMBER FLOURATE 4 7271.87 l 158 .00 161 -6892.66 600 -251.22 I THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 7271 87 i THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -7143.87 i f L l l f t r.. - ,
r EER No. ~91-0039 Rev. No. ~ 0-ATTACHMENT E: U1SCNRIO RESULTS FILE .Page No. 34- l h
. A
SUMMARY
OF CONDITIONS SPECIFIl : -OR THE NEXT SIMULATION FOLLOWS i THE FOLLOWING SPECIFIC DEMAND CHANCES ARE MADE : [ JUNCTION NUMBER DEMAND 13 110.00 " 66 .00 70 .00 f 302 .00 165 .00 I LINE 79 IS OPEN - LINE '198 IS OPEN LINE 128 IS OPEN LINE 134 IS OPEN THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 600 THE VALUE OF THE FIXED CRADE IS CHANGED TO 26.5 i PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED CRADE 2 1 2 9.7 16.6 5.0 1.55 .00 , i 5 4 5 9. 7 16.6 5.0 1.55 .00 79 66 70 29.5 15.3 .2 93.02 .00 ; 198 302 165 205.0 15.3 .2 2207.61 .00 ! THE RESULTS ARE OBTAINED AFTER 7 TRIALS WITH AN ACCURACY = .00283 ! U1SCNRIO CHANGE 11:NOVTLHDR CHANGE 15 SCENARIO (CALC G0050A-12 ATT 17) RUN ON l MODEL SET UP AS UICALEN2 i. i PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000 o '~ LINE 1 IS CLOSED , THE PUMP IN LINE 4 IS OPEPATING OUT OF RANGE i 4 0 4 8524.42 .05 83.98 .00 12.59 49.12 ! 16 12 13 110.00 .36 .00 .20 3.61 31.71 l l LINE 31 IS CLOSED 34 304 305 .00 .00 .00 .00 .00 .00 ! l LINE 38 IS CLOSED i LINE 41 IS CLOSED ! LINE 47 IS CLOSED I LINE 50 IS CLOSED LINE 57 IS CLOSED LINE 62 IS CLOSED 72 59 62 1030.74 .00 .00 1.31 1.97 .76 73 60 63 1000.50 .00 .00 1.23 1,91 72~ L 74 61 64 1013.43 .00 .00 1.27 1.93 .73 1 79 66 70 3044 67 .14 .00 41.30 5.35 4.82 LINE 88 IS CLOSED LINE 92 IS CLOSED LINE 97 IS CLOSED LINE 101 IS CLOSED 105 88 68 .00 .00 .00 .00 00 .00 LINE 109 IS CLOSED 1
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t A EER No. 01-0039 ~' ATTACHMENT E: U1SCNRIO RESULTS FILE Rev. No. O I
. Page No. 35 !
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'i LINE 116 IS CLOSED ;
LINE 120 IS CLOSED 128 109 110 911.62 .02 .00 6.19- L6.66
/,
134 115 871.62 17.30. '! 116 .02 .00 1.26 6.36 15.85 LINE 146 IS CLOSED LINE 152 IS CLOSED 166 143 144 1371.65 .03 753.58 .00 8.80 174 156 27.46 1 157 1368.53 .03 753.68 .00 8.78. -27.34- ;! 179 148 149 35.51 2.87 .00 1,44 7.40 ' 185 166.99 160 161 34.80 2.76 .00 1.38 7.25 160.63 197 170 171 2740.18 .02 .00 .17 4.81 i 198 302 3.94 : 165 2740.18 .81 .00 793.94 4.81 3.94 ! LINE 205 IS CLOSED LINE 213 IS CLOSED l LINE 218 IS CLOSED 1 LINE 224 IS CLOSED 233 203 204 .00 .00 .00 .00 .00 f 234 .00 .i 204 205 .00 .00 .00 .00 .00 .00 235 70 205 3044.67 .00 .00 .21 5.35 1 501 4.82 ; 86 301 .00 .00 .00 .00 .00 .00 ! 503 46 303 .00 .00 .00 .00 .00 600 .00- l 17 0 776.03 .00 .00 62.16 .91 .23 j i JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE 1 .00 88.66 43.10 20.34. 'i 2 .00 88.66 42.40 20.65 ! 14 .00 88.66 26.50 27.75 -i 15 .00 88.66 26.50 27.75 16 .00 88.66 26.50 27.75 > 18 .00 87.20 36.30 22.72- , 23 .00 87.20 12.50 33.34 ' 27 .00 87.20 11.00 34.01 > 28 .00 40.85 10.80 13.41 i 36 .00 87.20 17.50 31.11 : 37 .00 40.85 17.50 10.42 ' 49 .00 87.20 8.30 35.21 1 50 .00 40.85 8.30 14.53 ' 66 .00 82.33 77.20 2.29 70 .00 40.88 74.10 -14.83 74 .00 87.20 17.50 31.11 : 75 .00 40.27 17.50. 10.16 I 90 .00 87.20 31.60 24.81 -l 91 -. 00 40.27 31.60 3.87 100 .00 87.20 11.40 33.83 101 .00 40.27 28.50 5.25 109 .00 59.15 44.40 6.58 110 .00 52.94 44.40 3.81 143 .00 86.26- 72.80 6.01 144 .00 839.81 74.20 341.72 i 156 .00 86.24 72.80 6.00 1 157 .00 839.89 74.20 341.75 165 .00 40.96 58.80 -7.96 204 .00 40.67 33.10 3.38 205 .00 40.67 71.90 -13.94 302 .00 835.71 34.20 357.74
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l 1 EER No. 01-0039 .I Rev. No. 0 .! ATTACI* MENT E: U15CNRIO RESULTS FILE Page No. 36 j THE NET SYSTEM DEMAND = 110.00 { I SLHMARY OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES PIPE NUMBER FLOWRATE t 4 8524.42 158 -1783.24 : 161 -5855.16 ! 600 -776.03 I t THE NET FLOW INTO THE SYSTEM FROM FIXED GRADE NODES = 8524.42 ; THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -8414.42 ; i i
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I l I l 1 t h_ o m- - a w
I l EER No. 91-0039 l Rev. No. 0 .
- . ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 37 i j
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A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS ; THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : JUNCTION NUMBER DEMAND i 66 00 'i 70 .00 302 .00 l i 165 .- 00 l i 13 113.00 LINE 31 IS OPEN { i LINE 38 IS OPEN i LINE 41 IS OPEN LINE 47 IS OPEN j LINE 50 IS OPEN ' LINE 57 IS OPEN ' LINE 62 IS OPEN ! LINE 72 IS CLOSED LINE 73 IS CLOSED ! LINE 74 IS CLOSED '; LINE 88 IS OPEN LINE 92 IS OPEN j! LINE 97 IS OPEN i LINE 101 IS OPEN 'I LINE 109 IS OPEN l LINE 116 IS OPEN ' LINE 120 IS OPEN THE FOLLOWING CHANCES IN PIPE DATA ARE SPECIFIED ! FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANGED TO 14.0 l J FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANCED TO 14.0 ] FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 26.5. PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE [ 2 2 9.7 16.6 5.0 l 1 7.73 .00 .! 5 4 5 9.7 16.6 5.0 7.73 .00 198 302 165 205.0 15.3 .2 2000.00 .00 LI q
-THE RESULTS ARE OBTAINED AFTER 6 TRIALS WITH AN ACCURACY = .00465
- .UICSNRIO CHANGE 12: WORST CASE 210' MINUTE COOLING CHECK COPY OF U2NOPOWR CHANGE.
