ML102570084
| ML102570084 | |
| Person / Time | |
|---|---|
| Site: | Peach Bottom  |
| Issue date: | 11/19/2009 |
| From: | Wagner R Exelon Nuclear |
| To: | Office of Nuclear Reactor Regulation |
| References | |
| TAC ME4131, TAC ME4132 CC-AA-309-1001, Rev 5 | |
| Download: ML102570084 (91) | |
Text
{{#Wiki_filter:ATTACHMENT ATTACHMENT PEACH BOTTOM BOTTOM ATOMIC POWER POWER STATION STATION UNITS UNITS 2 AND 3 NRC Docket Nos. 50-277 50-277 and 50-278 50-278 Renewed Facility Operating License License Nos. DPR-44 and DPR-56 DPR-56 Calculation PM-0375, Revision 4, "To Establish Calculation Establish Limiting Demand for N Limiting Demand N22 for the CAD System and the SGIG System for Dual Unit Operation" Dual Unit Operation"
CC-AA-309-1001 Exelkn. CC*AA*309*1001 Revision 5 Page 1 of 1 Nuclear Nuclear ATTACHMENT ATTACHMENT 1 Design Analysis Major Major Revision Cover Sheet Sheet Design Analysis Analysis (Major (Major Revision) II Last Page Page No.6No.I Attachment IIIIpage 9 Analysis No.: No.:'
- PM-0375 Revision: 22 Revision: 4
Title:
3 To establish establish limiting demand demand for N2 N2 for the CAD system and the SGIG system for dual unit unit operation EC/ECR EC/ECR No.:
- 09-00416 Revision: 5 Revision:1 0 Station(s):
Station(s): 7 Peach Bottom Component(s): ** "4 Component(s): Unit No.: 68 22&3
&3 00T116 00T116 Discipline:
Discipline: 9 Mechanical Oescrip. Code/Keyword: Descrip. Code/Keyword: 10
'0 N/A N/A Safety/QA Class: "11 Safety/QA Q, Safety System Code: **2 07C, 16, 912 912 Structure: ,3 Structure: '3 N/A N/A CONTROLLED CONTROLLED DOCUMENT REFERENCESs15 DOCUMENT REFERENCES Document No.: From/To From/To Document Document No.: From/To From/To PM-0374 From PM-0804 PM-0804 To PM-0386 From SR 3.6.1.3.1 To To PE-0063 From SR 3.6.1.5.1 To To SR 3.6.3.1.2 SR 3.6.3.1.2 To To Is this Design Analysis Safeguards Information? .8, Safeguards Information? Yes [] 0 No ZI2J IfIfyes, see SY-AA-101-106 SY-AA-101-106 Does this Design Analysis contain Unverified Assumptions?"17 Unverified Assumptions? Yes El 0 No No I2JZ yes, ATI/AR#:
IfIfyes, ATIIAR#: This Design Analysis SUPERCEDES: SUPERCEDES: .8, N/A NlA in its entirety. Description of Revision (list affected Description partials): **,9This revision raises the required amount of nitrogen affected pages for partials): for seven days of SGIG post-LOCA post-LOCA operation from 49,904.77 49,904.77 SCF to 120,000 120,000 SCF. The original 25% margin margin (9,980.95 SCF) was removed and replaced with 80,422 SCF to account for estimated system leakage. In In addition, eight days of leakage addition, leakage through the CAC Vent and Purge Butterfly Valve Stations was replaced replaced with seven days since SGIG is only required seven required for seven days post-LOCA without additional additional supplies per TSB SR 3.6.1.3.1 and 3.6.1.5.1. 120,000 SCF of nitrogen is required 3.6.1.5.1. As a result, 120,000 required for 7 days of post-LOCA operation of SGIG and 320,000 SCF for CAD + SGIG. The affected pages of Revision Revision 3 include include 3, 3a, 3b, 4, 5, 7, 7a, 11, 11, 14, 16, 16a, 23, 24, and 24a. The leakage leakage estimate provided as attachment 1/II and inputs for the estimate has been provided the estimate are included in ECR 09-00416. Preparer: Preparer: ,0 Richard Wagner I. t?J. 'LL i2 *--. L 11/16/09 11/16/09 Print Name
-rnn-e ~gnName,.
,vQ., arnmeo'- Date Date Method of Review: Review: 2121 Detailed Review 121 [ Alternate calcz;n~Ched)
Alternate Calculaions (attached) E[ 0 Testing 0El Reviewer: Paul Paul Kester jJh'lo~ Reviewer: 12 22 Kester ._ Print Name Print Name
- Sign Name Sign Name Datb Oalt!
Review Notes: 23 23 Independent review [I:8J Independent Peer review 0 Ml (For External (For Analyses Only) External Analyses Only) External Approver: 2424 Print Name Sign Name Date Print Name Sign Name Date Exelon Reviewer: Reviewer: 2.25 Prtnt Name PlintName Sion Name Sign Name Date Date Independent a Independent rd 3 rd Party Review Reqd? 2016 Review Reqd? Yes 0 0 No I2J[ Exelon Approver: 27 Jeffrey Jeffrey Chizever ~._Cl<i~-' iiIlj;;O/cfj 1,0/01 Print Name Print Name 4 I r SignName Siqn Name Date Date V V I...-'
Exel¢!Jnw Exelk n.Nuclear CALCULATION Nuclear CALCULATION SHEET SHEET SPAGE: CALC NO.: CALC PAGE: PM-0375 NO.: PM-0375 2 of REVISION: 4 24 Nuclear REVISION: 4
1.0 Purpose
1.0 purpose of this design analysis The purpose analysis is to establish the limiting limiting system demand for nitrogen gas gas from the Containment Containment Atmospheric Atmospheric Dilution (CAD) tank for the combined limiting demand demand of Safety Grade Grade Instrument Gas (SGIG) and CAD system for dual unit (Le., (i.e., for both PBAPS UnitsUnits 2& & 3) operation. operation. The design basis for combustible gas control for P8APS PBAPS is NEDO-22155 NEDO-22155 (Reference (Reference 28). ThisThis evaluation, evaluation, which was reviewed reviewed and approved approved for PBAPS through Nuclear Regulatory Nuclear Regulatory Commission Commission (NRC) letter from John John F. Stolz (Chief Operating Reactors Branch Branch (Division of Licensing)) to Edward Edward G. Bauer, Jr., Jr., Vice President and General Counsel Philadelphia Electric Philadelphia Electric Company Company "Recombiner Capability Requirements of 10 CFR 50.44(c)(3)ii," Generic Capability Requirements Generic Letter 84-09, dated 6/26/85 (Reference (Reference 29), demonstrated that PBAPS does not rely on purge/repressurization system as the primary means of combustible gas control. The purge/repressurization The evaluation showed showed that with more more realistic, but conservative conserVative oxygen generation rates (0.1 molecules/1 00 ev for 12 hours and 0.003 molecules/100 molecules/1 00 ev greater than 12 0.003 molecules/100 12 hours), the primary containment containment oxygen concentration concentration will not reach the 5% limit within 30 days. Therefore, the the CAD system is not required to operate. The SER did however, require that the CAD system maintained as originally be maintained originally designed, therefore, therefore, this calculation calculation is maintained to document document that the CAD system is capable capable of meeting the original design design basis requirements. Per PBAPS UFSAR Section 5.2.3.9.4, the CAD system starts operating in about 24 hours (1 (1 day) following a LOCA. PBAPS PBAPS UFSAR Section 5.2.3.9.3, states that the on-site supply is sufficient to provide at least 7 days of dilution (Le, (i.e, CAD function) for each unit. Therefore, the the inventory of nitrogen calculated required inventory nitrogen in the CAD tank is based on 7 days combined combined demand of CAD and the SGIG systems for dual dual unit operation. Revision 2 of this calculation incorporates the resolution of SSFI Action Item No. SFIP 92-08, calculation incorporates items A, 0, D, F, and H.H. Revision 4 of this calculation calculation raises the required amount of liquid nitrogen for SGIG operation to account for system leakage. ItIt has also replaced the 8 days of leakage leakage with 7 days of \(q leakage through the CAC Vent and Purge Butterfly Valve Stations per ECR 09-00416. leakage 2.0 Summary Summary of Results: Based on this calculation, calculation, the total limiting demand demand for N2 N2 gas, for dual unit CAD and SGIG SGIG system operation, is approximately approximately 320,000 SCF. This amount of N N22 gas contains contains a margin of 80,422 SCF for the limiting demand demand for the SGIG system. A minimum CAD tank liquid N2 N2 inventory corresponding inventory corresponding to to 38.5" of water 38.5" of water column column (327,800 (327,800 SCF) SCF) was was selected selected and bounds the and bounds the ~v\ calculated amount of N N22 required for CAD and SGIG system operation. For dual unit SGIG SGIG system operation, approximately system operation, approximately 120,000 120,000 SCF SCF is required. A minimum minimum CAD tank liquid N2 N2
Exelon,~ Exekrn. CALC CALC NO.: NO.: PM-0375 PM-0375 CALCULATION CALCULATION SHEET SHEET PAGE: "3of 24 PAGE: '3 of 24 Nuclear Nuclear REVISION: REVISION: 44 inventory corresponding to 22" of water column (124,000 SCF) was selected and bounds the inventory corresponding to 22" of water column (124,000 SCF) was selected and bounds the calculated calculated amount amount of of N 2 required N2 required forfor SGIG SGIG system system operation. operation. Revision Revision 1 summary: The The additional additional N 2 consumption N2 consumption attributed attributed to to the the Containment Containment Emergency Emergency Vent Vent System System valves valves isis not not impacting impacting on on the the total total limiting limiting demand demand determined determined in in Revision Revision 00 of of this this calculation. calculation. The The total total N N22 consumption consumption margin margin remains remains approximately approximately 25% 25% and and the the calculated calculated N N22 inventory inventory of of approximately approximately 250,000250,000 SCF SCF remains remains valid. valid. Revision Revision 22 Summary: Summary: The resolution of SSFI Action Item No. SFIP 92-08, items A,D,F, and H does not impact the The resolution of SSFI Action Item No. SFIP 92-08, items A,D,F, and H does not impact the total limiting total limiting demand demand for for nitrogen nitrogen determined determined in in Revision Revision 11 of of this this calculation. calculation. Revision Revision 33 Summary: Summary: This This calculation calculation is is being being revised revised as as aa result result of of NCR NCR PB-98-01672. PB-98-01672. The The NCR NCR identified identified that that the the .design design basisbasis for for the the Containment Containment Atmosphere Atmosphere DilutionDilution system system isis inaccurately inaccurately described described in in various various design design andand licensing licensing documents. documents. This This revision revision will will revise revise this this calculation calculation to to clarify clarify the the design basis method of combustible gas design basis method of combustible gas control for PBAPS. control for PBAPS. Revision Revision 44 Summary: Summary: This This calculation calculation has has been been revised revised as as aa result result ofof ECR ECR 09-00416. 09-00416. Due Due to to the the estimated estimated system system leakage, the nitrogen consumption for seven days of post-LOCA leakage, the nitrogen consumption for seven days of post-LOCA operation of. SGIG has been operation of SGIG has been gl-{ raised raised from from 49,904.77 49,904.77 SCF SCF toto 120,000 120,000 SCF.SCF. As As aa result, result, the the total total demand demand for for CAD CAD and and SGIG SGIG was was changed changed from from 250,000 250,000 SCFSCF to to 320,000 320,000 SCF. SCF. TheThe computation computation to to determine determine the the system system leakage leakage has has been been added added as as anan attachment attachment to to this this calculation. calculation.
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Exelon'M xelon.f CALCULATION CALCULATION SHEET SHEET PAGE: NO.: of CALC PAGE: 5 of 24 24 PM-0375 0 Nuclear Nuclea'r REVISION: 4 REVISION: 4 5.0 Design Input/Criteria: Input/Criteria:
- 1) DID for mod 1316, Rev 6 dated 11/14/89 11/14/89 1316, Rev 21 dated 8/13/89
- 2) EWL for mod 1316, 8/13/89
- 3) Safety Evaluation Evaluation for mod 1316, Rev 12 dated 8/13/89 8/13/89
- 4) Piping and layout dwg M-3189 M-3189 &
& 3190 3190
- 5) Design Input Document for mod 5236, Rev 2 dated 11/22/91
- 6) ECR 09-00416 Rev 0 (Operator Log for DW Makeup Makeup using CAD - 8/4/08 to 8/4/09)
RI-1
- 7) TODI TOOl 710172-40, CAD Tank Level and Pressure, and DIW D/W Bulk Average Average Temperature Temperature from 8/4/08 - 8/4/09
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xektn. Exeion'M CALCULATION SHEET CALCULATION SHEET CALC PAGE. NO.: PAGE:Lof 24 _of24 7__PM-0375 Nuclear Nuclear REVISION: 44 REVISION: nd th
- 13) Compressed Air &
- 13) Compressed & Gas Data (Ingersoll (Ingersoll - Rand Co.) - 22nd Edition, Edition, 66th Printing Fleischmann to E.C. Kistner, dated 5/22/84
- 14) Letter, R.S. Fleischmann 5/22/84
- 15) Letter, Linda Mast to Tapan Banerjee, dated 6/25/90
- 15) 6/25/90 16)
- 16) Letter, JA Jordan Jordan to Mod 1316 12/4/89 1316 File, dated 1214/89
- 17) N2
- 17) N2 leakage from SGIG header, calculation based on LLRT data (L. (L. Mast to TK Banerjee)
- 18) Fax Transmittal, Process Engineering, Engineering, Inc. (Scott C. Nason) to PECO (TK Banerjee) dated 7/25/90; total 4 pages pages
- 19) Calculation PM-374, Rev 0 6280-M-1 17-74-1 Instruction Manual
- 20) Vendor Print 6280-M-117-74-1 Butterfly Valves Manual for Fisher Butterfly Valves
- 21) Calculation
- 21) Calculation PM-386, Rev 0 dated 9/13/90
- 22) Set Point CaIc.
Calc. for Pressure Switch Containment Isolation Butterfly Valves Boot Seals. Switch of Containment Calc No. PE-063, Rev 0 dated 8/14/908/14/90
- 23) PBAPS Alarm Response Card 30C284 C-5 dated 11/19/89 11/19/89
- 24) Telecon Record; Record; Tapan K K Banerjee (PECO/NESD)
(PECO/NESD) and R. Nesbilt (GE - San Jose) dated 7/25/90 7/25/90 Chemical Eng Handbook, 55 thth Ed.
- 25) Perry's Chemical
'26) G.H. Bettis Heavy - Duty Product Series Pneumatic Actuators Catalog # 30.00-1 A, pages
- 26) G.H. Bettis Heavy - Duty Product Series Pneumatic Actuators Catalog # 30.00-1 A, pages 11, 19, front 11, front cover, and back cover cover
- 27) Telecon record
- 27) Telecon Steward (G/C record Steward (G/C Inc.) and Burkenhoff Inc.) and Burkenhoff (GH(GH Bettis)
Bettis) dated 3/23/92 dated 3/23/92
- 28) NEDO-22155, Generation
- 28) NEDO-22155, Generation and Mitigation of and Mitigation of Combustible Combustible Gas Mixtures Mixtures Core Inerted Inerted Mark II Containments, dated June 1982 1982
- 29) Nuclear Regulatory
- 29) Nuclear Regulatory Commission Commission (NRC)(NRC) letter from from John F. F. Stolz Stolz (Chief (Chief Operating.