4 SCENARIO RUN ON MODEL SET UP AS.UICALBN2.;FOR SYSTEM LINEUP DETAILS OF U2NOPOWR o
' CHANGE 4 SEE CALC G0050A-12 ATT 3; NOTE THIS RUN ONLY HAS 2 DCs(vs U2NOPOWR CH 4) '
PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP:fEAD MINOR LOSS. VELOCITY HL/1000 LINE 1 IS CLOSED 4 0 4 7095.78 03 119.50 .00 10.48 -34.05 I 16 12 13 113.00 .38 .00 .21 3.70 33.45 31 27 28 50.88 .03 .00 26.62 3.86 25.60 34 304 305 389.78 .49 .00 1.55 10.91 102.19 38 36 37 79.25 .06 .00 19.10 6.01 59.67
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EER No. 01-0039 ATTACHMENT E: U1SCNRIO RESULTS FILE Rev. No. 0 Page No. 38-41 38 39 77.98 .06 .00 18.49 5.92 57,85-47 41 42 79.22 .06 .00 19.08 6.C1 59.62 50 43 44 77.73 .06 .00 18.37 5.90- 57.48: 57 49 50 11.76 .14 .00 8.44 5.21 137.25' 62 53 54 12.97 .17 00 4.10 5.75 LINE 165.49 72 IS CLOSED LINE 73 IS CLOSED LINE 74 IS CLOSED 79 66 70 .00 .00 .00 .00 .00 .00 88 74 75 91.82 .08 .00 9.05 6.97 79.20 92 76 77 93.15 .08 .00 9.31 7.07 81.43 97 81 82 94.33 .08 .00 9.55 7.16 83.43-101 83 84 91.06 .08 .00 8.90 6.91 77.94 105 88 68 470.20 1.12 .00 4.39 5.21 109 13.93 90 91 13.58 .18 .00 .56 6.02 180.75 116 96 97 13.56 .18 .00 1.68 6.01 120 100 101 72.72 180.11.
.05 .00 1.89 5.52 50.59 128 109 110 1111.00 .03 .00 9.19 8.11 134 25.36 115 116 1062.29 .02 .00 1.87 7.76 23.25 LINE 146 IS CLOSED LINE 152 IS CLOSED 166 143 144 1463.55 .03- 750.52 .00 9.39 174 156 31.14 157 1460.23 .03 750.63 .00 9.37 31.01 179 148 149 45.38 4.62 .00 2.35 0 ^6 268~36 185 44.48 160 161 4.44 .00 2.25 '
197 170 258.13 171 2923.78 .02 .00 .20 .,.44 4.46 j 198 302 165 2923.78 .91 .00 818.89 5.14 LINE 205 IS CLOSED 4.46 l' LINE 213 IS CLOSED LINE 218 IS CLOSED LINE 224 IS CLOSED 233 203 204- .00 .00 .00 .00 .00 234 .00 204 205 .00 .00 -. 0 0 .00 .00 .00 235 70 205 .00 .00 .00 .00 .00 501 .00 86 301 370.34 .02 .00 39.26 4.11 8.82 503 46 303 314.18 .04 .00 40.17 3.4B 600 6 45 17 0 935.86 .00 .00 90.41 1.10 .33 JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE 1 .00 116,91 43.10 32.94 2 .00 116.91 42.40 33.'26 14 .00 116.91 ~26.50 40.35 15 .00 116.91 26.50 40,35 16 .00 116.91 26.50 40.35 18 .00 116.10 36.30 35.62 23 .00 110.71 12.50 43.84 27 .00 102.88 11.00 41.01 28 .00 76.23 10.80 29.20 36 .00 108.94 17.50 40.81 37 00 89.80 17.50 32.27 49 .00- 103.65 8.30 42.56 50 .00 103.88 8.30 42.66 66 .00 40.10 77.20 -16.56 70 .00 40.10 74.10 -15.18 74 .00 105;12 17.50 39.11 75 .00 95.99 17.50 35.03 .. - < - . . . . . . , . . - _ - _ . - . . _ - - - . - _ ~ - - - -
l.
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EER No. 91-0039 -l Rev. No. O ! ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 39 t l 1 90 .00 102.99 31.60 31.87 91 .00 102.25 31.60 31.53 1 100 .00 96.57 11.40 38.01 i 101 .00 94.63- 28.50 29.52 ; 109 .00 73.81 44.40 13.13 110 .00 64.59 44.40 9.01 3 ! 143 .00 115.18 72.80 18.91 l l 144 .00 865.66 74.20 353.26 ; 156 .00 115.15 72.80 18.90 e 157 .00 865.75 74.20 353.29 ; 165 .00 41.15 58.80 -7.88 ! 204 .00 40.10 33.10 3.12 !' 205 .00 40.10 71.90 -14.20 302 .00 860.96 34.20 369.01 - THE NET SYSTEM DEMAND = 113.00
.l
SUMMARY
OF INFLOWS (+) AND OUTFLOWS (-) FROM FIXED GRADE NODES I PIPE NUMBER FLOWRATE ! 4 7095.78 , 158 -2173.29 ' 161 -3873.62 600 -935.86 : i THE NET FLOW INTO THE SYSTEM FROM FIXED CRADE NODES = 7095.78' ; THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -6982.78 I i
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EER No. 01-0039 Rev. No. O ATTACHMD!T E: U1SCNRIO RESULTS FILE Page No. 40 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS J THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : JUNCTION NLMBER DEMAND 13 113.00 66 .00 70 .00 302 .00 165 .00 THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANCED TO 11.4 FOR PIPE NUMBER 4 THE VALUE OF THE FIXED CRADE IS CHANGED TO 11.4 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 2 1 2 9.7 16.6 5.0 6.48 .00 5 4 5 9.7 16.6 5.0 6.48 .00 198 302 165 205.0 15.3 .2 1900.00 .00 THE RESULTS ARE OBTAINED AFTER 2 TRIALS WITH AN ACCURACY = .00015 U1SCNRIO CHANGE 13: ALTERNATE WORST CASE >10 MINUTE C00 LNG CHECK; COPY OF U2TYF00N CHANGE 2 RUN ON MODEL SET UP AS UICALEN2;FOR SYSTEM LINEUP DETAILS OF U2TYFOON CHANGE 2 SEE CALC G0050A-12 ATT 5 PIPE NO. NODE NOS. FLOWRATE HEAD LOSS PUMP HEAD MINOR LOSS VELOCITY HL/1000-LINE 1 IS CLOSED 4 0 4 7128.60 .03 119.15 .00 10.53 34.37 16 12 13 113.00 .38 .00 .21 3.70 33.45 31 27 28 30.34 .03 .00 26.06 3.82 25.09 34 304 305 384.88 .48 .00 1.51 10.77 99.70 38 36 37 78.53 .06 .00 18.75 5.96 58.63 41 38 39 77.27 .06 .00 18.15 5.86 56.84 47 41 42 78.49 .06 .00 18.73 5.96 58.58 50 43 44 77.02 .06 .00 18.03 5.84 56.48
.57 49 50 10.91 .12 .00 7.27 4.84 119.03 62 53 54 12.32 .15 .00 3.71 5.46 '150.10 LINE 72 IS CLOSED LINE 73 IS CLOSED LINE 74 IS CLOSED 79 66 70 .00 .00 .00 .00 .00 .00 88 74 75 91.07 .08 .00 8.90 6.91 77.97.
92 76 77 92.39 .08 .00 9.16 7.01 80.16 97 81 82 93.56 .08 .00 9.39 7.10 82.13 101 83 84 90.32 .08 .00 8.75 6.85 76.73 105 88 68 462.99 1.08 .00 4.25 5.13 13.52 109 90 91 12.81 .16 .00 .50 5.68 -161.67 116 96 97 12.79 .16 .00 1.50 5.67- 161.05' 120 100 101 70.05 .05- .00 1.76 5.32 47.10 128 109 110 1102.10 .02 .00 9.05 8.05 24.97 134 115 116 1053.77 .02 .00 1.84 7.69. 22.89
EER No. 91-0030 ATTACHMENT E: U1SCNRIO RESULTS FILE Rev. No. O Page No. 41 LINE 146 IS CLOSED LINE 152 IS CLOSED 166 143 144 1498.81- .03 749.28 .00 174 9.61 32.62 156 157 1495.43 .03 749.40 .00 9.59 179 148 149 44.93 4.53 32.48'
.00 2.30 9.36 263.24 185 160 161 44.04 4.36 .00 2.21 9.18 253.20 197 170 171 2994.24 .02 .00 '.21 198 302 5.26 4.67 165 2994.24 .96 .00 815.89 5.26 4.67 LINE 205 IS CLOSED LINE .213 IS CLOSED LINF 218 IS CLOSED LINE 224 IS CLOSED 233 203 204 .00 .00 .00 .00 234
.00 .00 204 205 .00 .00 .00 .00 .00' .00 235 70 205 .00 .00 .00 .00 501
.00 .00 86 301 367.34 .02 .00 38.62 4.07 8.69 503 46 303 311.31 .04 .00 39.44 3.45 600 17 0 928.65 6.34
.00 .00 89.02 1.09 .33 JUNCTION NUMBER DEMAND GRADE LINE ELEVATION PRESSURE 1 .00 115.52 43.10 32.32 2 .00 115.52 42.40 32.64 14 .00 115.52 26.50 39.73 15 .00 115.52 26.50 39.73 16 .00 115.52 26.50 39.73 18 .00 114.70 36.30 34.99 23 .00 109.46 12.50 43.28 27 .00 101.60 11.00 40.44 28 .00 75.51 10.80 28,88 36 .00 107.72 17.50 40.27 37 .00 88.91 17.50 31.87 49 .00 103.35 -8.30- 42.42 50 .00 95.96 8.30 39.13 66 .00 40.10 77.20 -16.56 70 .00 40.10 74.10 -15.18 74 .00 103.95 17.50 38.59 75 .00 94.97 17.50 34.58 90 .00 97.21 31.60 29.28-91 .00 96.55 31.60 28.99' 100 .00 92.75 11.40 36.31 101 .00 90.95 28.50 27.87 109 .00 73.09 44.40 12.81 110 .00 64.02 44.40 8.76 143 .00 113.73 72.80 18.27 144 .00 862.98 74.20 156 352.06
.00 113.70 72.80 18.26 157 .00 863.07 74.20 352.10 165 .00 41.20 58.80 -7.86 204 .00 40.10 33.10 3.12 205 .00 40.10. 71.90 -14.19 302 .00 858.05 34.20 367.71 THE NET SYSTEM DEMAND = 113.00
SUMMARY
OF 7NFLOWS(+) AND OUTFLOWS (-) FROM FIXED GRADE NODES
4
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.EER No. 91-0039 Rev. No. O ATTACHMENT E: U1SCNRIO RESULTS FILE Page No. 42 i
PIPE NUMBER FLOWRATE l 4 7128.60 l 158 -2155.87 161 -3931.08 ! 600 -928.65 THE NET FLOW INTO TlIE SYSTEM FROM FIXED GRADE NODES = 7128.60 THE NET FLOW OUT OF THE SYSTEM INTO FIXED GRADE NODES = -7015.60 6 i { f 8 t
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I EER No. 91-0039 , Rev. No. 0 ; ATTACHMENT F: U1SCNRIO INPUT DATA FILE Page No. 1 i
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FLOWRATE IS EXPRESSED IN CPM AND PRESSURE IN PSIG A
SUMMARY
OF THE ORIGINAL DATA FOLLOWS THE DARCY WEISBACH HEAD LOSS EQUATION IS USED, THE KINEMATIC VIS. = .0000070 . THE SPECIFIC GRAVITY OF THIS LIQUID = 1.03 i PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE : (FEET) (INCHES) ! 1 0 1 1.0 16.6 5.0 .00 14.00 - i LINE 1 PUMP DATA (HEAD FLOW): 200.0 .0 135.0 6400.0 90.0 8300.0 LINE 1 IS CLOSED 2 1 2 9.7 16.6 5.0 1.83 3 2 3 15.9 18.6 5.0 2.91 i 4 0 4 1.0 16.6 5.0 .00 14.00 i LINE 4 PUMP DATA (HEAD-FLOW): 200.0 .0 135.0 6400.0 5 4 9.7 16.6 90.0 8300.0 5.0 5 1.83 ' 6 5 6 15.9 18.6 5.0 2.91
- 7 3 6 6.0 28.5 5.0 .06 i 8 6 7 6.0 -28.5 5.0 .06 l 9 7 .8 308.8 28.5 5.0 .48 l 10 8 18 371.0 28.5 5.0 .84 t 11 8 9 2.7 16.6 5.0 .33 12 9 10 63.7 17.3 .2 .60 13 10 103 124.3 16.6 5.0 .52 14 7 11 1.4 3.5 5.0 .71 !
15 11 12 3.8 3.5 5.0 3.69 ; 16 12 13 11.3 3.5 5.0 .99 ! 17 14 3 70 28.5 5.0 .06 + 18 15 14 6.1 28.5 5.0 .06 19 16 15 70 28.5 5.0 .06 'i 20 17 16 2.3 28.5 5.0 .00 21 306 19 2.3 29.3 .2 .07 22 19 21 9.1 22.5 5.0 .79 1 23 19 20 11.4 29.3 .2 1.49 24 l 20 55 24.1 19.3 .2 .68 ! 25- 18 22 28.1 6.1 .2 2.76 26 22 23 15.5 6.1 .2 .30-4 27 23 24 6.5 6.1 .2 .18 ! 28 24 25 111.6 6.1 .2 2.63 29 25 26 67.3 3.8 .2 .22 i i 30 26 27 40.8 1.7 .2 3.46 31 27 28 1.0 2.3 .2 115.00 LINE 31 IS CLOSED 32 28 29 31.5 1.7 .2 33.18 33 29 30 1.2 3.8 .2 17.02
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i f t' EER No. 91-0039 i Rev. No. O ATTACHMENT F: U1SCNRIO INPUT DATA FILE Page No. 2 34 304 305 4.8 3.8 .2 .84 35 23 32 13.1 6.1 .2 .81 i 36 33 34 1.3 3.0 .2 .54 37 34 36 8.2 2.3 .2 .