Operating. Reactors Branch (Division of Licensing)) to Edward G. Bauer, Jr., Vice Reactors Branch (Division of Licensing)) to Edward G. Bauer, Jr., Vice President and President and General Counsel Philadelphia Electric Company "Recombiner General Counsel Philadelphia Electric Company "Recombiner Capability Capability Requirements Requirements of of 10 CFR 10 CFR 50.44 (C)(3)ii Generic 50.44 (C)(3)ii Generic Letter 84-09," 84-09," dated dated 6/26/85 RW- ý6
Exelon<~ Exek Nucleaa. CALC NO.: PM-0375 CALCULATION SHEET CALCULATION CAGNO:7 RPAGE:I PAGE:-7q of-24 of 24 Nuclear NuclearREVISION: REVISION: 44
- 30) Calculation PM-804, "Post LOCA Containment Containment Atmosphere Atmosphere Dilution System Analysis onon power" rerated core power" 09-00416 Rev 0, "Revise Calc PM-375 (CAD/SGIG Required N
- 31) ECR 09-00416
- 31) N22 Level)"
TOOl 710172-40,
- 32) TODI Level and Pressure, 710172-40, CAD Tank Level Temperature D/W Bulk Average Temperature Pressure, and DIW 8/4/09 from 8/4/08 - 8/4/09 24 U."
P.4
Exelonw Exekon. CALCULATION CALCULATION SHEET SHEET N7 of PAGE:NO.: CALC PM-0375 PAGE: 7b of 24 24 Nuclear Nuclear REVISION: 44 REVISION:
7.0 Attachments
The following references references are attached with the calculation: Reference Reference Description Pages Pages 1 Inc., Print No. 6280-M96-189-1 Process Eng. Inc., 6280-M96-189-1 1 10 Table A-26; Properties Properties of Sat. N2N2 : Temperature Temperature Table 5 13 Compressed Air & & Gas Data 1 14 Fleischmann to E.C. Kistner Letter, R.S. Fleischmann 1 15 Banerjee Letter, Linda Mast to Tapan Banerjee 1 16 Letter, JA Jordan to Mod 12/4/89 Mod 1316 File dated 1214/89 1 17 N N22 Leakage Leakage from SGIG header, Calculation based on 1 LLRT LLRT data (L.Mast (L.Mast to TK Banerjee) 18 Fax Transmittal, Process Eng. Inc. dated 7/25/90 4 20 Vendor Print 6280-M-117-74-1 6280-M-1 17-74-1 Instruction Instruction Manual Manual for 9 Fisher Butterfly Butterfly Valves Valves 23 PBAPS Alarm Response Response Card 30C284 C-5 1 24 Banerjee and R. Nesbilt Telecon Record, TK Banerjee Nesbilt (7/25/90) 1 26 GH Bettis Heavy-Duty Heavy-Duty Product Series Pneumatic 4 Actuators Actuators Catalog #30.00-1 A Catalog #30.00-1 A 27 Telecon Steward and Burkenhoff Telecon Record, Steward Burkenhoff (3/23/92) 1 Attachment 1- I - Evaluation for SSFI SSF! Action Item No. SFIP92-0B, SFIP92-08, Item 1A Attachment IIII - Computation of System Leakage Attachment Leakage (ECR (ECA 09-00416) jgL(4
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INSERT INSERT 9-1: 9-1: 200,000 scfm is isananarbitrary limit for the CAD system shouldbebenoted It Itshould noted thatthethe that demandofof totalN2N2demand total 200,000 scfm 30) arbitrary limit Calculation for theshows PM-804 CAD system that usage uSagewhichwhichisis confirmed confirmed bybyCalculation PM-804. (Reference Calculation PM-804. (Reference 30) Calculation PM-804 shows that CAD systemusage CADsystem usagewillwillbebeless than less 200,000 scfm for 7 days. than 200,000 scfm for 7 days.
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Mod 1950A was installed installed to provide a backup pneumatic (N 22 )) supply for the
- SRV's RV-2/3-02-071 RV-2/3-02-071 E, E, 'H, and J (for (for both PBAPS Units 22 and 3) 3) in in the event event of of an A an A endix endix R fire.
R fire. The The N N2z supply supply for for thesethese vakm va~mes 9mes from the CPB CAD tank throug througg ,the the .Safety Safety Grade Instrument Gas (SGIG)r~ping. Grade. Instrument (SGIG)f!Iping. The Nz2 supply header header going to t~ each unit has a locked close valve. valve. On 6~ a postulated Appendix R fire fire (for a particular particular unit), unit), the locked close valve has to be opened by manual manual operator action to establish N2 Nz flow to the above referenced valve stations. stations. 4ssen-da jupply AN2 gas i aintai n the Cltainmen Atmospkric Di 1io/ (CAD tnk-i ,th form f Yiquid it ogen N2 iv try tzoyrv4 t t 0 CA aý the SGIG uncoTns Wit in seve d peidth~Ata t.4nkLN, inventory can be _enishe om outse source An Appendix Appendix R fire is is an independentindependent event of a DBA-LOCA and also, the DBA-LOCA is not an initiating event for an Appendix R fire. Therefore, the DBA-LOCA is not an initiating event for an Appendix R fire. Therefore, the post-LOCA CAD N N2z demand and N2 demand&for Mod 1950A N, demand~'for 1950A are not additive. additive. The The SGIG system supplies supplies backup N to the CAC Isolation Valves, Valves,supplies CAD CAD vent vent valves
- and torus vacuum breaker isolation z2 valves. The SGIG system N, valves gas to and torus vacuum breaker isolation valves. The SGIG system supplies N, gas to
- these valve stations stations in case of a postulated loss of normal instrument air. air.
The SGIG SGIG system system normally is is a standby system and the N2 N2 demand (for the the SGIG SGIG system) is is not significant compared to the LN inventory available in in the CAD the CAD z2 tank. tank. The Mod 1950A 19S0A nitrogen demand is also extremely small is also extremely small compared to the compared to the available N N2z inventory inventory in in the C.W tank. CAD tank. Therefore, Therefore, N2 N2 demand for Mod for Hod 1950A is 1950A is not a concern for determining determining the CAD tank capacity or the volume of of LN LN 2 2 inventory to be maintained in in the CAD tank. ~¥ -A--ccpq-f Rvi of RellisioA 1of-of lied -10i5,0-- 1-9~ Sa-fe-~-ltlat-i-on-i-s-a-~t,aGA-ed for Fci jinnfor:mat~fl. frmt~n. '~st 8t ~Oqq ~P/IA1>/k",:>
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Exeken CALCULATION SHEET Exel~n'M CALC NO.: PM-0375 CALC NO.: PM-0375 Nuclear CALCULATION SHEET RPAGE: .LL PAGE: M of 24 of 24 Nuclear REVISION: 4 NucleaTREVISION: 4 Calula~tion Calculation to establish total liquid liouid nitrogen nitroaen demand for CAD and SGIG system system for dual unit unit Cqlculation to establish total liouid nitrooen demand for CAD and SGIG svstem for dual unit operation: Demand = N22 Gas Demand Total N = 320,000 SCF (pg 23) SCF is defined at 14.7 psia and at 70 of OF Using ideal Gas Law for N2 2: 33 M- M= Px V =
= PXv (latm) x (latm) x (320,00ft (320,OOOjt ))
Tat - f3 RxT (0.730 atm t - ft fit 3 ) x (529.7 OR) (0.730 am- )x(529.7 OR) lb - mol OR lb-moi oR Note: R == Universal Universal Gas Constant R =0.730 atm R=0.730 atm-- ftjt33 (Ref 10) lb --mol mol OR oR
= 459.7 +70 T =459.7 + 70 =529.7
= 529.7 oR OR M= 827.56 lb - mol
= 827.56lb
= 827.56 lb -
= 827.561b 28.0lb mol xx 28.01lb mol lb - mol
=
= 23,179.83lbm 23,179.83 Ibm ofoj NN2
. . .196-21453 7/89
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Exelonw SCACALC Exekrno. CALCULATION CALCULATION SHEET CALC NO.: PM-0375 PAGE: i14 of 24 PAGE: 14 of 24 PM-0375 Nuclear Nudear REVISION: 44 REVISION: Tank With Liquid With Both Liquid and Vapor N N22 Considered in the the Pressure Pressure Inventory Only Tank Tank Max Tank Vol Nominal Nominal Tank Tank Capacity
== 882.62 cu-ft cu-ft
= Gallons
= 6000 Gallons
= Gallons
= 6602 Gallons XL 0.13368x 0.02513 0.02513 170 psig 170 psig =23,179.8lbm 0.13368[ XL + (6602-XL)] 0.13368[ XL + (6000-XL)]
= 23,179.8 Ibm 0.13368[ Xl. +(6602- X t.)] 0.13368[ x I.. + (6000 - XL)]
V =0.02513 VLL = 0.02513 L0.02513 0.025 I 3 0.30027 0.30027 L0.02513 0.02513 0.30027J 0.30027 ft3 /lb fe/lb XL = 4357.48 Gallons = 23,179.8 Ibm 23,179.8 Ibm XL = 4357.48 Gallons =23,179.8 Ibm = 23.179.8 Ibm
=
Vg = 0.30027 0.30027 ft3/Ib X ~ = 4152.5 Gallons = 4207.5 fe/lb X L = 4152.5 XLI.. = X 4207.5 Gallons Gallons Gallons Vendor Calculated Calculated 4342.8 Gallons at 170 psig (Ref 18) XL XL 0.13368x 0.13368x 0.02719 0.02719 250 psig
==23,179.8lbm 23,179.8 Ibm 0.13368.
0.13368[ XL L0.02719 0.027 19 (6602 -XL)L)] Xl. + (6602-X 0.19867 0.19867 1 0.13368[ 0.13368[ XL XL L.02719 0
+ (6000-XL)-
+ (6000 - XL)]
0.19867 0.02719 0.19867 VL VL ==0.02719 0.02719 3/Ib 23,179.8 Ibm
=23,179.8 lbm = 23,179.8 Ibm
= 23,179.8 Ibm ft fe/lb X L=
XL = 4714.7 Gallons 4714.7 Gallons Vg ==0.19867 ft3/lb
/Ib X = 4415.4 Gallons XL~ =4415.4 Gallons XL XL =4510.9
= 4510.9 Gallons Gallons Vendor Calculated Vendor Calculated 4710 Gallons at 250 250 psig (Ref 18) psig 18)
196-21453 7/89 196*21453 7189
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Exelon,,, CALCULATIO CALCULATION N SHEET SHEET PAGE: PAGE: 16 of 24 24 l ofPPM-0375 CALC NO.: Nuclear Nuclear REVISION: REVISION: 44 3 ft 3 std ft x 10-33 Std Total Leakage == 34 valves xx 7.062 34 valves 7.062 x 10- --------- min-min- valve valve
==0.240SCFM 0.240 SCFM
=(0.240 S~F)(60 0.240 SCF min mm I60 (6 mm~in)(24 iY22-(7hr J(7 days) hr day) day
= 2419.2 SCF total for 7 days (2) Containment AtmospheriC Control Vent and Purge Butterfly Valves (18'"
Containment Atmospheric (18" Size): These valves are normally closed and fail closed. It is assumed assumed that thethe Containment Containment was being purged while LOCA occurs. Following a LOCA, and loss of instrument air, these valves will go closed. These valves are not required be required to be operated following a LOCA (except for emergency venting through the large Butterfly Butterfly vent valves which is beyond the design design basis). However, the boot seals for all the following the accident containment isolation butterfly valves need to remain inflated 'following containment accident scenario. The N requirement for maintaining boot seals inflated condition has been N22 requirement accounted for in this calculation. During a TW sequence sequence venting operation, thethe inboard 18" CAC vent valve is required to operate concurrent concurrent with the Containment Containment Emergency Vent System valve to establish the vent path to atmosphere.
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em CALO NO.:,PM-0o75 Exel~Jn\~. PAGE:Z CALC 24 NO.: PM-0375 CALCULATIO N SHEET CALCULATION SHEET NO.:f PAGE: Z"3> of 24 Nuclear Nuclear REVISION: 44 REVISION: Total Demand for Dual Unit Operation Operation
- 1) CAD Demand
- 1) Demand 200,000 SCF I
- 2) Leakage through CAC Vent & & Purge Butterfly Valve 2419.2 SOF 2419.2 SCF Stations Stations lgq
- 3) N2N2 for stroking valves 140.215 140.215 SCF
- 4) Purge & & Vent B/F Valves Boot Seals 13.3 SCF SCF
- 5) Inventory Inventory inin SGIG System 90.5 SCF SCF
- 6) Pressure decay make up in SGIG Header and 915 SCF 915 SCF Tubing 915_SCF
- 7) PCV Fail Open (4 hours) 36,000 SCF
- 8) Available Computation Margin ( Leakage) of System (Attachment IIII -
Leakage) 80,422 SOF 8,2 C Computation of System Leakage) 80,422 SCF R4 SGIG Demand (items (2) through (8)) = = 120,000 SCF 120,000 CAD + SGIG Demand (Total Demand) == 320,000 SCF Setting of Minimum Minimum Liquid Nitrogen Nitrogqen (LNg) (LN2 ) Level and Low Level Alarm (LIS-6530AB) (LlS-6530A,B) Setpoint in in CAD Tank: The minimum required level and low level alarm setpoints setpoints are based on CAD Tank Vendor provided provided information information (Ref. 18). The vendor supplied table provides liquid nitrogen volume at corresponding corresponding inches of water column for an operating operating pressure pressure of 250 psig in the CAD storage storage tank. Using the 250 psig table provides the most conservative conservative setpoints and is the same as the the maximum maximum allowed working pressure of the CAD storage tank. 9q-The minimum CAD storage tank level for 7 days of Post-LOCA Post-LOCA operation for SGIG and SGIG + CAD were calculated calculated and rounded up to an acceptable acceptable level. The following values were selected from the vendor supplied supplied table (Ref 18) as the minimum CAD storage tank levels: minimum SGIG SGIG operation operation = 22" 22" water column I/ 124,000 124,000 SCF /I 1,825 1,825 gallons gallons CAD + SGIG operation = =38.5" water column / 327,800 SCF / 4,826 gallons gallons The low level level alarm setpoint must be set at a level above above the minimum level requirements listed listed determining the low level alarm setpoint, the 250 psig vendor supplied table above. When determining table (Ref.18) should be used.
Exen CLUCALC NO.: PM-0375 Exelon," CALCULATION SHEEPAGE: CALCULATION SHEET CALC NO.: PM-037S
'Z-_of 24 PAGE: 'l."\of 24 Nuclear Nuclear REVISION: 4 REVISION: 4 This page This page left intentionally blank left intentionally blank
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/0 I ~,c6I S"5.r THERMODYNAMICS THERMODYNAMICS Fifth Edition Edition Kenneth Wark, Jr. Jr.