.74 38 36 37 1.0 2.3 .2 34.00.
39 37 40 7.0 2.3 .2 1.13 40 34 38 7.2 2.3 .2 1.17 41 38 39 1.0 2.3 .2 34.00 42 39 40 7.1 2.3 .2 2.03 43 40 45 5.0 3.0 .2 .69 44 32 33 5.0 6.1 .2 .48 45 33 35 2.8 3.0 .2 .79 46 35 41 9.2 2.3 .2 .74 47 41 42 1.0 2.3 .2 34.00 ' 48 42 45 7. 0 2.3 .2 2.06 49 35 43 7.9 2.3 .2 1.76 50 43 44 1.0 2.3 .2 34.00 51 44 46 8.0 2.3 .2 2.60 52 45 46 1.5 6.1 .2 .12 ' 53 303 47 20.8 6.1 .2 .93 I 54 47 30 200.0 6.1 .2 3.33 55 24 48 3.5 1.4 .2 .85 ' 56 48 49 11.0 1.0 .2 11.64 57 49 50 1.0 1.0 .2 20.00 58 50 51 17.2 1.0 .2 125.00 59 51 52 1.1 1.4 .2 .90 60 52 47 2.9 1.4 .2 1.73 l 61 48 53 19.0 1.0 .2 12.94 i 62 53 54 1.0 1.0 .2 8.00 63 54 51 9.0 1.0 .2 100.00 i 64 31 139 47.4 18.6 5.0 .08 65 22 71 125.1 6.1 .2 3.02 66 55 56 104.2 18.6 5.0 12.71 67 56 57 14.9 18.6 5.0 .60 68 57 58 5.0 18.6 5.0 .30 69 57 59 16.1 14.6 5.0 .67 ' 70 58 60 16.1 12.6 5.0 .47 71 58 61 18.3 14.6 5.0 1.02 2 72 59 62 1.0 14.6 .2 21.80
-73 60 63 1.0 14.6 .2 21.80 t 74 61 64 1.0 14.6 .2 21.80 75 62 65 12.5 15.3 .2 .51. '
76 63 65 10.9 13.3 .2 .37 j 1 77 64 66 13.3 15.3 .2 .87 78 65 66 5.7 15.3 .2 .08 79 66 70 29.5 15.3 .2 218.95 LINE :79 IS CLOSED 80 205 69 9.3 15.3 .2 .62 81 69 68 30.2 28.5 5.0 1.82 82 68 137 36.9 28.5 5.0 .04 83 71 98 51.2 6.1 .2 2.85 84 98 67- 2.9 6.1 .2 .63 85 71 72 8.2 6.1 .2 .36 86 72 300 37.1 6.1 .2 1.17 87- 73 74 9.8 2.3 .2 1.35 88 74 75 1.0 2.3 .2 12.00 LINE 88 IS CLOSED
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.i EER No. 01-0039 ,
Rev. No. 0 ' ATTACIIMENT F: U15CNRIO INPUT DATA FILE Page No. 3 l 89 75 78 7.2 2.3 .2 1,76 90 73 79 -.9 6.1 .2 .12 ' 91 79 76 8.5 2.3 .2 1.08 92 76 77 1.0 2.3 .2 12.00 t LINE 92 IS CLOSED 93 77 78 8.6 2.3 .2 1.51 94 78 85 4.7 3.0 .2 .57 i 95 79 80 1.2 3.0 .2 1.13 96 80 81 9.1 2.3 .2 1.01 < 97 31 82 1.0 2.3 .2 12.00 ' LINE 97 IS CLOSED 98 82 85 7.5 2.3 .2 .81 l 99 85 86 4.2 6.1 .2 .42 ! 100 80 83 9.2 2.3 .2 1.35 101 83 84 1.0 2.3 .2 12.00 LINE 101 IS CLOSED ; 102 84 86 8.4 2.3 .2 1.62 ! 103 301 87 27.5 6.1 .2 1.17 ! 104 87 88 606.1 6.1 .2 4.82 105 88 68 80.2 6.1 .2 10.40 ' 106 72 102 12.5 1.7 .2 .60 ; 107 102 89 2.9 1.4 .2 .73 108 89 90 13.0 1.0 .2 12.28 109 90 91 1.0 1.0 2 1.00 i LINE 109 IS CLOSED 110 91 92 24.0 1.0 .2 75.00 111 92 93 .9 1.4 .2 .22 l 112 93 94 2.9 1.4 .2 1.35 I 113 94 95 18.7 1.7 .2 1.20 ; 114 95 87 .9 1.7 .2 1,67 115 89 96 20 3 1.0 .2 12.46 116 96 97 1.0 1.0 .2 3.00 LINE 116 IS CLOSED i 117 97 92 11.2 1.0 .2 75.00 1 138 98 99 101.9 3.8 .2 1.46 1 119 99 100 35.0 1.7 .2 3.57 120 100 101 1.0 2.3 .2 4.00 ) LINE 120 IS CLOSED l
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121 101 88 34.5 2.3 .2 . 100.00 j 122 120 104 31.0 16.6 5.0 .89 ' 123 104 105 5.4 '16.6 5.0 .89 1 124 105 106 .8 16.6 5.0 .00 i 125 104 107 56.3 5.6 5.0 4.01 126 107 108 12. 7 5.6 5.0 .73 127 108 109 1.9 7.5 5.0 .76 128 109 110 1.0 7.5 .2- 9.00 LINE 128 IS CLOSED 129 110 111 1.9- 7.5 5.0 .98 130 111 112 79.0 5.6 5.0 3.28 131 105 113 79.8 5.6 5.0 4.34 132 113 114 12.0 5.6 5.0 .73 133 114 115 1.9 7.5 5.0 .76 134 115 116 1.0 7.5 .2 2.00 LINE 134 IS CLOSED i i 135 116 117 1.9 7.5 5.0 .98 t 136 117 118 100.4 5.6 5.0 3.61 137 119 118 .8 16.6 5.0 .00 l l