Associate Professor Professor of Mechanical Engineering Mechanical Engineering Purdue Purdue University University
~'"
McGraw-Hill McGraw-Hill Book Company C.2mpany New York New York St.St. Louis Louis San San Francisco Francisco Auckland Bogoti Caracas Colorado Springs Auckland Bogota Springs Hamburg Hamburg-Lisbon London Lisbon London Madrid Mexico Milan Montreal Madrid Mexico Montrcal New New Delhi Oklahoma City .--'....~- Panama Paris Paris San San Juan Panama Juan Sio Paulo Singapore Sao Pllulo Singapore Sydney Sydney Tokyo Tokyo Toronto Toronto
P Al 3-7 ~ k (~l, C PfVI- 3?~ APPENDIX APPENDIX fc-.f qi /0 A_-2 A-2 2 D'fO S SUPPLEMENTARY SUPPLEMENT ARY TABLES TABLES AND FIGURES (USCS FIGURES AND (uses UNITS) UNITS) I! 882
4ie.3Cý ,I-r2 Iv 2 oF - SUPPLEMENTARY SUPPLEMEl'fI"ARY TABLES TABLES AND AND FIGURES (uses UNITS) fiGURES (USCS UNITS) 883 883 TABLE A4I TABLE A~l . Physical constants Physical constants and and conversionconversion factors factors Physical constants constants Standard gravity Standard gravity g9 = 32.174 ft/s' 32.174 ft/s1 Universal gas constant Universal constant R. = R, 1545 ftft.lb./(lbmol-*R)
*lb,/(Ibmol* OR)
= 1.986 Btu/(lbrnol*-*R) 1.986 Btu/(lbmol OR)
= 0.730 atmatm'* ftJ/(lbmol ftJ/(lbmol.oR) .*R)
= 10.73 psia.
10.73 ft?/(lbmol.*R) psia.ft'/(lbmo\.oR) Conversion factors Conversion (actors Length 1I em cm = == 0.3937 0.3937 inin === 10'10* Pmrpm = == 10' A 10' A 1I in = 2.540 2.540 cmem 1 ft = 30.48 1ft 30.48 cmem Mass I Ibm lb,, = 453.59 g;" g,;6= 70007000 gr gr 1 kg kg,,.. = 2.205 Ib. 2.205 IbM Force Force Ilib lbrI = 32.174 lb,. ft/s' 32.1 74 IbM' ft/s2 1I Ib IbI1 = 444,800 444,800 dyn=dyn = 4.448 4.448 N 1 torr = 1I mmHg mmHg at 0*C O°C '" = 103 pin Hg 10' I,m 1.933 xX 10-
= 1.933 10-"2 psi Volume I L = 0.0353 £I' ft 3 = 0.2642 0.2642 gal === 61.025 in' in3 3
ft' = 1 fll = 28.316 28.316 L L = 7.4805 gal = 0.02832 ml 1I in' in' = 16.387 16.387 em'cm' 3 2 Density Density lb,,.'ft = II Ib.,/ft' = 0.01602 gjcm 0.01602 g..lcm' Energy Energy 1 Btu Blu = 778.16 ft-lbf = 1055 778.16ft.lb, IOS5) 3 I Blu,'Ib Btu/lb = 2.32 kJ/kg power Power 1 \VNV= = 1 3/s J/s ==
= 3.413 Btuih 3.413 Btu/h IJ hp/tp = = 746 W = 5jO 556 ft. lbf/s == 2545 Btu/h re*/b,/s Btu/It Velocity Velocity II mi/h = == 0.447 m/s mls Specific heat Btui(lb,...
- F) =
II Btuj(lb == 4.187 kJ/(kg-kJ/(kg* K) Temperature Temperature T(*R) T(OR) = T(°F) + 459.67 ==
== T(*F) 1.8[T(CC) + 273.15]
= 1.8(T<<C) 273.15) = == I.8T(K) l.8T(K)
TABLE A-2 TABLE A-2 uses (engineering) derived units UJSCS (engineering) Physical quantity -Unit lJnii Symbol Definition Force pound-force pound-force lbh Ib f 32.174 IbM' ft/s2 32.174 lb,.- ft/s!2 Pressure atmosphere atmosphere atm arm 68,087 lb,,,ft Ib...;Tt _-s5' (= 14.696 (= lbf/in-) 14.696 Ib,lin!) 2 2 Energy root-pound-force fooc-pound-force It.lbr {I.lb f 32.174 lb.rt 32.174 lb ..
- f1 2-/s
/5 1
power Power foot-pound-(oot-pound- ft.lb,/s (t*lbf/s 32.174 IbM' 32.174 ft-/sl lb,.(t!/sJ force/second force/second (= 1.S2 xx 10-] ( .. 1.82 10"' hp)hp)
. ~1It.c pM - 3?S""
REF
/?EF t10y SOF=
918 918 (uses UNITS) if of ~ I, SUPPLEMENTARY TABLES SUPPLEMENTARY TABLES AND FIGURES (USCS AND FIGURES TABLE A-19 TABLE A-19 Properties of saturated Properties saturated nitrogen nitrogen (N (Nl): Temperature table 2 ): Temperature table 3 v, ft v, /lb; uII and frl/lb; and h, Btu/lb; s, h, Btu/1b; 5, Btu/(lb-°R) Btu/(Ib' OR) . Specific Specific volume. volume. Internal Internal energy energy Enthalpy
.Enthalpy Entropy Entrop~'
Temp., Press., Press., Sat. Sal. Sat. Sal. Sat. Sal. Sat. Sat. Sat. Sat. Sat. oR OR p~il\ psia liquid liquid vapor vapor liquid liquid ,-apor vapor liquid liquid Evap. Evap. vapor vapor liquid liquid vapor
\"apor TT p h, P VI r, t, uf ul u, hf h~f hI' h, he si..
sl 3s,
-r 113.7*
113.7" 1.82 1.82 0.0185 23.73 35.32 I 119.91 119.91 35.33 92.59 92.59 127.90 127.90 0.5802 1.395 1.395 120.0 3.34 0.0188 13.56 38.33 38.33 120.93 38.34 38.34 90.98 90.98 129.32 129.32 0.6060 1.365 1.365 130.0 130.0 7.67 0.0193 6.321 43.19 43.19 122.47 43.22 43.22 88.22 88.22 131.44 131.44 0.6449 1.324 1.324 139.2 139.2 14.70 14.70 0.0198 3.473 3.473 47.71 47.71 123.77 47.77 47.77 85.45 85.45 133.22 133.22 0.6785 1.293 1.293 140.0 15.46 0.0199 3.315 3.315 48.09 48.09 123.87 48.15 48.15 85.21 85.21 133.36 0.6812 1.290 1.290 i
~J., I' 150.0 28.19 28.19 0.0205 0.0205 1,899 1.899 53.02 125.11 53.13 81.89 135.02 0.7153 1.262 1.262 160.0 160.0 47.52 0.0213 1.164 1.164 58.00 126.14 58.19 78.19 136.38 136.38 0.7474 1.236 1.236 170.0 75.18 75.18 0.0222 0.750 0.750 63.08 126.91 63.39 73.96 73.96 137.35 0.7782 1.214 1.214
- I!
,~ 180.0 113.0 113.0 0.0233 0.502 0.502 68.30 127.36 68.79 69.07 137.86 0.8082 1.192 1.192 ~
190.0 162.8 162.8 0.0246 0.344. 0.344 73.75. 73.75. 127.40 74.49 74.49 63.28 137.77 0.8378 1.171 1.171 200.0 226.9 0.0262 0.239 0.239 . 79.52 126.84 126.84 80.62 56.24 136.86 136.86 0.8677 1.149 1.149
~ 210.0 307.3 0.0285 0.164 0.164 85.86 125.33 87.48 47.20 134.68 134.68 0.8992 0.8992 1.124.
220.0 406.9 406.9 0.0325 0.107 0.107 93.57 121.80 96.01 96.01 33.85 129.86 0.9363 0.9363 1.090 1.090 226.0 477.9 0.0394 0.071 101.46 115.66 104.95 16.97 121.92 0.9742\ 1.049 0.9742 1.049 227.2* 227.2" 493.1 0.051 0.051 108.59 108.59 113.25 0 113.25 113.25 1.010 1.010 1.010 1.010 I
*1113. 7~R is the triple state and 227.2'R is 13.7-R is the critical state.
Sourc.: Adapted from National Bureau Source: Bur<au of Standards, Technical Note 648. Stand~rds. Tochnical 649, 1973. 1973. I 1~ I I I I t A..
.~.
/ / 3'7-7 I O SUPPLEMENTARY SUPPLEMENTARY TABLES TASlES AND F1GURESFIGURES (uses UNlTS) (USCS UNITS) 919 919 TABLE A-20 TABLE A-20 Properties of nitrogen nitrogen (N21): Superheated-vapor table*
): Superheated-vapor table v, (,J/lb;* IIwand It, v, f[t/Ib; Btu/lb; 5, It, Btu/Ib; Btu/(Ib'°R) s, Btu/{lb*oR)
Temp., v V I u II hh I !s s (v u IIu u Ih It .i I s
'R OR 20 psi2 rr...
psi~ (T,ý, = 144.10R)144,1"R) (T,, = 161.0'R) 50 psia (1;" 161.00 R) I 200 3.755 134.83 148.73 148.73 1.364 1.454 133.97 133,97 147.44 1.295 1.295 250 250 300 300 350 350 4.740 5.714 6.682 6.632 143.87 152.82 161.74 I 161.42 161.42 173.98 t173.98 186.49 186.49 1.421 1.467 1.467 1.505 1.866 1.366 2.266 2,659 2.659 143.30 152.40 152.40 161.41 161.41 160.58 173.38 173.38 186.03 1.354 1.354 1.400 1.400 1.439 1.439 400 7.647 170.65 198.97 1.539 3.050 170.37 198.61 198.61 1.473 450 450 8.610 179.54 179.54 211.4 1.568 1.568 3.438 179.30 211.1 211.I 1.502 1.502 123.9 I 500 500 9.572 188.42 223.9 1.594 1.594 3.826 188.22 223.6 1.529 1.529 550 550 10.53 197.31 236.3 1.618 4.212 197.13 197.13 236.1 1.553 100 psia (T.,Cr.** = 176.9°R) 176.9"R) 200 psia 200 0.684 132.40 145.07 145.07 1.238 1.238 0.289 128.33 128.33 139.04 1.166 1.166 250 250 0.908 0.908 142.31 159.13 1.300 0.427 140.1 140.188 156.01 156.01 1.243 300 1.116 )51.68
.151.68 172.36 1.349 .0.542 150.19 .170.25 1.295
.350 350 1.319 160.84 160.84 185.26 1.389 0.649 159.69 183.71 1.336 1.336 400 1.518 169.90 198.Ql 198.01 1.423 0.752 168.96 168.96 196.81 1.371 1.371 450 1.715 1.715 178.91 178.91 210.7 210.7 1.452 0.853 178.12 178.12 209.7 1.401 10401 500 1.910 187.88 I 223.3 1.479 0.953 187.20 187.20 222.5 1.428 550 550 2.105
\
196.83 I 235.8 196.83 500 psia I\ 1.503 1.052 I 196.23 I I 235.2 psia 1000 psi:i 1.453 1.453 250 250 0.132 0.132 I 131.52 1 143.78 131.52 143.78 ! 1.141 0.038 I I 0.038 I 106.30 106.30 113.40 1I3.40 0.994 300 350 350 0.197 0U247 0.247 I* 145.25 145.25 156.09 . 178.96 163.45 I 1.213 1.261 0.083 0.115 I 135.26 135.26 149.67 149.67 150.59 170.95 170.95 1.131 1.131 1.194 1.194 400 450 450 0.293 0.337 0.337 166.10 175.73 I [93.23 193.23 206.9 I 2.299 1.299 1.331
\.331 0.142 I 161.23 0.166 1 171.77 187.45 187.45 202.5 1.238 1238 1.274 1.274 500 0.379 185.16 I
220.3 220.3 II1:38 1.359 1.359 0.189 181.81 181.81 216.8 216.8 1.304 1.3~ I 550 550 0.421 194.46 233.4 I.J84 1.384 0.211 191.56 191.56 230.6 1.330 1.330 2000 psia psla psia 3000 psia I 250 0.029 i 95.00 0.029 ! 115.61 0.939 0.026 0.025 I 90.47 90,47 114.97 114.97 0.917 0.917 300 300 350 350 0.040 I 118.41 0.055 I 137.38 137.38 i 133.[7 I 133.17 157.78 157.78 ! 1.040 1.040 1.116 1.116 0.032 0.032 0.040 II 110.73 110.73 128.97 123.60 123.60 15 t.3<1 151.34 1.003 1.073 1.073 400 450 450 500 0.070 0.083 0.096 131.93 151.93 164.27 164.27 175.50 175.50 I, 177.78 177.78 195.11 195.11 211.0 211.0 II 1.169 1.210 1.210 1.244 1.244 0.049 0.058 0.066 I I 144.47 144.47 157.89 169.99 169.99 171.81 171.8 I 190.16 207.0 207.0 1.128 1.12S 1.l71 1.171
- 1.206 1.206 550 550 0.108 186.11 IS6.Jl 226.0 I 1.272 1.272 0.075 I
¢ ,
181.28 181.28 222.8 222.8 1.237 1.237
- r r>
Source: SUI/ret: Adapted (romfrom NUlional National Bureau or of Standards, Siandards, Technical Note 648, T.cnnic31 NOle 648, 1973. 1973. \ J_
.1
--------------------~----------~----~------~---------,-.-...-- -- .. *t~zc
~LC P/-~/~-37r*
37S'
... . oISCHARG,E OF DISCHARG.E OF %AIR-AIR THROUGHTHROUGH'A.N ORIFICE(:
AN *ORIFICE .* ;(£F.*LFP3 /3
... ., . .... -... . . 'K-. 1/ .~ 1
- In ciubic In cubic feet of of free free air air per per minute minute at at standard atmospheric pressure standard atmospheric pressure - C> of 14.7 Ib of 14.7 lb per sq. per sq. in. absolute and absolute and 70oF. 70°F. Gauge Gauge DIAMETER OF ORIFICE j: Pressure Pressure before before DIAMETER OF ORIFICE 1 Orifice Orifice 1M" 14"" Ik" IA" 06" 1/61. '/s"' ~"
/4if %" '12" 1/21J. %" *."
3/4
'Va " lip 1"
in Pounds in Pounds per sq. per sq. in.in. Discharge in Discharge in cubic cubic feet feet ofof free free air air per per minute minute 11 .028
.028 .112
.112 .450 1.80
.450 1.80 7.18 7.18 16.2 16.2 28.7 45.0 64.7 45.0 64.7 88.1 88.1 115 115 28.71 22 .040
.040 .158
.158 .633 2.53
.633 2.53 10.1 10.1 22.8 22.8 40.5 40.5. 63.3 91.2 63.3 91.2 124 124 162 162 33 .048
.048 .194
.194 .775 *3.10
.775 3.10 12.4 12.4 27.8 27.8 49.5 49.51 77.5 111 77.5 111 152 152 198 198 44 .056
.056 .223
.223 .892 3.56
.892 3.56 14~3 14.3 32.1 32.1 57.0 57.0 89.2 128 89.2 128 175
.175 228 228 5 .062
.062 .248
.248 .993 3.97
.993 3.97 15.9 15.9 35.7 35.7 63.5 63.51 99.3 143.
99.3 143 195 195 254 254 66
.068
.068 *.272
.272 1.09 1.09 4.34 4.34
- 17.4 17.4
- -39.1 -
39.1 69.5 69.5 109 109 I156 156
- 213 1278 278 77 .073
.073 .293 1.17
.293 1.17 4.68 4.68 18.7 18*7 42.2 75.0 42.2 75.0 J 17 117 168 168 230 230 300 300 99 .083
.083 .331 1.32
.331 1.32 5.30 5.30 21.2 21.2 47.7 84.7 47.7 132 132 191 260 339 339 12 12 .095
.095 .379 1.52
.379 1.52 6.07 6.07 24.3 24.3 54.6 97.0 54.6 152 152 218 218 297 297 388 388 15 15 .105 .420 1.68
.420 1.68 6.72 6.72 26.9 26.9 60.5 108 60.5 108 168 168 242 242 329 329 430 430 20 .
20 .123
.123 .491
.491 11.96 .96 7.86 7.86 31.4 31..4 70.7 126 126 196
-- 283
- 385 I-503 283 385 503 25 25 .140 .562
.562 2.25 2.25 8.98 35.9 8.98 35.9 80.9 144 144 225 323 323 440 575 30 30 .158
.158 .633 2.53
.633 2.53 10.1 10.1 40.5 40.5 91.1 162 162 253 365 496 648 648 35 35 .176 .703
.703 2.812.81 11.3 45.0 101 11.3 101 180 281 405 551 720 720 40 40 .194 .774 3.10
.774 3.10 12.4 12.4 49.6 49.6 112. 112- 198 198 310 310 446 446 607 793
- - 122 - - 487 607 I~
45 45 .211 .845
.845 3.38 13.5 54.1 13.5 54.1 . 122 216 216 338 338 487 662 865 865 50 50 .229 .916
.916 3.663 *.*66 14.714.7 58.6' 58.6' 132 132 135 235 366 366 528 718 718 938 938 60 .264 1.06 1.06 4.23 4.23 16.9 67.6 16.9 67.6 152 152 271 271 423 609 828 828 1082 1082 70 .300 1.20 4.79 19.2 76.7 173 173 307 479 690 939 1227 1227 80 .335 1.34 1.34 5.36 5.36 21.4 85.7 193 343 343 536 771 1050 1050 1371 90 .370 1.48 5.92 1.48 5.92 23.7 23.7 94.8 213 213 379 592 59"2 853
- 1161 1161 1516 1516
*100 100 .406 1.62 6.49 26.0 1.62 26.0 104 234 234 415 415 649 934 1272 1272 1661 1661 110 .441 1.76 1.76 7.05. 7.05- 28.2 113 254 452 705 1016 1383 1383 1806 1 120 .476 1.91 7.62 30.5 122 274 488 762 1097 1494 1951 195\ I 125 .494 11.98
.98 7.90 7_90 31.6 126 284 284. 506 506 790 1138 1549 1549 20231 20231
-:45 - -- -- - -
~
\ 150 . .582 2.37 2.37 99.4 -45 37.5 1 338 600 91 -1315 910 1315 1789 2338-1 2338 200 .761 3.10 12.35 12.35 49.0 196 1961 441 784 1225 1764 2401 240\ 3136 3\36 250*
250 .935 3.80 15.18 60.3 241 542 964 1508 2169 2952 3856 3856 300 .995 4.88 18.08 71 71.8 .8 287 646 1148 1795 2583 2583 3515 3515 4592 4592 400 1.220 5.98 23.81 5.~8 23_81 94.5 378 851 1512 2360 . 3402 4630 4630 6048 6048 sao 1.519 500 7.41 29.55 117.3 469
-- - 1055 1055
- 1876 1876 2930 4221 5745 7504 7504 750 2.240 10,98 10.98 43_85 43.85 174.0 696 1566 1566 2784 4350 6264 8525 8525 11136 11136 1000 2.985 14.60 58.21 1231.0 1231.0 924 2079 3696 5790 8316 11318 11318 14784 14784 Table is based on 1000/0 100% coefficient coefficient of flow. For well rounded rounded en!rance multiply values by 0.97.
0.97. sharp edged orifices aa multiplier of 0.61 may ~e For sherp be used for approximate approximate results. Values for pressures from from 1 to 15 Ibs lbs gauge calculated calculated by standard adiabatic formula. Values for for pressures above 15 lb gauge calculated by approximate 15 Ib approximate formula proposed by S. A. A. Moss. Ac Where: W == 0.5303 ACpW ~ discharge in lbs. per in Ibs. sec per sec , WA = discharge vr, -- area of orifice in sq in. A :::::: area of orifice in sq in. i.-- C = Coefficient of flow
= Coefficient flow I pt = Upstream tctal PI T, =
TI total pressure
== Upstream temperature in pressure in Ibs.
in Of. lbs. per sq.
*F. abs.
sq. in. absolute absolute I; Values used Values in calculating used in calculating above table were; above table were; C C = 1.0, PI
= 1.0, p, == gougegauge .pressure +
pressure + 14.7 lbs./sq. in. 14.7 Ibs./sq. in. ! T, = TI = 530°F. 530°F. abs. Weights (WI correct for dry air were converted (W) were air at 14.7 converted to lbs. per 14.7 Ibs. to volumes per sq. volumes using sq. in. density factor using density pressure and in. absolute pressure factor of of 0.07494 700 F. and 70"F. lbs./cu. ft. 0.07494 lbs./cu. ft. This This is is I. Formula cannot Formula cannot bebe usedused where PI p, isis less less than two times times the the downstream pressure. pressure. (See page 5-10 for (See for a discussion of"?rifice of orifice flow).
_S¥%#Si%1\j¥.,;" ,;j*e*: := Cite, ~ ~ ". ?i:~ F-?L4 N0 2 84r CA°5 p itU..8lQNO 284 002 )023860 3B6 0
- j(cF . P'L )0250.60 284 0025*0,60 7.~~L cF1.. Al .284(
"EACH SVA CItI. !iOTTI)I~ ATOMIC hOTTOM POWEh :;Tf.Tl!;/I
'.T()HIf. I'OWF.h ;TATPI.?i1 liel I' (~n n:1 Y 1 v OJ n i a t a', P,;nnniy'vania 11I!l t:,,
1rrr'E'~
. C. KISTNER C. KISTNER ULCHAIIIM E14I1i[RINlG PAJ.
LlllJl'\lilCAl UI';UlURIIIG 11 R Ha7y 2? , 198 1.
* :'.r nI3 J'
.lldl 19844 FF RHil ilJjl~ : iI. :.;. F I ': i :)I.llman '<<:-<<-:<I~--------1 E. C. Ki'ztn,.r TO:
TO:
- IJ*O J r: C T :
- UJ-3JJE(T: HOD REQUr::;*j 1HOD REQUE:;T ilU ilu.. JI.jCJ 14 39 - PiiIHA Pillf~"il'( 'R f:r:!I'j,*,I1Il~r:*IIT
... ,,TA I .1. VENIT
'.'F:IIT
;FT AUD PNEIUMATIC !;l!PPLIE::;.
A!ID PURGE I'IlEIJJrI;'TiC SUPPLJE:. IlErEflEIlCF.: REFERENCEK: Memorandum, J.ip.liIorandum, J.J. I.. L.. Horro'" Horrow dated dated .4/,'1/34 1,//'d:J1, Tho referenced memorandum The referenced memorandum provides pr0vidc3 lc~knBe leakage criteria criteria pneumatlc for pneucatlc
~upplle~ to supplles containment vent Lo contnlnment vent and purge purge valves. valve3. The memo memo con:Jlc:ler.:J leakage conoider3 Ip.,]I<~e;e up. to }O SCCM 1O wlth a r.equll'ed
- >I.:CI1 with required nitrogen nitrogen bottle change bottle ch~nBa before before bottle bottle pressure pre3:Jure 13 len3 le~3 than 15~O 1550 psig. p~ig.
Aclu~1 leakage Actual leaKage rate~ rates are :Jlenlflcnntl, 3ignificant1y p,renler, greater, on the order order of 50 ')0 to 150 150 Sc4. !;CCH. Rc'palr of RPpalr or any an:l one component coeponent on these the:Je air *3 u p p 1 'J system3.
-Supply !l :I s t c ms. 1!l is not in indicated rj i c OJ ted :J inc e ~several Since i? v P. r;j 1 co components 1:1 P 0 n e n t!l cQntribute contribute .. . 3nal~lamount3..
- J~all'amount:J ..
Some undocu6ented experience
,one undocumented experience with local local leak rate rate tCJllngtesting and the ILRT ILRT indicatesindicates that that a 1033 ]oa3 or pneumatic pressure of pneumatic pre!l~ure on a closed cloJed purge or vent valve doeJ does not rC!lult result In in gross gros~
leakage. leakage. It It i1 estimated that. leakage would be le~3 13 c!llimated less .than than .~ 600 scc foro oat case 600 SeeH for mo~t C3!lC3. Leakage at this rate would not Leakage at th13 rate w6uld not -fo:~f)
- Jerlou31y degrade primary primary (onlainQentcontainment Integrlty~ Integrity'. f;.l 1:],7l;~
Seriously degrade
.-:::t:;~!.;...
~f'.r~
. Plc3Je Pica3e !nveJligaleinventigate nltp.rnntive~ alternative3 to the prc3cnt present lOO O00 day sarety safety grade pcnumallc penumatic Jupply. supply. Pre3ent pneumatic PreJenl pneucallc syntem sYJlem leak leak rale3 rates cannot be 1eproved cannol improved wilh with lasting results. re~ultJ. The Station 3tatlon will will Support Jupport any investigatlon Inve:Jtlgatl~n needed to formally formally downgrade downgr~de the lroportance importance of thlJ this ~arClY Safety grade air air determine reaIIstjc or to determine reali:Jl~c cap~clt!cj for alt~rnat!~c capacities alternative :Jupply Supply ~1:JlcmJ. systemz.
!ir r you hhave- a '1 I!. 3any 11 Y questiona,
'l u c :; t ion ~ , plp'~JP' please contact JIm contact .Jia Mit~anlittman of of my
.ptarf.
ptarr. M--- il. Z.
,l. ~.
- 'tation
~latlon Fleischmann FlelJchoann ZuperintendenL
~uperlntcndenl PF/!JFJ4: lhd r:;f/.JFH:
APPIOVAL J\PPIlOVA!. TO (JOYAIII OBTA III FiTIHATEf.:JTIHATi:: APPROVAl. OF
',Pl'kOVf.L OF CAPITAL CAPITAL flEQUr:Si R.OUFS" A t tarihmo nt p.*
J ****
" . "':, . ' '.' REF IS-
?c. j 6l*.i .. ' ... . TO: . Tapan Tapan Banerjee' Banerjee ." . ... ':. ' . " :: ........ . - .
FROM: Linda Y. Mast Linda Y. Mast . .
SUBJECT:
SUBJECT:
Mod 1316 Acceptance Mod 1316 Acceptance CrITeria Criteria for dual dual unit unit operation operation'
- .'" : ... :. '. - .. , '.': -:", .. '.':, .:-:.. :.!.~".. -'-:"- "';.. _.. '. -::-. ---:: :...
- **j~~25.1m**:':,:7 June25,1990 .,
Mod Mod 1316 1316 IsIsscheduled scheduled for completion during the next next refueling outage for unit 2. This will This will result result in in both both unit 2 and unit unit 3 being supplied supplied from the common CAD tank supply. During During the past the past unit unit 33 refueling refueling outage, outage, the mod was installed installed and accepted based on acceptance acceptance criteria criteria established established in in the the Engineering Engineering Work Letter for Mod 1316, Rev Rev 20. This criteria, criteria, however' however
.only only considered one operation..
one unit in operation
.; . MT tn As As the the system system engineer engineer for Primary Containment. Containment, II do not not think it it isis possible to do
, MAT testing that will SMAT testing that will directly directly affect unit 3.
3, which will be in in operation at the time of the MAT for unit 2, because of the risk
- 2. because of the risk of violating of violating primary containment containment integrity. Decreasing boot pressure seal pressure to less than acceptable to less than acceptable (67 (67 psig) psig) results in the valve being inoperable for containment isolation.
believe that the condition for which we want to prove Mod 1316 isisa lOCA II believe LOCA on one one unit with four unit with four containment containment butterfly valves open and the other unit in in safe shutdown. shutdown. This is is based on thethe unit 3 criteria and talks with you on the subject The Safety. subject.. .The Safety Grade .Instrument Gas Grade Jnstrument Gas based on Supply Supply (SGIG), (SGIG), will will have have to to be capable of closing the four open containment containment valves valve5 within 5 . seconds, seconds, as as well well as as supply maintain 67 psig on all of the remaining supply and maintain remaining boot seals and-provide and* provide pressure to pressure keep the torus to reactor building vacuum breakers closed. The unit in to keep safe in safe shutdown will require shutdown will require boot seal boot seal pressure and pressure to the torus to reactor building vacuum breakers. This breakers. This usage usage will have to be simulated due to the operating operoting condition of unit 3 at 3 the at the time of the unit the unit 2 MAT. 2 MAT. think that the best way to simulate this unit 3 usage II think usage is is to set up unit unit 22 for SGIG supply for SGIG supply lineup lineup andand measure measure the flow through the SGIG pressure pressure control valve. This flow will represent the represent the leakage of the SGIG system. This leakage leakage leakage can be scaled up by some factor to factor to simulate 'worst simulate 'worst case leakage.* The unit 22 MAT can then be performed case leakage." performed with this leakage established to to represent represent unit 3unIT 3 usage using criteria similar to that used for unit 3. This will will allow allow testing testing without without disturbing disturbing unit 3 operating operating conditions. The SGIG system will be isolated isolated from from unit unit 3 3 by by one one manual manual valve with personnel stationed stationed at the valve for quick restoration restoration if if required. One additional change One change I would like like to see from the unit 3 acceptance acceptance criteria is is the the minimum pressure required minimum pressure required at the Clow torus to reactor reactor building building vacuum breaker, breaker, AO-2(3)502B. AO-2(3)502B. This pressure should be 75 psig as specified specified by the manufacturer manufacturer and not not 80 80 psigpsig as as shownshown in in the the EWL rev 20. EWl If you would like If meeting to discuss the development like to have a meeting development of of acceptance acceotonce criteria or need clarification on any of the above. need clarification above, please please feel free to call me me at X4972., Peach at X4972., Peach Bottom.
,~~,~6)fpV Linda Y.
Linda Y. Mast Mast Station Engineer for Mod 1316
~ ..
Station Engineer for Mod 1316
. * * * . * ' ......... -....... !~. " - :", " , ' : ' * . "
Plant Division Plant Division /*'F b , ~ .