EER No. 91-0039 ATTACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. O Page No. 4 138 118 112 .8 16.6 5.0 .07 139 112 136 26.8 16.6 5.0 .45 140 103 120 18.9 16.6 5.0 35.41 141 103 121 12.0 16.6 5.0 35.41 142 121 122 3.1 5.6 5.0 .00 143 120 123 58.0 5.6 5.0 4.00 144 123 124 13.7 5.6 5.0 .73 145 124 125 1.7 7,5 5.0 .76 146 125 126 1.0 8.0 .2 9.00 LINE 146 IS CLOSED 147 126 127 1.9 7.5 5.0 1.48 ' 148 127 128 74.8 5.6 5.0 2.68 149 121 129 54.5 5.6 5.0 4.01 150 129 130 16.3 5.6 5.0 .91 151 130 131 1.7 7.5 5.0 .50 152 131 132 1.0 8.0 .2 9.00 LINE 152 IS CLOSED ' 153 132 133 1.9 7.5 5.0 .98 + 154 133 134 75.7 5.6 5.0 3.28 i 155 135 134 2.3 16.6 5.0 .00 ' 156 134 128 30.8 16.6 5.0 .07 157 128 136 4.3 16.6 5.0 .45 158 136 0 414.1 16.6 5.0 .96 159 28.90 137 138 16.4 28.5 5.0 .92 160 139 138 126.7 18.6 5.0 .64 2 161 138 0 286.2 34.5 5.0 1.13 40.00 162 21 140 27.2 22.5 5.0 .20 163 140 141 6.5 12.6 5.0 .34 164 141 142 4.3 12.6 5.0 .12 165 142 143 4.3 8.0 .2 .32 166 1.0 8.0 143 144 .2 .00 i LINE 166 PUMP DATA (HEAD-FLOW): 775.0 .0 580.0 4000.0 500.0 4725.0 167 144 145 9.9 12.0 .2 3.76 168 145 146 16.7 i 12.0 .2 .93 169 140 153 16.0 22.5 5.0 .06 i 170 153 173 21.5 22.5 5.0 .30 l 171 153 154 6.5 12.6 5.0 .44 'l 172 154 155 4.3 12.6 5.0 .12 173 155 156 4.3 8.0 .2 .32 l 174 156 157 1.0 8.0 .2 .00 'i i LINE 174 PUMP DATA (HEAD-FLOW): 775.0 .0 580.0 4000.0 500.0 4725.0 1 175 157 158 9.8 12.0 .2 3.76 176 158 '146 31.4 -! 12.0 .2 1.07, i 177- 141 147 .8 1.7 .2 .20 178 147 148 .5 1.7 .2 .07 179 148 149 17.2 1.4 .2 1,69 180 149 150 .7 1.7 .2 26.27 181 150 151 2.2 1.4 .2 27.12 182 151 152 19.9 1.4 .2 2.42 183 154 159 .8 1.7 5.0 .69 184 159 160 .5 1.7 .2 .07 185 160 161 17.2 1.4 .2 -1.69 186 161 162 1.0 1.7 .2 26.57 187 162 163 2.7 1.4 .2 28.70 188 163 164 19.9 1.4 - .2 2.21 1 189 193 164 21.2 3.0 .2 .32 i 190 164 152 16.7 3.0 .2 .54 j i
ia l l EER No. 91-0039 j ATTACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. O i' Page No. 5 i f 191 152 -165 117.8 3.0 .2 4.45~ i 192 146 166 156.0 16.0 .2 h 1.15 193 166 167 18.7 16.0 .2 44 ' 1 194 167 168 10.5 15.3 .2 .14 ' 195 168 169 2.5 15.3 .2 .00 196 169 170 1.0 19.3 .2 11.50
- 1. 197 170 171- 5.0 15.3 .2 .48 198 302 165 205.0 15.3 .2 759.63 LINE 198 IS CLOSED ,
199 165 172 7.5 19.3 .2 .00 200 172 31 31.0 18.6 5.0 .07 , 201 173 174 1.0 12.6 5.0 .00 202 174 175 4.7 13.3 .2 !
.10 203 175 176 4.3 13.3 .2 .12 '
204 176 177 4.2 8.0 .2 .32 205 177 178 1.0 8.0 .2 .00 LINE 205 PUMP DATA (HEAD-FLOW): 775.0 .0 580.0 4000.0 500.0 '4725.0 LINE 205 IS CLOSED ; 206 178 179 9.8 12.0 .2 1 207 3.76 - 179 180 27.9 12.0 .2 .46 208 173 181 16.0 22.5 5.0 a 209 181 182
.12 !
.4 12.6 5.0 .00 210 182 183 4.8 13.3 .2 .00
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211 183 184 4.4 13.3 .2 .12 } 212 184 185 4.2 8.0 .2 .32 213 185 186 1.0 8.0 .2 .00 ! LINE 213 PUMP DATA (HEAD FLOW): 775.0 .0 580.0 4000.0- 500.0 4725.0 LINE 213 IS CLOSED l 214 186 187 10.4 12.0 .2 3.76 -l 215 187 180 17.4 12.0 .2 .29 t 216 175 188 1.0 1.7 .2 .49 I 217 188 189 .3 1.4 .2 .07 1 218 189 190 16.9 1.4 .2 1.69 LINE 218 IS CLOSED 'l 219 190 191 1.0 1.7 .2 25.00 _l 220 191 192 2.3 1.4 .2 3 221 192 193 15.00 19.5 1.4 2 2.44 i 222 183 194 .4 1.7 2 .49 223 194 195 .7 1.4 .2 .07 224 195 196 16.4 1.4 .2 1.69 LINE 224 IS CLOSED l 225 196 197 1.0 1.7 .2 10.00 j 226 197 198 2.9 1.4 .2 15.00' 227 198 193 39.2 1.4 .2 5.21
-228 180 199 212.5 15.3 .2 1.33 229 199 200 2.5 15.3 .2 .25 I
230 200 201 2.5 19.3 .2 .00 231 201 202 1.0 19.3 232 202 203 .2 11.50 J 2.5 19.3 .2 .19 e 233 203 204 2.5 15.3 .2 .00 234 204 205 235.1 15.3 .2 -1814.60 I 70 205 235 .7 15.3 500 300
.2 .48 73 4.8 .6.1 .2 .76 501 B6 301 2.3 6.1 .2 502 171- 302 .4 150.00 !