. ~;: ',' -. - Technical Section Technical Section =====. ."
~?G~ ,1 - d\:=
.... . - Oec~m'ber'4, *1989-December.4, 1989 FROM:
FROM: J. A. J. A. Jordan
. ...;. '::," -.: .... ~
TO: TO: -MOD MOD 1316 File 1316 File Peach Bottom Peach Bottom Atomic Atomic Power Power Station
SUBJECT:
MOD
SUBJECT:
MOO 1316 1316 Memorandum Memorandum Regarding Regarding interpretation Interpretation Of Loss Of Instrument Air Loss Of Instrument Air Criteria For Criteria For Testing MOD 1316 1316 'wasdesigned provide aa safety was designed to provide safety grade grade pneumatic pneumatic backup backup supply supply lo- 10" . CAD CAD and CAC CAC system system valves valves which which are are normally normally supplied supplied by by instrument instrument air. air. -
-. Design Design of.the of the system system requires requires that this backup backup -system be be operable operable "upon"upon loss loss
-of of the normal supply system" systemll (reference (reference letter fromS.
letter from Oaltroff to S. L. Daltroff NRC to NRC Chief J. J. F. F. Stolz, Stolz, dated November November 6, 1985). 1985). The EngineeringEngineering Work Letter Letter (Rev. (Rev. 18 18 dated dated November November 14,14, 1989) specified as 1989) specified as part of part of the the MAT acceptance acceptance criteria criteria that instrument instrument air to the SGIG supplied valves be valved valved out but and vented. vented. The Station'sinterpretation Station's interpretation of this this criteria was that prior to functional criteria functional testing of the CAC CAe and and CAD valves with the SGIG system, system, measures would would-be taken to ensure be taken ensure that air pressure in the valve boot seals seals and associated tubing"would associated tubing would be vented. vented. The The MAT was set up-to '-.- set.'up~to . ... -.,_. __ .. --- make sure make sure that this criteria criteria was met. met. In order order to ensure ensure aa conservative conservative interpretation interpretation of the design criteria criteria relative to loss of the instrument air system, system, itit was decided to perform a test test on the instrument instrument air supply lines to individual users. useis. This test would would ensure that (1) the check check valves valves on the supply lines (siesmic boundary boundary between instrument air and SGIG system) would prevent instrument preveht backflow of SGIG - supplied nitrogen out of the valve valve operators operators and associated tubing tUbing when the normal air air supply was lost, lost, and (2) the manual valves which isolated instrument air from from
,the
,the individual users during the testing did not leak through (which could have have masked an inability of the SGIG system to satisfactorily operate satisfactorily operate the valves).
valves). The results of this test are attached. attached. . . The test results indicate that there was no leakage through any of the the. check valves that isolate SGIG from the normal air supply or through the . manual valves that isolate the normal air supply from the valve operators-. operators.. These results, results, along with the MAT results, meet the conservative conservative interpretation interpretation of the design criteria speCified specified ii the EWL.EWL. React React S *ems Engineer Supervisor JAJ:gkm JAJ:gkm Attachments (4) (4) cc: H. H. G. G. Coleman J. G. Hufnagel, Jr. G. Hufnagel, Jr. J. L. Y. Y. ~last Mast s.S. F.F. Payton
R*E F /7 .. --- _CDF:0 I1. 5)
- 5) After taking .a random sampling of bottle leakage_ (reviewing "
results of. ST 7.9.2),. the bottles'-lose an average of..32 psig per week. This ST procedure. currently calls for the.replacement of bottles when the pressure falls below 1,300 psig. --The-curreht-
.:achievable a minimum bottle pressure o "30P psig willmaintain..a 20-day-supply..: Based on a review ofT-"
past ST77.9.2 -records, the bottles would have to be replaced approximately every twenty-eight weeks assuming an initial bottle pressure of 2200 psig.
\-_) Yewnoc-qC) PQA moo
-AO
~1-~1i jli7-"
,68
" (1.-<
lh tJ 1.1-~Pi, Jc,r! (1- ... . . . Prepared Prepared by: S. F.
- s. F. Payton 2, 1 ~
.J.1.
Decemb December er 27, 1989 .. SFP1289.1 SFP1289.1 LLPW dct)*15-bry aj, On4J~- .:, (,P Tos+ 0 T *up &1*-c5+am-cx. 9 0 FOD-D5.
*oO- ASk (5 c&~m Ro- -15OP (05 scc,S+/- A ~X c*.
vc-Sz, C&'M Ln*, s(. WOr'S+ vc). \~ ::to c.on X 1.'5 S<.c. fI) u.Xs vdolQC\ --Tent r xd.c;s..fY')srcf. _ __cI 0PYQ 5S-uor c o- 5028 0 2*0 PO-a5ý0
,5wZ, FA~r C) we 2 . _ .p.- -5l s
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ý5yTf\ -4ý r c~o.'
,Q5 5C rr-) z9ýr csYx 2un' [(A- -) 1 cý5 4 GOr klY4-5O 0~y -TLrc sýJ 7JcuýS ,
.,. ,.~~('.... : .;' .. : .....
10:09 U'.I03' 332 2" 139. SPROCESS 3 c, _
- PROCESS EN"GINE.:.ER.:J::N"G INC_
~ ::. .': P.O. BOX P.O. BOX 467 467 ...... -.
.... : '.. PLhlSTOW PLA ISTOW,r Ha NH 03865 03865 TEL: 603-382-6551 603-382-6551
... PAX: 603-382-2139 FA: 603-382-2l39
~: ... '
- "*. t . .
~ .'
Date: 07/25/90 company: company: PhiJ.adelphia Electric Philadelphia Electric Attention: Attention: Tapan Banerjee Tapan Banerj ee Telephone No-: Teleptiofe No.: 215-640-6474 215-640-6474 (- 3-Pax No-: Fax No.: *215-640-6582 215-640-6-582 We are transmitting transmitting 04 pages, pages, including including tn;s ths page, page, to the person person listed listed aboVE~. above. Should you have any proble::::tS Should prob!e-s and/or uo not receive
<3-"'ld/or do all the page, all page, please please let let us 'know know by calling calling (603) 382-6551 and ask (603) 382-6551 for for extension 2163.
extension 2l63.
~ttacbed are ~ee Attcached three conte~ts c~2Its for the refe~6nced contemts charts referenced units_ units. -Mmey Tney axe are calculated ca1culated based r~~ogen p=ope~es based on nitrogen properties et at 0 psig, 170 170 psig and 250 psig, ps~g, per per
.... '. -your re~~est_ your reqaest. The .c~t chart at 0 psig is for COEpa-~son psi5 is compazison to your o_2_g1_ c~ vour original cbar-..
.:' ...... -::.. The ... alues ;5Ia identical. .D2 close, but not idam::ical. All of thesetbese charts ue based on are based on
-' :'. :'.-:; values are close, very limited limited research into ~to these nov year old units, sev6ntaell yea-DOw sevezzeen. should be units, and should used for ~o~.refererrce reference or~yo-*y..
Liquid height: linear inches is in linea height i.1l relaedto 1:0 ;;he
- i.s related reading of gage J:eao.fug
_..e gage of "-ches "i1:lches o:E
. .of.....water coitm- by
-at:er c01U1Im by- the aq:ua.d.on:
equarion: linea=
~inea:r incches inches (inches H2 0 column)(.036 psi/inch of H2 0 colun) densi-t -- lbs/in 3
aens1.:::Y -- 1oS/1.D:
-* 3
?ron:
?ron: Scott Scott C. Nason Nason DesignC.Engineer Design U"lgineer cc: Ken PaQl, Paul, PEIPEI Ref:
Ref:C-383-*38573 C-383-38573 (Model E-6000-special) (Model H-6000-special)
.OT".25/90 10:10 .- T603 3. 2 2139 PROCESS EXGRG-PROCESS - NGINEERIN~G.-10 &~(Z ~L P Tjt, ~WE'ST 3
- M~OD=, 00 P~A Conversion.fron Conversion inches of water fron inches water column col~~ to liquid liauid volume considers vanor volume considers vacor volume with volume d~lSity ofj.0.28700 with density of.0.Z8700 ibs/cu.ft. lbsjcu.ft.** Material shri~~age is.
ateria! sb-i-kage is* 0.00291 0.00291 weight and MSCF Weight MSCF are are for !iaculidliquid only.. only ~ ~ .' . . ... .. . -.
.LIQUID LIQlTID NITROGGEN.
NITROGBf@ abn.
@ 21. atm. 50.4020 lbs/cu.ft.
50.4020 lbs/cu.ft. 13.803 scf/lb 13.803 sCfjlb
.' pomms MSCF IN.E20 HýCF Dr .H20 2.L1.H20 Gp,T,T:OUS GAT.LLONS POUNDS .E20 GAL.LONS GALLONS poDUS POUtIDS ¥.:.SCF
. ".-' 0.00 0.00 0 0 0.0 0.0 ~5.00 45.00 4,298 4,298 28,958 28,958 399.7 399.7 1.00 l.00 11 77 !
...1.1 46.00 46.00 ...4,4!2 4,412 29,725 29,725 410.3 41.0.3
...... :.200 2.00 39 39 . 264-264: . 3.7 3.7' '.47.00-
~7.00* . :4,524
- 4,524 .' 30,484 30,484 420.8 420.8 3.00 3.00 77 517.
517 7.1* 7.1. .. 48.00 48.00 4-,636 4,636 . 31,235. 31,235. 431.1 431.1 4.00 4.00 1.22 122 822 822 1l.3 11.3 49.00 49.00 4,746 4,746 31,978 31,978 441.4 41:1.4-5.00 17L', 174 1.,170 1,170 1,6.1 16.1 50.00 50.00 4,855 4,855 . 32,712 32,712 451.5 451..5 6.00 231 1,557 1,557 21,.5 21.5 51.00 5l.00 4,962 33,435 461.5 461..5 7.00 294-294 1,578 1,978 27.3 52.00 5,068 34,147 471.3 471.3 '" ..: 34,847 481.0
. 8.00 8.00 361 2 r 431 2,431 33.6 53.00 53.00 5,172 5,1.72 .34,847 .481.0 9.00 432 2,913.
2,913. 40.2 54.00 54.00 5,274 5,274 35,535 490.5 490.5
'\ 10.00 508 3,421 3,421, 47.2 .. 55.00 5,374 5,374.- 36,208 36,208 499.8 499.8 54 ~6' 56.00 5,472 36,866 508.9 11.00 587 3,955 54.6- 56.00 5,472 36,866 508.9
- 12.00 12.00 670 4,511 4,511 62.3 57.00 57.00 5,567 5,567 37,509 37,509 517.7 517.7 113..00 13.*00 755 5,089 *70_2
.70.2 58.00 58.00 5,660 38,135 38,135 526.4 526.4
-14.00
'14.00 844: .. .5,687 844- 5,687 78.5 59.00 5,750 38,742 38,742 534.8 534.8 1.5.00 15.00 936 6,304-6,304 87.0 60.00 5,837 5,837 39,330-39,:330 542.9 542~9 i6.00 16.00 1,030 1,030 6,938 6,938 95_8 95-8 61.00 5,921 5,921 39,897 39,897 550.7 550.7 17.00
.17.00 1,126 1,126 7,589 104.8 62-00 62.00 6,002
'6,002 40,442 40,442 558.2 558.2 18.00 18.00 1,22:;
1,225 8,255 113.9 11.3.9 19.00 1,326 1,326 8,936 123.3 123.3 20.00 1.,429 1,429 9,630 132.9 132.9 21-00 21.00 1,534-1,534 10,336 1.42.7 142.7
.-. 22.00 1,641.
1,641 11,054 11,054 1,52.6 152.6
- - 23.00 1,749 11,782 12,782 162.6 162.6
. ,.,:: \
24.00 24-00 1.,858 1, 858 1.2,521 12,521 1,72_8 172-8
.. ~ ,"' . ,',i. ' 25.00 25-00 1/969 1,969) 13,268 13,268 183.1 183.1.
26.00 . 26.00 2,081-' 14,024 2,081 -1 024 1.93.6 193.6
- '-':"'; .. 14,737 204.1 204.1
""'.:.: 27.00 2,195 2,195 14,787 28.00 2,309 15,557 15,557 2l4.7 224.7 29.00 29-00 2,424-2,424 16,332 16,332 225-4 225~4 30.00 2,540
.2,540 17,113 236.2 236.2 31-00 31.00 2,656 2,656 17,89B 17,896 247.0 247.0
- 32.00 2,773 18,687" 18,687" '257.9 257.9 33.00 2,891.
2,89J. 19,479 263.9 34.00 3,009 20,27'3 20,273 279.8 .. 35.00 *3,1.27 3500 "3,127 21,069..290 "290~3' ,
'21.,069' 36.00 36.00 ,24:)
33,24:5 21,865 21.,865 301.8 301-8 37;00 S27*00 3,363 22,662 22,662 312.8 31.2.8 38.00 38.00 33,482" I
~",,).
_o~ 23,459 323.8 322.8 39.00 39.00 3,600 3,600 24,254 24,254.- 334.8 334.2 40.00 40.00 3,717 3,717 25,047 345.7 345.7 4-1.00 41..00 3,835 25,837 356.6 ";:.< 42.00 42.00 3,951 3,951. 26,624 26,62~ 367.5 367.5 43.00 4,068 '27,407* 27,407 -...: 378.3 378.3 44.00 ..... 4,183 . 28,1,85 28,185 389.0 - 25-Jul-90
'., . O!3'0 ***10:10 Oil25/90 10:10 . 'B60;}
'E603 3829 2139 .~,.
382 2139 . *;_**~~J5.9CE.~LE:)!* PROCESS ENi N003. .. :.,..... gOOL ,.;*gt~~;t;2~~~2~~~iii~lf!i~'~I~I~f~~~t~l.~l~~f[~~~1!i'0t
~.".
* . .. . . .. . . '--HODEL-10DIEL H~*6000-Sp.ECn H- 6000 SPE'CLIn"
' . /* * * '. :. " * * * * *_ _ _* * * ' _ * 'oW _... * ****** ** " * * '" _,'
Conversion Conversion froJjl froni inches off of water column colmnn to liquid volume VOlUJIle considers vaDor vapor
- ":-;".- .volUlUe volue 'Hith with density of 3.33560 3. 33560 . Ibs/cu.f"t.Material bs/cu. ft.: Material shr.Ln_J<.ageis sPhrin~kage 0. 0o291 is :0.00291 weight and- 25CI? are Weighit and'MSCY are for liquidll-acid only~ only.
. '~:~':.\
- :: ~ :::J"4-LIQUID NTTROGEH LIQUID NITR.0Gal @ 170 PSIG
@ 170 PSIC- 39.9292 Lns/cu.ft. lbs/cu.ft. 13.803 scfjlb 13.803 scf/Tb I2{.H20 IH.E20 GALLONS G1>LLONS POuNDS PC-U-NDS MLSCF
}ISCF ZN .E.20 I.N .R20 2 GA LLONS GALL-cms POUN1DS POu~"DS 1{SCF 1{SCF 4.50 0 0 -0.0
-0.0 27.50 2,7J.7
.2,717 14,505 l4- ,50S . 200-2 200.2 14,933
. 5.00 5.00 6 30 30 0.4 0.4 ....