15.3 .2 .00 503 46 303 5.8 6.1 .2 213.26 1 504- 30 304 1.5 3.8 .2 .00 i e l t
EER No. 91-0039 ATTACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. O Page.No. 6 505 305 31 32.9 5.6 5.0 1.94 506 18 306 103.8 28.5 5.0 .08 600 17 0 1. 0 18.6 5.0 4800.00 116.10 A SUCCESSFUL CE0 METRIC VERIFICATION HAS BEEN COMPLETED JUNCTION NUMBER DEMAND ELEVATION CONNECTING PIPES 1 .00 43.10 1 2 2 .00 42.40 2 3 3 .00 26.50 3 7 17 4 .00 43.10 4 5 5 .00 42.40 5 6 6 .00 26.50 6 7 8 7 .00 26.50 8 9 14 8 .00 26.50 9 10 11 9 .00 29.20 11 12 10 .00 31.80 12 13 11 .00 24.60 14 15 12 .00 24.60 15 16 13 118.00 24.60 16 14 .00 26.50 17 18-15 .00 26.50 18 19 16 .00 26.50 19 20 17 .00 26.50 20 600 18 .00 36.30 10 25 506 19 .00 81.50 21 22 23-20 .00 81.50 23 24 21 .00 81.50 22 162 22 .00 .19.10 25 '26 65 23 .00 12.50 26 27 35 24 .00 12.50 27 28 55 25 .00 .33.80 28 29 26 .00 34.50 29 30 27 .00 11.00 30 31 28 .00 10.80 31 32 29 .00 32.30 32 33 30 .00 23.20 33 54 504 31 .00 35.50 64 200 505 32 .00 12.50 35 44 33 .00 12.50 36 44 45 34 .00 12.50 36 37 40 35 .00 12.50 45 46 -49 36 .00 17.50 37 38' 37 .00 17.50 38 39 38 .00 17.50 40 41 39 .00 17.50 41 42 40 .00 14.20 39 -42 43 41 00 17.40 46 47 42 .00 17.40 47 48 43 .00 17.40 49 50 44 .00 17.40 50 51 45 .00 14.20 43 48 52 46 .00 14.20 51 52 503 47 .00 10.80 53 54 60 48 .00 12.50 55 56 61 49 .00 8.30 56 57
EER No. 01-0039 Rev. No. O ATTACHMENT F: U1SCNRIO INPUT DATA FILE Page No. 7 50 .00 8.30 57- 58 51 .00 10.80 58 59 63 52 .00 10.80 59 60 53 .00 8.30 61 62 54 .00 8.30 62 63 55 .00 81.50 24 66 56 .00 S1.50 66 67 57 .00 79.00 67 68 69 58 .00 79.00 68 70 71 59 00 74.80 69 72 60 .00 74.80 70 73 61 .00 74.80 71 74-62 .00 74.80 72 75 63 .00 74.80 73 76 64 .00 74.80 74 77 65- .00 77.20 75 76 78 66 4000.00 77.20 77 78 79 67 .00 16.80 84 68 .00 35.50 81 82 105 69 .00 65.80 80 81 70 -4000.00 74.10. 79 235 71 .00 .10 65 83 85 72 .00 .10 85 86 106 73 .00 16.10 87 90 500 74 00 17.50 87 88 75 .00 17.50 88 89 76 .00 17.50 91 92 77 .00 -17.50 92 93 78 .00 14.20 89 93 94 79 .00 16.10 90 91 95 80 .00 16.10 95 96 100 81 .00 17.40 96 97 82 .00 17.60 97~ 98 l 83 .00 17.40 100 101 ! 84 .00 17.60 101 102 ' 85 .00 14.20 94 98 99 86 .00 14.20 99 102 501 87 .00 20.90 103 104 114 88 .00 33.20 104 105 121 89 .00 14.20 107 108 115 90 .00 31.60 108' 109 91 .00 31.60 109 110 92 .00 12.10 110 111 117 93 .00 12.10 111 112 94 .00 23.00 112 113 95 .00 21.00 113 114 96 .00 8.30 115 116 97 .00 8.30 116 117 98 .00 16.80 83 84 118 99 .00 34.50 118 119 100 .00 11.40 119 120 101 00 28.50 120 121 102 .00 14.20 106 107 103 .00 34 50 13 140 141 104 .00 34.50 122 123 125 105 .00 34.50 123 124 131 106 .00 34.50 124
i t EER No. 91-0039 I Rev. No. O ! ATTACHMENT F: U1SCNRIO INPUT DATA FII.E Page No.. 8 i [ t 107 .00 43.80 125 126 t 108 .00 42.90 126 127 I 109 .00 44.40 127 128 ; 110 .00 44.40 128 129- i 111 .00 44.50 129 130 ; 112 .00 34.50 130 138 139 t 113 .00 43.80 131 132 ! 114 .00 42.90 132 133 ? 115 .00 44.40 133 134 116 .00 44.40 134 135 117 .00 44.30 135 136 118 .00 34.50 136 137 138 ! 119 .00 34.50 137 120 .00 34.50 ( 122 140 143 _; 2 121 .00 34.50 141 142 149 7 122 .00 34.50 142 I 123 .00 47.30 143 144 ! 124 .00 43.80 144 145 125 .00 44.40 145 146 i 126 .00 44.40 146 147 ! 127 .00 43.80 147 148 .; 128 .00 34.50 148 156 157 129 .00 i 43.80 149 150 t 130 .00 43.80 150 151 131 .00 44.40 151 152 132 .00 44.40 152 153 l 133 .00 43.80 153 154 ' 134 .00 34.50 154 155 156 i 135 .00 34.50 155 i 136 .00 34.50 139 157 158 137 .00 ! 19.30 82 159 , 138 .00 19.30 159 160 161 ! 139 .00 19.30 64 160 ! 140 .00 81.50 162 163 169 l 141 .00 75.00 163 164 177 i 142 .00 72.80 164 165 l 143 .00 72.80 165 166 ; 144 .00 74.20 166 167 ; 145 .00 77.53 167 168 ! 146 .00 81:.20 168 176 192 i 147 .00 7 '.: 30 177 178 148 .00 7S.00 178 179 149 .00 73.80 179 180 150 .00 73.90 180 181 151 .00 74.30 181 182 152 .00 63.50 182 190 191 153 .00 81.50 169 170 171 154 .00 75.00 171 172. 183 155 .00 72.80 172 173 156 .00 72.80 173 174 157 .00 74.20 174 175 158 .00 77.50 175 176 159 .00 75.00 183 184 160 .00 75.00 184 .185 161 .00 73.80 185 186 162 .00 73.90 186 187 163- .00 .74.30 187 188 i
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i EER No. 91 0039 Rev. No. O i ATTACHMENT F: U1SCNRIO INPUT DATA FILE Page No. 4 r 164 .00 63.50 188 189 190 ' 165 -2800.00 58.80 191 198 199 , 166 .00 46.80 192 193 167 .00 34.20 193 194 6 168 .00 34.20 194 195 169 .00 34.20 195 196 -! 170 . 00 34.20 196 197 f 171 .00 34.20 197 502 172 .00 51.00 199 200 173 .00 81.50 170 201 208 , 174 .00 79.60 201 202 ! 175 .00 75.00 202 203 216 ' 176 .00 72.80 203 204 177 .00 72.80 204 205 ' 178 .00 74.10 205 206 179 .00 77.50 206 207 180 .00 77.50 207 215 228 181 .00 81.50 208 209 182 .00 79.80 209 210 183 .00 75.00 210 211 222-184 .00 72.80 211 212 185 .00 72.80 212 213 186 .00 74.10 l 213 214 - 187 .00 77.50 214 215 188 .00 75.00 216 217 l 189 .00 75.00 217 218 ' 190 .00 73.40 218 219 ! 191 .00 73.40 219 220 192 .00 74.30 220 221 193 .00 63.50 189 221 227 ! 194 .00 75.00 222 223 ! 195 A .00 75.00 223 224 ' 196 .00 73.40 224 225 197 .00 73.40 225 226 ! 198 .00 74.08 226 227 ; 199 .00 33.10 228 229 ; 200 .00 33.10 229 230 l l- 201 .00 33.10 230 231 ' j 202 .00 33.10 231 232 I l 203 .00 33.10 232 233- ! 204 .00 33.10 233 234 ! 205 .00 71.90 80 234 235 : 300 .00 16.00 86 -500 t l- 301 .00 14.20 103 501 i i 302 2800.00 34.20 198 502 303 .00 12.50 53 503 l 304 .00 33.20 34 504 ! 305 .00 33.20 34 505 306 .00 81.50 21 506 OUTPUT SELECTION: THE FOLLOWING RESULTS ARE OUTPUT RESULTS ARE OUTPUT FOR ALL PIPES WITH PUMPS - CLOSED PIPES ARE NOTED RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES - 1 4 16 31 34 38 41 47 50 57 62 ' 72 73 74 79 88 92 97 101 105 RESULTS 197 198 205ARE 213OUTPUT 218 224 FOR THE235 233 234 FOLLOWING PIPES : 109 116 120 128 134 146 152 166 174 179 185 RESULTS ARE OUTPUT FOR THE FOLLOWING PIPES : 501 503 600 l l
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l i i EER No. 01-0039 I ATTACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. 0 Page No. 10 t i i t RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTICN NODES . 1 2 14 15 16 27 28 36 37-49 50 66 70 74 75 , RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES : 90 157 18 23 204 205 302 91 100 101 109 110 143 144 156-RESULTS ARE OUTPUT FOR THE FOLLOWING JUNCTION NODES 165 THIS SYSTEM HAS 243 PIPES WITH 212 JUNCTIONS , 27 LOOPS AND 5 FGNS . TERMINATION DUE EITHER TO THE DETECTION OF AN ERROR OR USER INSTRUCTIONS , I A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS j THE FOLLOWING SPECIFIC DEMAND CHANCES ARE MADE : JUNCTION NUMBER DEMAND ' 13 110.00 . 66 .00 ; 70 .00 165 .00 ! 302 .00 LINE 31 IS OPEN i LINE 79 IS OPEN LINE BB IS OPEN LINE 92 IS OPEN : LINE 97 IS OPEN LINE 101 IS OPEN f! LINE 109 IS OPEN LINE 116 IS-OPEN i LINE 120 iS OPEN 'l LINE 128 IS OPEN -t LINE 134 IS OPEN , LINE' 198 IS OPEN THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED t FOR PIPE NUMBER 600 THE VALUE OF THE FIXED CRADE IS CHANCED TO 26.5 I r PIPE 2 NO. NODE NOS. LENGTH 9.7 DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE. 1 2 16.6 5.0 1.59 .00 5 4 5 9.7 16.6- 5.0 1.59 .00 24 20 55 24'.1 19.3 .2 79 7') 420.08 .00-66 29.5 15.3 .2 85.93 .00 198 302 165 205.0 15.3 .2 i 2192.66 .00 i I i f i
f I t EER No. 91-0039 , Rev..Ne,. 0 , ATTACHMENT F: U1SCNRIO INPUT DATA FILE Page L. 11 , e A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS : THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : 1 JUNCTION NUMBER DEMAND 66 4000.00 70 4000.00 i 302 2800.00 ' 165 -2800.00 , 13 124.00 l LINE 31 IS CLOSED ' LINE 79 IS CLOSED LINE 88 IS CLOSED l LINE 92 IS CLOSED l LINE 97 IS CLOSED -[ LINE 101 IS CLOSED t LINE 109 IS CLOSED LINE 116 IS CLOSED , LINE 120 IS CLOSED ! LINE 128 IS CLOSED LINE- 134 IS CLOSED , LINE 198 IS CLOSED l' THE FOLLOWING CHANCES IN PIPE DATA ARE SPECIFIED l_ FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANGED TO 22.0
- FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANCED TO 22.0 .!
FOR PIPE NUMBER 600 THE VALUE OF THE FIEED CRADE IS CHANGED TO 116.1 - i PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 2 1 2 9.7 16.6 5.0 1.78 .00 5 4 5 9.7 16.6 5.0 1.78 .00 24 20 55 24.1 19.3 .2 .68 .00 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS THE FOLLOWING SPECIFIC DEMAND CHANCES ARE MADE : JUNCTION NUMBER DEMAND 66- .00 I 70 .00 ! 302 .00 1 165 .00 1 13 110.00 LINE 31 IS OPEN l LINE 88 IS OPEN LINE 92 IS OPEN LINE 97 IS OPEN l LINE 101 IS OPEN l LINE 109 IS OPEN ! LINE 116 IS OPEN
EER No. 01-0039 ATTACHMENT F: UlSCNRIO INPUT DATA FILE Rev. No. O ; Page No. 12 i LINE 120 IS OPEN > LINE 128 IS OPEN LINE 134 IS OPEN [ LINE 79 IS OPEN LINE 198 IS OPEN i THE FOLLOWING CHANCES IN PIPE DATA ARE SPECIFIED , FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 26.5 PIPE 2 NO. NODE NOS. LENGTH DIAMETER FOUGHNESS MINOR LOSS R FIXED CRADE 1 2 9.7 16.6 5.0 1.56 .00 5 4 5 9.7 16.6 5.0 1.56 .00 24 20 SS 24.1 19.3 .2 79 420.08 .00 66 70 29.5 15.3 .2 91.88 .00 198 302 165 205.0 15.3 .2 2204.74 .00 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS b THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : ', JUNCTION NUMBER DEMAND ' 13 168.00 > 66 4000.00 70 -4000.00 302 2800.00 165 -2800.00 ! LINE 31 IS CLOSED LINE 38 IS CLOSED ' LINE 41 IS CLO5ED LINE 47 IS CLOSED LINE 50 IS CLOSED , LINE 57 IS CLOSED LINE 62 IS CLOSED LINE 79 IS~ CLOSED > LINE 88 IS CLOSED LINE 92 IS CLOSED LINE 97 IS' CLOSED LINE 101 IS CLOSED LINE 109 IS CLOSED LINE 116 IS CLOSED LINE 120 IS CLOSED l LINE 128 IS CLOSED LINE 134 IS CLOSED f LINE 198 IS CLOSED THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 1 THE VALUE OF THE FIXED CRADE IS CHANGED TO 42.0 ! FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANGED TO 42.0 FOR-PIPE NUMBER 600 THE VALUE OF THE FIXED CRADE IS CHANCED TO 116.1 i
)
l ; l l EER No. 91-0039 i ATIACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. O I Page No. 13 h i PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE j 2 1 2 9.7 16.6 5.0 1.79 .00 4 9.7 1 5 5 16.6 5.0 1.79 .00 ! 24 20 55 24.1 19.3 .2 .68 .00 ! i i A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS i i THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : ( JUNCTION NUMBER DEMAND ? 13 110.00 ' 66 .00 70 4
.00 l- 302 .00 i l 165 .00 LINE 79 IS OPEN LINE 128 IS OPEN '
LINE 134 IS OPEN LINE 198 IS OPEN ' l THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED ' FOR PIPE NUMBER 600 THE VALUE OF THE FIXED CRADE IS CHANGED TO 26.5 ) i PIPE NO. NODE NOS.-LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE [ 2 1 2 9.7 16.6 5.0 1.47 .00 ! 5 4 5 9.7 16.6 5.0 1.47 79 66 70 .00 1 29.5 15.3 .2 119.25 .00 ' 198 302 165 205.0 15.3 .2 2261.08 .00 i e A
SUMMARY
OF' CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : i JUNCTION NUMBER DEMAND
-i' 13 179.00 66 .00 70 .00 -
302 4100.00 ' 165 -4100.00 LINE- 38 IS OPEN LINE 41 IS OPEN LINE 47 IS OPEN. LINE 50 IS OPEN LINE 57 IS OPEN ! LINE 62 IS OPEN ' LINE 72 IS CLOSED ' LIhT 73 IS CLOSED
i EER No. 91-0039 ATTACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. 0 ' Page No. 14 LINE 74 IS CLOSED LINE 128 IS CLOSED LINE 134 IS CLOSED LINE 198 IS CLOSED THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED ' FOR PIPE NLHBER 1 THE VALUE OF THE FIXED CRADE IS CHANCED TO 11.4 ' FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANGED TO 11.4 FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANCED TO 116.1