- 28.00 28.00. 2,798 2,798 "14,933 206.1 206.l*
1.5 1..5 28-50 2,878 15,363.. 212.1 5.50 21 112 112 28.50 2,878 15.1 363 . 2l2.l 6.00
*6.00 42 42 223 223 3.1 3.1 29.00 2,959 2,959 15,794 15,794 218.0 218.0 6.50 67 358 358 4.9 4.9 29.50 3,040 3,040 16,225 16,225 224.0 224.0 7.P0 7.,00 96 96 513 513 7.1 7.1. 30.00 3,121 3,121. 16,657 229.9 229.9
*:.~ .'
7.50 128 123 685 685 9.5 9.5 30 .50 30.50 3,201 17,089 17,089 235.9 235.9 161, 164 874 12.1 12.1 31.00 3,282 17,521 .241.8 8.00 874: 3.1 282 17,521 241..8 8.50 202 2,077 J., 077* 14.9 14:.9 31.50 3,363 17,953 17,953 247.8 247.8 9.00 242 1,293 17.9 . 17.9 32.00 3,444 18,385 18,385 253.8 253.8 9.50 285 285 1,522 21.0 21.0 32.50 '3,525 8 ,817 18,817 259.7 259.7 10.00 10.00 330 330 1,763 24 -3 24.3 33.00 3,606 3,606 19,248 19,248 265.7 265.7 10.50 378 378 2,016 27.8 27.8 33.50 3,687 19,678 271.6 27:1.6
"" 11':00 006 1:1. 300" Ii 427 2,278 31.4 31.4- 34. 00 34~OO 3,767 3,767 20,'108 20 ,'~08 277.5*
277.5 11.50 11..50 478 478 2,551 35.2 35.2 34-50 34~50 3,847 3,847 20,536 20,536 233.5 233.5 12.00 532 531. 2,833 2,833 39.1 39.1 35.00 3,927 3,927 20,963 20 1 963 289.4 289.4-
. ,'**~t**** . .1 35.50 4,007 21,389 12.50 12.50 585 585 3,124-3,124 43.1 4;007 21,389 295.2 295.2 13.00 641 64J. 3,424 3,424 47.3
. 47.3 36.00 36.00 4,087 4,087 21,813 21,813 301.1 301.1
. 36.50
~
. 13.50 13,50 699 699 3,732 3,732 51.5 51.5 36.30 4,166 4,J.66 22,235 22 1 235 306.9 306.9
- r:~:cr&'- ,*'"
... 758 4,047 55.9 55.9 37.00 37.00 4,244 22,655 22 1 655 312.7 312.7 i4.50 14.50 819 4,370 60.3 60.3 37.50 37.50 4,323 23,073 23,073 318.5 318.5 15.00 881 88~ 4,701 64.9 64.9 38.00 4,400 23,489 23,4-89 324-2 324.2 15.50 15.50 944 5,038 69.5 69.5 38.50 38.50 4,478 23,902 329.9 944- 4,478 23,902 329.9 16.00 1,008 1,008 5,381 5,381 74.3 74.3 39.00 39.00 4,555 24,312 24,312 335.6 335.6
- 16.50 1,074 5,731 79.1 79.1 39.50 39.50 4,631 24,719 341.2 1,074 4,631 24,719 341..2
.17.00 84.0 84.0 40.00 4,707 25,123 346.8
. 17.00 1,140 . 6,086 4,707 25,123 34:6.8 17.50 27.50 1,208 1,208 6,448 6,4:48 89.0 89.0 40.50 4,782 4,782 25,524 25,524 352.3 352.3 i8. 00 1.8.00 1,277 1,277 6,814 6,814- 94.1 94.1 41.00 4,856 4,856 25,921 25,92l 357.8 357.8 18.50 1,346 1,346 7,186 7,186 99.2 99.2 41.50 4,930 26,314 26,314- 363.2 363.2 19.00 1.9.00 1,417 1.,41,7 7,563 7/563 104.4 104.4 42.00 5,003 5,003 26,703 26/703 368.6 368.6 19.50 1.9.50 1,4&3 1,483 7,944 109.7 109.7 42-50 42.50 5,075 . ...27,088 27,088 373.9 373.9 20.00 1,561 2,56J. 8,330 8~330 115.0 21.5.0 43.00 43.00 5,146 5 1 1.46 27,468 27,468' .* 379.1 379.1 20.50 1,634 1,634- 8,720 120.4 120.4 43.50 43.50 5,216 5,216 27,844 27,844 384.3 334.3 21.00 1,707 1,707 9,. 14 9,1.14- 125.8 125.3 44.00 44.00 -5,286
- 5,286 .. 28,215 28,215 389.4 389.4 21.50 91;512.
131.3 " ' .. 4:z4.50 23..50 1.,782 1,782 .: 9;512 .. '1.31.3 44-.50 . 5,354 5~354: h281580
.28;580 . 294.5 394.5 22.00 1,857 9,913 136.8 136.8 45.00 5,-22 399.5 22.00 i,ss7 45.00 5,422 28,941
- 28/941. 399.5 22.50 1,933 1.,933 10,318 1.0,318 142.4 1.42.4- 45.50 5,48a 5,488 29,295 29,295 404.4 404.4 23.00 2,009 10,725 10,725 148.0 46.00 46.00 29,644 409.2
*... ~
5,554 29,644 4-09.2
..:..... 23.50 2,086 11,136 11,136 153.7 153.7 46.50 5,618 5,618 29,986 29,986 413.9 413.9 24.00 2,164 2,164 11,550 159-.4 ~:.
159.4 47.00 4:7.00 5,681 5,681 30,321 30,321 Z1!8.5
~18.5 24.50 2,242 11,966 11.,966 165.2 165.2 47.50 4:7.50 5,742 5,742 30,650 423.1 30,650 423.1 25.00 2,320 12,384 12,384- 170.9 170.9 48.00 4-8.00 5,802 5,802 30,972 30,972 427.5 427.5 25.50 2,399 12,805 176.7 176.7
- 48.50
~8.50 5,861.
5,861 31,286 31/286 431.88 431.
,": 26.00 26.00 ...2,478 13,227 182.6 182.6 * -- 49.00 5,919 31,592 436.1
',' ~. 2,478 49.00 31 1 592 436.1 26,'50 26.50 188.4 49.50 440.2 2,558 13,652 188.4- 49.50 5,974 31,890 31 / 890 440.2 27.00 194.3 6,029 2,637 14,077 294.3 50.00 6,029 32,180 32,180 444.2 444.2 5-Jul--90 25-Jul-90
07/25/90
.- 10,1.1 'IE603 382:2139 *---. .PRI)CESS.E\NGRG.
7*J- 1 3ý
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conversion frO~1 Conversion fromi inches of wcter water colma~ coluunn to liquid volume consid~s considers vanorvaror volUlile with volume ,..-ithdensity density of 5';04800 5'04800 l.bs/cu~ft~ Tbs/cu.ft- Material ateria! sbri..!"l.kage shrinkage is is 0.00291 0.00291 Weight and MSCF ¥...5CF are for liguid only.
-Fr . liquid only.
36.8110 lbs/c,.rft. 36.8110 lbs/~~.ft. 13.803 scf/lb 13.803 scf/2b LIQUID NITROGEN-LIQUID NITROGTIT @ @ 250 PSIG
.. .:'::....... MScCF 22{.?R20 lli.E20 POUN1DIS KSCF
,IN .H20, G
.2N.R20. G~.LI.'()NS A L.ONS POu-hDS peilli"DS HSCF G:;'i.T:ONS CIILN POm-illS ESCF
'. -0.0 216.7
-;'~,'
~. . 7.00.
7.00 a0 a0
- 38 -:-0.0
' 0.5 " 29.50 29.50 3,190 3,190. 15,698 16,157 216.7 223.0
'33 . '0.5 30.00 30.00 3,283
***.3,283 1.6,iS7 223.0
.r: 7.50 8 1.8 .. 3,377 .229.4
.8.00 133 1..8 30.50.
30.50. 3,377 16,616
- 16,616 _229.4:
.. :~.;;~ . 8.00 27 27 133 262 3.6 3.6 31.00 3,470 17,075 17,075 235.7 235.7
,. 8.50 53
.53 262 31.00 3,470
'7,:'.',- 417 5.8 31.50 3,563 17,533 242.0 9.00 9.00 85 85 417 5.8 31.50 3,563 17,533 242.0
.... .. - 595 8.2 8.2 32.00 32.00 3,656 3,656 17,991 17,991 248.3 248.3 9.50 121 121 595 793 '0.9 32.50 3,749 18,447 254.6 254.6 10.00 16j.
163. 793 10.9 32.50 3,749 1.8,447 1,008 23.9 .33.00 3,8421 18,902 260.9 260.9 10.50 1.0.50 205 205 1,008 13.9 .33.00 3,841 18,902 1,240 17.2. 33.50 3,933 19,356 267.2 1i.00 11.00 252 1,240' 17.1 33.50 3,933 19,356 267.2
*1,488 20.5 20.5 34.00 34.00 4,025 4,025 19,808.
1.9,808. 273.4 273.4 11 50. lL50 302 302 1,438 1,749 24.1 24.l 34.50 4,117 20,258 279.6 279.6 12.00 355 355 1,749 34.50 4,117 20,258 2,024 27.9 35.00 4,208 20,705 235.8 12.50 41J. 42.2. 2,024- 27.9 35.00 4,208 20,705 285.8 2,311 31.9 35.50 4,298 21,150 291.9 1.3.00 13.00 .470
,470 2;3U. 31.9 35.50 4,298 21.,150 291.9 2,610 36.0 36.'0 36.00
-36.00 4/388 21,592 298.0 298.0 13.50 530 530 2,610 4;388 21 1 592 2,920 40.3
- 40.3 36.50 4,477 22,031 304..
14.00 24.00 593 593 2,920 36.50 4,4-77 22,031 304.1 3,240 44.7 44.7 37.00 4,565 22,466 22,466 310.1 14.50 6Sg 658 3,240 37.00 4,565 310.1 3,570 49-3
'4-9.3 37.50 4,653 22,898 316.1 15.00 725 725 3,570 37.50 4,653 22,898 316.1 3,909 54.0 54.0 38.00 4,740 23,326 322.0 15.50 25.50 794 794- 3,909 38.00 4,740 23,326 322.0 4,258 58.8 38.50 4,826 23,749 327.8 16.00 865 865 4,258 58.8 38.50 4,826 23,749 327.8
... 4,614- 63.7 39.00 4,911 24,168 333.6
- '- ,':.. ;'. 16.50 938 938 4,614- 63.7 39.00 4,911 24,168 333.6
- ~.~ ;..': 68.7 68.7 39.50 4,995 24,582 339.3 17.00 2,012 1,012 4,979 39.50 4,995 24,582 339.3
~.,-:- .. 5,351 73-9 40.00 5,079 24,991 345.0 17.50 i,087 1,087 5,351- 73.9 40.00 5,079 24,991 34-5.0
.. :. 5,731 79-1 40.50 5,161 25,395 350.5 18.00 1,16~i 1,1:65 5/731- 79.1 40.50 5,1.61 25,395 350.5
- " . \
6,117 84-4 41.00 5,241 25,792 356.0
,- , . 18.50 1,243 6,1.1.7 84.? 41..00 5,241 25,792 356.0 6,510 89.9.
89.9. 41.50 5,32a. 26,184 361.4 19.00 19.00 1,323 6,51.0 41.. 50 5,321_ 26,184 361-4 6,909 95.4 42.00 5,399 26,569 366.7 i9.50 19.50 1,404 1,4-04 '6,909 95.4- 42.00 5,399 26,569 366.7 7,313 100.9 42.50 5,476 26,947 371.9 20.00 1,486 7,31.3 100.9 42~50 5,4:76 26,947 371.9
- .. 43.00 5,551 27,318 377.1 20.50 1,569 7,723 7,723 106.6 106.6 43.00 5,551 27,318 377.1 21.00 1,654. 8,138 112.3 11.2.3 43.50 5,625 27,681 :
27,681 382.2. 21.00 I, 65~~ 8,138 4:3.50 5,625 332.1 8,558 118.1 118.1 44. 00 5,697 28,036 387.0 21.50 1,739 1,739 8,558 44.00 5,697 28,036 387.0 8,982 124.0 44.50 5,768. 28,383 391.8
.. '.;': 22.00 1,825 2,825 8,982 124.0 44.50 5,763. 28,383 391.8 ; .' ~
9,411 129.9 129.9 '45.00 5,836 28,720 396.4
.' 22.50 1,912 1,912 9,411 45.00 5,836 28,720 396.4 2,000 9,843 135-9 135.9 45.50 5,903 29,04* 401.0
; 23.00 9,843 45.50 5,903 29,048 401.0 10,280 2.4-.1-9 '46-00 _ ._5,968
'46.00 5,968 * ....29,367 405.3
- ,:-23.50,
"'.:-23.50' . 2.1 089 2,089 .10,280 .. 14L9 29 r 367 405.3 148.0 46.50
-24. 00 24.00 2,178 10,719
'10,719 148.0 46~506,036 6,030 29,674 29~674: .' . 409.6 409.6
!1,162 154.1 24.50 2,268 2 1 263 11,162 154.1 25.00 25.00 2,359 2 1 359 11,607 21,607 160-2 160.2
" .~
22,450 .!2,055
.12,055 166.4 1.66.4 25.50 1 450
" .. 2,541 12,505 12,505 172.6 1.72.6 26.00
'26.00 2,5~l 26.50 2,633 12,957 12,957 178.8<3 178.8,;:
13,411 185.2. 185.1 . 27.00 2,725 13,411 2,818 13,867 13,867 191.4 1.91. 4 27.50 28.00 2/91J. 2,911 14,323 14,323' 197.7 197.7 S28.50 3,004
*3, OOL~ 14,781 14,781. 204-0 204.0
'28.50 3,097 3,097 15,239 15,239 210.3 210.3 29.00 25-JJul-90 25-Jul-90
GI/-LC. Prl - '37 S
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FHlLAUElPHIS. EIEcr~ac coCOiUIZILt *. GO., TJJ4STA.LLATION. --- MTRCTIONS-4FI~iM
---, ~ -- ....
AAIIMSIS & ijt~AwXIGS llJSTALIATION HOD~A# 1007 INSTRUCI'IONs-FLSHER C01ITIWLS co.
'ANALYSIS & lJR1l..WINGS M01# 1007 PiO 6280 M 117L-74-1 . ;-":".- ....-.
P.F# 6280 :M 117'-74-1 Al TROM RILA.XZING 1298 AI'PRDVED ll.A.KING i I'
AND AFqiXi NOT CO$N1 RLEO. P~ec,.2 0 F1 CO.NSULT DRAMING C' T dIg -2 O Type*9200
*FOR .:SSIBLE L~lER M-117-:-74
. CtlFFOnU B. WES LS &
& CO., INC.