.i PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE ,
2 1 2 9.7 16.6 5.0 2.77 .00 i 5 4 5 9.7 16.6 5.0 2.77 .00 1 1 1 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS i THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : i JUNCTION NUMBER DEMAND i l 13 110.00 66 .00 l 70 .00 -! l 165 .00 ' 302 .00 LINE 31 IS OPEN LINE 88 IS OPEN LINE 92 IS OPEN I LINE 97 IS OPEN LINE 101 IS OPEN ' LINE 109 IS OPEN ' LINE 116 IS OPEN LINE 120 IS OPEN : i LINE 128 IS OPEN LINE 134 IS OPEN LINE 198 IS OPEN i THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED j FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 26.5 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GPADE 2 1 2 9.7 16.6 5.0 l'.82 .00 J 5 4 5 9.7 16.6 5.0 1.82 .00 198 . 302 165 205.0 15.3 .2 1035.00 .00 l l A SLHMARY OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS l 1
1 i i l EER No. 01-0039 ' ATTACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. O Page No. 15 l i i THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : 1i JUNCTION NUMBER DEMAND 13 167.00 66 .00 I 70 .00 302 4600.00 1 165 -4600.00 .., LINE 31 IS CLOSED LINE 88 IS CLOSED LINE 92 IS CLOSED ! LINE 97 IS CLOSED l i LINE 101 IS CLOSED , LINE 109 IS CLOSED LINE 116 IS CLOSED LINE 120 IS CLOSED' I LINE 128 IS CLOSED LINE 134 IS CLOSED LINE 198 IS CLOSED l THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANCED TO 42.0 FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANGED TO 42.0 FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANCED TO 116.1 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 2 1 2 9.7 16.6 5.0 2.41 .00 5 4 5 97 16.6 5.0 2.41 .00 i i A
SUMMARY
OF CONDITIONS SPECIFIED FOR.THE NEXT SIMULATION FOLLOWS THE FOLLOWING SPECIFIC DEFAND CHANGES ARE MADE : JUNCTION NUMBER DEMAND 13- 110.00 66- .00 70 .00 i 165 .00 ' 302 .00 LINE 31 IS OPEN LINE 88 IS OPEN LINE' 92 IS OPEN I LINE 97 IS OPEN ' LINE 101 IS OPEN LINE 109 IS OPEN LINE 116 IS OPEN l LINE 120 IS OPEN LINE 128 IS OPEN LINE 134 IS OPEN 4
r EER No. 91-0039 l ATTACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. O i Page No. 16 LINE 198 IS OPEN THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 26.5 PIPE NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE 2 1 2 9.7 16.6 5.0 1.54 .00 5 4 5 9.7 16.6 5.0 1.54 .00 198 302 165 205.0 15.3 .2 822.68 ., 00 A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE : JUNCTION NUMBER DEMAND , 13 128.00 66 4000.00 70 -4000.00 i 302 2800.00 165 -2800.00 LINE 31 IS CLOSED LINE 38 IS CLOSED LINE 41 IS CLOSED LINE 47 IS CLOSED LINE 50 IS CLOSED LINE 57 IS CLOSED LINE
~
62 IS CLOSED LINE 72 IS OPEN LINE 73 IS OPEN LINE 74 IS OPEN LINE 79 IS CLOSED LINE 88 IS CLOSED LINE 92 IS CLOSED - LINE 97 IS CLOSED LINE- 101 IS CLOSED LINE 109 IS CLOSED LINE 116 IS CLOSED LINE 120 IS CLOSED ! LINE- 128 IS CLOSED LINE 134 IS CLOSED LINE 198 IS CLOSED THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS ' CHANCED TO '14.0 FOR PIPE-NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANGED TO 14.0 FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 116.1 PIPE NO. NODE NOS. LENGTH- DIAMETER ROUGHNESS MINOR LOSS K FIXED CRADE i g
I EER No. _91-0039 AITACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. O Page No, 17 t 2 1 2 9.7 16.6 5.0 1.89 .00 5 4 5 9.7 16.6 5.0 1.89 .00 24 20 55 24.1 19.3 .2 .68 .00' A
SUMMARY
OF CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS l THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE - JUNCTION NUMBER DEWWD ' 13 110.00 l 66 .00 70 .00 302 .00 165 .00 l LINE 79 IS OPEN I LINE 198 IS OPEN LINE 128 IS OPEN I LINE 134 IS OPEN THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED I $ FOR PIPE NUMBER 600 THE VALUE OF THE FIXED CRADE IS CHANGED TO '26.5 j
.J l
PIPE2 NO. NODE NOS. LENGTH 9.7 DIAMETER 16.6 ROUGHNESS MINOR LOSS K FIXED GRADE ' 1 2 5.0 1.55 5 4 9.7 .00 :! 5 16.6 5.0 1,55 .00 79 66 70 29.5 15.3 .2 l 198 93.02 .00 ' 302 165 205.0 15.3 2207.61 2 .00. A
SUMMARY
OF. CONDITIONS SPECIFIED FOR THE NEXT SIMULATION FOLLOWS i THE FOLLOWING SPECIFIC DEMAND CHANGES ARE MADE . JUNCTION NUMBER DEMAND 1 66 J! l- .00 70 .00 302 .00 165 .00 13 113.00 LINE 31.IS OPEN LINE 38 IS OPEN LINE 41 IS OPEN LINE' 47 IS OPEN LINE 50 IS OPEN LINE 57 IS OPEN LINE 62 IS OPEN
'LINE 72 IS CLOSED LINE 73 IS CLOSED LINE 74 IS CLOSED LINE 88 IS OPEN 1 i
j l l i 1'
i EER No. 91-0039 ATTACHMENT F: U1SCNRIO INPUT DATA FILE Rev. No. O _ ) Page No. 18
'l LINE 92 IS OPEN LINE 97 IS OPEN i LINE 101 IS OPEN
- LINE 109 IS OPEN LINE 116 IS OPEN '
LINE 120 IS OPEN 'I THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR PIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANGED TO 14.0 l FOR PIPE NUMBER .) 4 THE VALUE OF THE FIXED GRADE IS CHANGED TO 14.0 : FOR PIPE NUMBER 600 THE VALUE OF THE FIXED GRADE IS CHANGED TO 26.5 _l PIPE 2 NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE ! 1 2 9.7 16.6 5.0 7.73 .00 5 4 5 9.7 16.6 5.0 7.73 .00- .; e 198 302 165 205.0 15.3 .2 2000.00 .00
.'e h
I A
SUMMARY
OF CONDITIONS SPECIFIED FOR TE NEXT SIMULATION FOLLOWS. ; THE FOLLOWING SPECIFIC DEMAND CHANGES ARE PADE : JUNCTION NUMBER DEMAND 13 113.00 i 66 .00 i 70 .00 3 302 .00 165 .00 ! THE FOLLOWING CHANGES IN PIPE DATA ARE SPECIFIED FOR FIPE NUMBER 1 THE VALUE OF THE FIXED GRADE IS CHANGED TO 11.4 . t FOR PIPE NUMBER 4 THE VALUE OF THE FIXED GRADE IS CHANCED TO 11.4 ! PIPE 2 NO. NODE NOS. LENGTH DIAMETER ROUGHNESS MINOR LOSS K FIXED GRADE ! 1 2 9.7 16.6 5.0 6.48 .00 I 5 4 5 9.7 16.6 5.0 6'.48 .00 198 302 165 205.0 15.3 .2 -j 1900.00 .00 e 1 l J}}