~. 601 Cl1010H Oil RDO [10M)
- t~rm Of pnUSSlf~ Iill, P A. 1946a Pi\. 19~U~
PuWss OF (215) 331-4%0 fip V~OH~ t, Instruction Manual Instruction Manual -7 Type 9200 T-Ring T-Ring*Butterfly Butterfly Valve Valve~ Bodies Bodies Form 2432,2432, March March 1974 1974
. I1.
Introduction Introduction . The Type 9200, The Type shown in figure 9200, shown figure ,\, is i;i heavy-dqty 1, butterfly . heaVy*d4ty butt'erfly ic ,-" valve body'designed)or stringent shutoff valve body'designed.for requireme~ts. An shutoff requirements. An elastomer or TFE elastomer TFE T-ring seat is"used to obtain seat is"*sed obtain shutoff. shutofi. TheThe . construction yariations of the Type '9200', a\iailable construction available 9200- are" are", : described below. The described The method'of T*.ring seal effecting the T-ring method' of effecting varies with the type of construction: varies with construction. . . .,: Specification Specification A-The A-The pressure-activated pressure-activated T-ring is. is con-... : ..~': ..~'. , tained tained inin tne body as shown in figure 22... Ex~er~~I. the body s*ealing .. :. i ;,:::,,~ l.:.:Fige External sTealing T Type 9200 Butterfly Contro'l F.iglJre 1. Control Valve Body pressure forces the T-ring against pressure 9~s~~,eriph.eiY* only:: against the disc-tperiphery, only0.0 ".,:,'.' ~ \':~ .. , .... :.'. ~~~ ,--,,;' when when thethe disc disc is closed. closed. There is no coritact contact'bet een the. betwe.eT) th.~ ,'. ::: ; ~. ;; . . .' ".".' ; ,- disc and T-ring when the disc is is opening opening or 'closing. or *closing. Installation".... ~- In~t~ilatior{' disc Specification Specification A A valves are available with elastomer elastomer T-rings T-rings only. bnly. ..~-- , ., Do not Do install the not install valve in systems where the the valve i"n systems where the Specification 8 Specification The adjustable B-i-The elastomer T-ring seat is adjustable elastomer service conditions exceed thosethose for which the contained between the body contained b0dyand and retaining flange as shown shown service conditions exceed for which the valve was designed, or damage to the valve and in figure 3. The adjusting in figure 3. The adiusting set screws and compression ring ling valve was designed, or damage to the valve and personal injury may personal injury result. may result. . force force the the T -ring against the' T-ring pi'!riphery to provide in-the disc periphery terference between between the T-ring and disc disc.. .
- 1. Inspect the
- 1. Inspect the valve valve forfor shipping damage and be certain shipping damage and be certain that the that the body cavity is body cavity free of is free of foreign materials.
foreign materials. Specification B-2-Similar to Specification Specification 8-1 except. B-1 except. pipelines to remove all foreign to remove ali foreign Clean out
- 2. Clean
- 2. adjoining pipelines out adjoining with TFE T-ring material that cculd damage that cculd the valve seat.
material damage the valve seat.
- 3. In
- 3. In those cases where those cases a flow direction arrow is attached where a flow direction arrow is attached that thethe flow through flow through Specification Specification C-i C-1--TheThe adjustable adjustable elastomer T'ring T-ring seat is to the to the valve body, install the body valve body, install the body soso that contained contained in the valve valve disc as shown in figure 4. The ad- jthe valve will be in the direction indicated. (Although some
~:the valve will be in the direction indicated. (Although some justing set screws and compression compression ring force the the T-ring materials and seat materials service conditions and service require flow in one conditions require
. seat flow in one against the body provide interference between the body bore to provide only, the Type 9200 is direction only. the Type 9200 is normally capable normally capable of flow in direction of flow in T-ring T-ring and body bore seating surface. either direction and either direction and will have no will have no flow attached.)
arrow attached.) flow arrow
. ,'; .-: ~; 4. Be certain that Be certain that the the pipeline flanges are pipeline flanges in line with each are in y:.:.- 4. line with each Specification Specification C-' except C-1 except other and that thethe disc is fully closed before inserting the disc is fully closed before inserting the Specification C-2-Similar to to Specification other and that valve valve into into the pipeline.
the pipeline. with with TFE T-ring
(si)
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'1-:-------- HANC. BOLTINC Figure2. Type 9200 Specification A ~.
Figure 2. Type 9200 Specifica.tion A .'
+
flOW SPECIFICATION C-7 TFE SPECIfICATION T.RINC C.l HE T*RINC SPECFICATION 9-1
+
FLew speCIFICATION ELASTOMCR T-R*NG8-1 SPECIFICATION C-I ELASTOMER T-RINC SPECIFIC ..T-RING ELASTOMEn TION C-, Figure 3. Type 9200 Specifications 8- 1 and 8-2 EUSTOMEA T.RINC Figure 3. Type 9200 Specifications 8-1 and 8-2 Figure 4. Type 9200 Specifications C-i and C-2 Figure 4. Type 9200 Specifications C*l and C-2 2 2
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~ft.c 20
.2-
- e. I'~ ./II OF
. Acfe or: q 9 When the disc is brought from its open position to its closed closed CAUTIO CAUTION position, position. there is a delay before seal pressure is applied. The sealing system is tripped just as the disc is entering entering the seal alignment or if the .disc If the flanges are out of alignment disc and allows the disc to close fully (completely in the seat) is open. installation and/or damage difficulties in installation open, difficulties damage :l before the seal pressure is applied. This operation operation is factory to the valve may occur. Be certain certain that flanges ~'t. adjusted on each valve;valve: if problems arise, arise. the system can be be and adjacent interfere with the adjacent piping will not interfere the ". ie-adjusted per the seal system instructions.
instructions. opening of the valve disc. ReviewReview the dimension dimension drawings to ensure that the inside diameters of On valves without power actuators,actuators. the sealing pressure pressure the adjacent flanges and piping are large enough enough must be released operated loading valve released with the manually operated rotation without interference. to allow disc rotation interference. before the valve re-applied after the valve is valve is opened and re*applied closed. Center th~
- 5. Center the valve between the pipe flanges. flanges. Although the valve may be installed in any position, position. the normal posi-posi-CAUTION tion is horizontal and the actuator ver-is with the valve shaft horizontal tical above the valve body. Never Never apply pressure to the sealingsealing system system unless the Valve valve disc is fully closed, closed. or damage
- 6. Follow accepted accepted piping practices when installing the to the T-ring T'ring may result.
valve. Provide suitable flange bolting bolting and flange gaskets.
- 7. If
- 7. actuator is furnished with the valve body, If a power actuator body. Specifications 8*1. B-1. B-2, B-2. C-1, C*1. and C-2 C.2 refer to the appropriate actuator instruction manual manual for infor*
infor- For Specification 8-1 and 8*2 For Specification B-2 valves, valves. the valve disc rotates rotates mation regarding installation and .operationoperation .of of the actuator. into into contact with the T'ringT-ring seat on closing. For Specmica-Specifica-
- tion tion C*l C-I and and C*2 C-2 valves.
valves, the valve disc rotates the T*ring T-ring into' into-If a sealing
- 8. If sealing system Specification A system is supplied for Specification A con- contact with the body bore seating surface on closing.
contact closing. No No structions, structions. refer to the seal system instructions instructions for operation operation sealing pressure is required. ,~: information. information . Maintenance
. Maintenance Specification Specification A Sealing Pressure Pressure Specification A Required sealing pressure for Specification Required A valves is equal to (a) 50 psig or (b) the valve inlet pressure plus one-half one*half the
'outlet
\ outlet pressure, pressure. whichever is greater. Maximum allowable allowable sealing pressure is equal to (a) the maximum allowable allowable To avoid personal injury and damage damage to tha the pressure oi of the sealing sealing system being used or (b) 2.5 times times process system, isolate the control process system. control valve from all the inlet pressure, pressure. whichever is lower. pressure and release release pressure from the valve body and actuator before disassembling.
disassembling. Operation Operation Outboard Roller Bearings' Outboard Bearings' If the valve is equipped equipped with outboard roller bearings,.bearings *. SpeCification A Specification lubricate lubricate the bearings bearings periodically periodically with a good quality roller roller power-actuated valves when the disc is in the fully On power*actuated bearing grease. grease. closed position, position. the seal pressure pressure is applied to to the back of the elastomer T-ring,T-ring. forcing the T*ring T-ring against the disc periphery. Packing periphery. Immediately Immediately upon activation ac:ivation of the actuator ac:uator to open the valve. valve, the seal seal pressure released, allowing the pressure is released. Key numbers used in this section Key section are shown shown in figure 5. 5. For disc disc to leave t!1ethe seat without any any force being exerted exened on the the ,', valves valves with with lubricating-type lubricating-type packing boxes,boxes. lubriate lubriCate the elastomer T-ring T-ring by the disc. The The disc is then positioned at at packing packing periodically. periodically. The frequency of lubrication requiredrequired th~ required the required angle of operation. operation. depends depends upon the severity severity of service conditions.
-3
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PURGING PURGING Q.RING O-RING U RICATIP*G LUSRICATlIIG Figure 5. Packing Figure Packing Box Types It may be necessary to tighten the packing packing follower follower nuts (key Replacing T-Ring Replacing
- 13) to stop leakage. If leakage cannot cannot be stopped in this this
-.. manner, replace the packing manner, replace. packing per the instructions instructions below. Specification Specification A
- ... : Key 6numbers used in the following steps are shown in figure Ke'/n'umbers packing, unscrew packing For split-ring packing, packing follower nuts (key 2 excep't\'Ihere indicated.
except where indicated. 131 and slide slide packing follower (key 15) away from the valve. valve. Remove old packing rings (key 16). 1. Making.certain that the valve disc (key 2) is fully closed. closed, remove rer:nove valve body from pipeline. pipeline. For lubricating packing packing boxes, boxes, remove actuator actuator mounting mounting, bracket. Remove lantern ring rihg (key 45) to gain access to the.. the." 2. Note the location
- 2. location of travel stopstop (key 9, 9, figure 6) on on packing rings behind behind the lantern ring. Place new rings over retaining ring (key 7) in respect respect to the body. This travel stOP stop
*" the valve shaft. When inserting the rings into the packing will be in either location A or B as shown in figure 2 and box, be box. be certain that the split in each ring is positioned 90° 900 must be replaced in the same location during reassembly. reassembly.
from the split in the adjacent adjacent ring. ring.
- 3. Unscrew Allen-head Allen-head cap screws (key 8) and remove remove For ring-type ring-type packing, remove the actuator actuator and all retaining retaining ring and T-eingT-ring (key 5).
51. accessories. Unscrew packing follower nuts (key 13). accessories_ 13), Remove packing follower and packing packing rings (ke'ls (keys 15 15 and and t(ey 51. 0-ring \key 6). If If G-ring O-ring requires replacement.
- 4. Inspect Coring replacement, 16). For lubricating packing boxes.
16). boxes, also remove lantern lantern ring remove it [rom from the body. (key 45) to gain (key gain access to the packing rings behind the the .... lantern ring. lantern ring. Install Install new new packing packing rings on on the the shaft shaft and insert 5. Clean
- 5. Clean T-ring T-ring and 0-ring grooves.
and a-ring grooves, andand coat the new new them into the packing box. T-ring with a good quality T*ring quality silicone grease. For O-ring For O-ring packing packing boxes. boxes, disassemble the components componenis of 6. Making Making certain that the T-ring seat
- 6. seat angle angle matches matches the
,. , :he control
;he control valve assembly assembly asas far far as as isis required to remove remove seat angle angle (as' (as'shown disc seat inset in figure 2),
shown in the inset 2), install the the the 0-ring follower (key the G-ring (key 491. 0-rings (keys 49). Replace O-rings 47 and (keys.47 and T-ring in the body. Insert the new Coring T-ring O-ring iiif replacement is
- 48) in the
- 48) the follower as required. required.
4
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. Type T_y_ 9200 _ _ _-..1.
p e_9_2_o;......O. __ __1 - Using care to avoid Specifications C-i and C-2
- 7. 7.Place retainingring Placeretaining ringonon1he 1hebody.
body. Using care to avoid Specifications C-t and C*2 the 0-ring (key 6). rotate the retaining ring slightly damaging the a-ring (key 61. rotate the retaining ring slightly damaging Key numbers used in the following steps are shown in figure and counterclockwise to ensure proper alignment Key numbers used in the following steps are shown in figure clockwise clockwise and counterclockwise to ensure proper alignment 4 except where indicated. stop is positioned in the 4 except where indicated. ononthe certainthe T-ring.BeBecertain theT-ring. thetravel travel stop is positiol}ed in the \ ' noted during disassembly. 1. Making certain that the valve disc (key 2) is fully closed, location
. location noted during disassembly. . \ ,. Making certain that the valve disc (key 2) is fully closed *
,,remove valve body from pipeline.
',remove valve body from pipeline.
cap screws (key 8), Replaceand
- 8. 8.Replace tightenAllen-head andtighten Allen-head cap screws (key 8).
- 2. Specification C-1 and C-2 valves may be furnished with
- 2. Specification C-, and C-2 valves may be furnished with section. a travel stop on the body. This travel stop, if furnished, is not Replacevalve 9.9.Replace pipelineper valveininpipeline perthethe"lnstallation" "Installation" sectioQ. a travel stop on the body. This travel stop. if furnished. is not
-removable.
*removable.
SpecificationsB-I Specifications 8 -1and 5-2 and S-2 3. Completely loosen adjusting set screws (key 54).
- 3. Completely loosen adjusting set screws (key 54).
steps are shown in figure
.Key numbersused Keynumbers usedininthethefollowing following steps are shown in figure 4. Unscrew Allen-head cap screws (key 8) and remove exceptwhere
- 3. 3except whereindicated.
indicated. 4. Ur.screw Allen-head cap screws (key 8) and remove retaining ring, compression ring, and T-ring (keys 7, 53, retaining ring. compression ring, and T-ring (keys 7. 53. and 5). and 5). (key 2) is fully closed, 1.1. Making certainthat Makingcertain thatthe valvedisc thevalve disc (key 2) is fully closed. remove valve body from pipeline. 5. Clean the T-ring groove. For elastomer T-rings, coat the remove valve body from pipeline. 5. Clean the T*ring groove. For elastomer T-rings. coat the new T-ring with a good quality silicone grease. new T-ring with a good quality silicone grease. stop (key 9, figure 6) on 2.2. NoteNotethe locationofoftravel thelocation travel stop (key 9. figure 6) on retaining ring (key 7) in respect to the body. This travel stop 6. Making certain that the T-ring seat angle matches the retaining ring {key 7) in respect to the body. This travel stop 6. Making certain that the T-ring Seat angle matches the as shown in figure 2 and body seat angle, install the T-ring in the disc. willbebeinineither will locationAAororB B as shown in figure 2 and eitherlocation body seat angle. install the T-ring in the disc. must be replaced in the same location during reassembly. must be replaced in the same location duri~g reassembly.
- 7. Place retaining ring on the disc and rotate the retaining
- 7. Place retaining ring on the disc and rotate the retaining Ikey 54). ring slightly clockwise and counterclockwise to ensure Completelyloosen 3.3. Completely adjustingset loosenadjusting setscrews screwS (key 54). ' ring' slightly Clockwise and counterclockwise to ensure proper alignment on the T-ring.
proper alignment on the T-ring. (key 8) and remove Allen-head cap UnscrewAllen-head 4.4. Unscrew capscrews screws (key 8) and remove 53), and T-ring (key 5). 8. Replace and tighten Allen-head cap screws (key 8). retainingring, retaining compressionring ring.compression ring(key (key 53). and T -ring \key 5). . 8. Replace and tighten Allen-head cap screws (key 8). Inspect, O*ring'(key 5.5. Inspect0O-ringý a-ringrequires {key6).6).IfIfO-ring replacerment, requires replacement. 9. Adjust the T-ring per instructions in the "Adjustments"
/ 9. Adjust the T-ring per instructions in the "Adjustments"
--- remove it from the remove it from the body. body. section.
section. elastomer T-rings, 10. Replace valve in pipeline per the "Installation" sec-T-ringand CleanT-ring 6.6. Clean andO-ring grooves.For a-ringgrooves. For elastomer T-rings. 10. Replace valve in pipeline per the "Installation" sec-coat the new T-ring with a good quality silicone grease. tion. coat the new T-ring with a good quality silicone grease. tion. seat angle matches the Replacing Valve Disc certainthat Makingcertain 7.7. Making thatthe theT-ring T-ring seat ansle matches "the Replacing Valve Disc disc seat angle (as shown in the inset on figure 21, install the If replacement of the valve disc is required, follow the disc seat angle (as shown in the inset on figure 2). install the If replacement of the valve disc is required. follow the new O-ring if replacement is "Replacirog T-Ring"* instructions to the point at which the T-ringininthe T-ring thebody. Insertthe body.Insert the new a-ring if replacement is "Replacing T-Ring" instructions to the point at which the required. retaining ring and T-ring have been removed. Then proceed required. retaining ring and T-ring hove been removed. Then proceed with the instructions below. Key numbers used in the follow-with the instructions below. Key numbers used in the follow-Using care to avoid ing steps are shown in figure 6. retainingring Place retaining 8.8. Place ring on onthethe body. body. Using care to avoid ing steps are 'shown in figure' 6. damaging O-ring (key 6). rotate the retaining ring slightly damaging O*ring (key 6). rotate the retaining ring slightly to ensure proper alignment 1. Remove actuator, mounting bracket, packing followers clockwiseand clockwise andcounterclockwise counterclockwise to ensure proper alignment 1. Remove actuator. mounting bracket. packing followers the travel stop is positioned in the (key 15) and packing. ononthe T-ring.Be8ecertain theT-ring. certain the travel stop is positioned in the Ikey 15) and packing. location noted during disassembly. location noted during disassembly.
- 2. If the ends of the taper pins (key 3) are peened. grind
- 2. If the ends of the ta per pins (key 3) are peened. grind cap screws (key 8). off the peened portion. Drive out taper pins.
9.9. Reptace Replace and tighten Allen-head andtighten Allen-head cap screws (key 8l. off the peened portion. Drive out taper pins. per instructions in the "Ad- 3. If there is one set of taper pins in the disc, pull shaft
- 10. Adjust the
- 10. Adjust the T-ring T-ring per instructions in the "Ad- 3. If there is one set of taper pins in the disc. pull shaft justments" section. (key 4) out of body and remove disc (key 2). Two sets of justrnents" section. (key 4) out of body and remove disc {key 2). Two sets of "aper pins indicate that-stub shafts are used. Each shaft por-
-taper pins indicate that'stub shafts are used.aztempt Each shaft por-to drive per the "r'stallation'" tion must be pulled out of the body; do not
- 11. Replace valve
- 11. Replace valve inin pipeline pipeline per the "Installation" tion must be pulled out of I'ne body; do not attempl to drive section. the shaft portions through the disc.
section. the shaft portions through the disc.
,_0 5
5
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- 4. Moving clockwise around the retaining ring (key 7,
- 4. Moving clockwise around the r~taining ring (key 7.
figure 3 or 4). tighten each set screw 114 turn. Continue ( CAUTION] figure 3 or 4), tighten each set screw 1/4 turn. Continue until the T-ring contacts its seat at one point. until theT-ring contacts its seat at one point. . disc, also install a new When installing aa new When installing new di::c. also install a new 5. When contact at one point has been made, return to shaft and taper pins. Attempting to use a new 5. When contact ai one point has been made. return to shaft and taper pins. Attempting to use a new the set screw selected as the siarting point. Move around disc and old disc and shaft will oldshaft require drilling new taper will require drilling new taper the ~et Screw selected as the starting point. Move around weakening the the retaining ring in a clockwise pattern, and wherever there holes in the shaft. thereby pin holes pin in the shaft, thereby weakening the the retaining ring in a clockwise pattern. and wherever there is clearance between the T-ring and its seat, tighten the set shaft. The weakened shaft may fail in service. A is cl~arance between the T-ring and its seat. tighten the sel shaft. The weakened shaft may fail in service. A with an old disc, using screw at that point 1/4 turn. Bypass any screws where the new shaft new may be shaft may be used used with an old disc. using screw at that point 1/4 turn. Bypass any scraws where the pin holes in the old disc as guides for T-ring is in contact with its seat. the'taper the- taper pin holes in the old disc as guides for T-ring is in contact with its seat. drilling taper pin holes in the shaft. drilling taper pin holes in the shaft.
- 6. When contact has been made at all points on the
- 6. Whim contact has been made at all points on the
- 19) installed, place valve T-ring, tighten each set screw on Specifications B-1 and C-1 4.4. With bushings (key inboard bushings With inboard (key 19) installed. place valve T-ring. tighten each set screw on Specifications 8-, and C-1 disc in the body. For large valves, block the body in the an additional 1/4 turn. No further tightening is required on disc in the body. For large valves. block the body in the an additional 1/4 turn_ No further tightening is required on clearance under the body specifications B-2 and C-2.
position. Be hOrizontalposition. horizontal certainthe Becertain the clearance under the body specifications 8-2 and C-2. at least one-half the disc diameter. With the disc equaltoto at least one-half the disc diameter. With the disc isi,;equal
- 7. Replace the valve in the pipeline per instructions given
-,"-.al. use a hoist of suitable capacity to place the disc in
.. ~.t;-;al. use a hoist of suitable capacity to place the disc in 7. Replace the valve in the pipeline per instructions given pin holes are on the actuator in the "Installation'" section.
thebody.
;he body. Be cerainthe Becerain the taper taper pin holes are on the actuator in the "Installation" section.
side of the side of the body. body. . box holes in
- 5. Alignthe
*5. Align thedisc shafthole discshaft thepacking withthe holewith packing box holes in Double-Thrust Double-ThrustBearingsBearings the body. It is unlikely that the thrust bearings will require adjustment.
the body. It is unlikely that the thrust bearings will require adjustment. If it does become necessary to adjust the bearings, proceed body and disc. Make cer- If it does become necessary to adjust the bearings, proceed Insert the 6.6. Insert through the shaftthrough the shaft the body and disc. Make cer- as follows. Key numbers used in the following steps are tain the key seat in the shaft is on the actuator side of the as follows. Key numbers used in the following steps are tain the key seat in the shaft is on the actuator side of the shown in figure 6. body. body. ..... . shown in figure 6.
- 1. Making certain the valve disc is in the closed position, and packing box parts (keys 1 ~ Making certain the valve disc is in the closed position *
., ' 7.7. Replace bushingretainers Replacebushing retainers and packing box pans (keys remove valve from pipeline.
' ., 17, 16, 15, and 13). remove valve from ~ipelli1e.
18.17.16.15. and 13). 2,. Loosen the screws found in each clamp-type collar (key should be centered in the 27);2 .. Loosen the screws found in each clamp-type collar (key taperpins. Installtaper 8.8. Install *Thedisc pins.The disc should be centered in the body bore. 27): body bore. .
- 3. With the valve disc closed, center the disc in the body per instructions in 3. With the valve disc closed. center the disc in the body T.ringand Re-installT-ring 9.9. Re-install retainingring andretaining ring per instructions in bore.
the "Replacing T-Ring'" section. For Specifications B-I, B-2. bore. the "Replacing T-Ring" section. For Speciiications B-l. B-2. C-1. a3'nd C-2, adjust the T-ring per instructions in the "Ad-C-l, alnd C-2. adjust the T-ring per instructions in the "Ad* 4. With the valve disc centered, position one clamp-type justments'" section. 4. With the valve disc centered. position one clamp-type justments" section. collar against each end of the bearing bracket (key 21) hub. collar against the Then, tighten each end of the bearing bracket (key 21) hub. screw in each collar. pipeline per instructions in the Then. tighten the screw in each collar. Installthe 1 O. Install
- 10. yalveininthe thevalve the pipeline per instructions in the "Installation' section.
"Installation" section. . 5. For Specifications B-I, B-2. C-I, and C-2 valves, adjust
- 5. For T-ring per Specifications the procedureB-'. B-2. Co,. and C-2 valves. adjust above if the adjustment was dis-T-ring inper turbed the procedure centering the disc.above if the adjustment was dis-turbed in centering the disc.
Adjustments Adjustments 6. Replace the valve in the pipeline per the "Installation"
- 6. Replace the valve in the pipeline per the "Installation" section.
Specifications B-1, B-2, C-1, and C-2 T-Ring section. Specifications 9-1. 8-2. C-', and C-2 T-Ring Adjust the T-ring as required to compensate for wear and to Adjust the T-ring as required to compensate for wear and to retain satisfactory shutoff capability. Actuator Linkage retain satisfactory shutoff capability. Actuator Linkags
- 1. Rotate valve disc to the fully closed position. Due to the large number of different types of actuators that
- 1. Rotate valve disc to the fully closed position. Due to the large number of diiferent types oi actuators that can be used with the Type 9200, it is not practical to present can be used detailed with the Type instructions for the9200. it is not practical to present various types. However, to
- 2. Loosen all adjusting set screws (key 54, figure 3 or 4)
- 2. loosen all adjusting set screws (key 54, figure 3 or 4) so that there is clearance between the T-ring and its seating simplify this adjustment and to ensure types.
detailed instructions for *the various However. to proper valve disc so that there is clearance between the T-ring and its seating closure, an internal travel stop is normally furnished valve simplify this adiustment and to ensure proper disc surface at all points around the T-ring. with the surface a t all points around the T-ring. closure. an internal tr2vel stop is normally furnished 'tIiith the valve. When checking or adjusting the linkage, the disc may valve. When checking or adiusting the linkage. the disc may be closed until contact is made with this travel stop. Adjust
- 3. Select one adjusting set screw (key 54) as a starting
- 3. Select one adjusting set screw (ke'! 54) as a starting r be closed until Contact is made with this travel stop. Adjust point and tighten that screw 1/4 turn (clockwise rotation). linkage to close the disc to this point.
point and tighten that screw Y4 turn (clock'.vise rotation). linkage to close the disc to this point. 6
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Figure6, Figure 6. Type 9200 3200 Ordering Replacement Ordering Replacement Parts Parts Parts Reference Reference Kay Key Part Part Name Name To order replacement parts,parts. specify the key number nod and . K,ey Kaey 23 Screw Hex Head Screw PattN.me Part Name name of each each part part required from the "Parts Reference" sec-
-Parts Reference" 27 Clamp-Type Clamp' Type Collar Collar 1 Beey Body 45 Lantern Ring (Lubricating lantern (Lubricating tion. Also state the original material of the part. known.
part, if known, 2 Oisc Valve Oisc ~nd and purging p~c~ing packing the desired quantity. valve type number, size. size, serial number. number, 33 Taper Taper Pin Pin boxes only) and all other pertinent nameplate information_ information. The correct 4 Valve Valve Shall Shalt 46 Fitting (O*ring (0-ring packing packing part will be selected based on this information. information. S' 5 " T-Ring T,Ring boxes only) 6' 6" O-Ring O,Ring (Specifications 47" 47' O-Ring t0.ring packing O-RinglO,ring A. B-1. and B-2 only) A_ B-1. boxes only) In all correspondence correspondence with the sales representative, representative. mention 7 Retaining Ring Relaining Ring 48' 48' 0-Ring 0- (0-ring packing Ring (O-ring packing the serial serial number of the valve. valve. 88 Allen-Head Allen-Head Cap Screw Screw boxes only) 9 Travel Stop Stop 49 O.Ring Follower (0-ring O*Ring Follcwer (O-ring 10 10 Set Screw Screw packing boxes only) packing
....:. :. I11' 11' K**
Ke.Y 50 Hex Head Bolt (O-ri.g 8011 (O*(ir.g
- "~" '. 13 13 Packing Follower Nut F,ckin9 NUl packing boxes only)
*:J:......
14 Packing Packing Follower Stud 51 51 Spacer Block Spacnr 15 Packing Follower PaCking Follower 52 Washer Washer is, 1S' Packing Pocxing Ring Ring 53 Compression Ring Compression Ring 17' 17' Pad~~nc~ Washer Packing (Specifications 8-1, B- " is 18 Retainer Bushing B-2, C:t, and B-2. CI. and C,2 C-2 only)- only)- IS 19 Inboard Bushing 54 Adjusting Set Screw Adiusting Screw 20 Bushing 6-1. B-2, Specirications B-I. Specificalions 6-2, 21 aearing Bracket Bracket C-I1.and C-l. and C-Z C-2 only) only} 22 Lock Washer lock
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'Recommended Spare Pari
, Recommended Spare Part
-- * .A '*CIJt.C CALCP'-32 PM - 37!:'
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. i Figure o. Figure 6. TypeT ype 92009200 Ord~ring Replacement Ordering ft2placemenl P~r13 P:r Parts ReferenceReference Kay Key P3r\ Nama Part Name Y*o 10 order replacement parts. specify the key number and replacement parts, (!;,\d , Key K.ey Part Name Part Name 23 23 Hex Head S~re.,., Screw name of each from the Referenca" sec- 27 27 Clamp-Type Collar Collar each part required :rom the""Parts Parts Refer:nca" 1 BodV Body 45 (lubric~ting Lantern Ring (Lubricating Lantern tion. ticn. Also state the original material oi known, oi the part, if known. 2 Valve Disc Valve Disc purging ~Jckir.':I olnd and pu,,.ing packing the desired quantity, valve desired quantity. valve type number, serial number, number. size, seriel number. 33' Tapcr Pin Taper boxes only) and all other pertinent pertinent nameplate information. The correct nameplate information. correct 44 Shaft Valve Shalt 46 fitling Fitting (O-(ing packing (0-ring packing 5' T-R:ng T-Rng boxes only) onlv) part will be selected based on this information. information. 5' 6' O-Ring (Specilications O-Ring (Specifications 47" 47" a* Ring (0-ring 0-Ring (O'ring poc'<infJ pocking A. 8-A. B-1, 1, and g. Qn~'I) 2 onty) 13-2 bo~es boxes only) In all In correspondence with the sales representative, aU correspondence representative. mention mention 7 Re taining Ring Retaining Ring 48' 48' O*iling pac~in;; 10'ring paching O-Ring (0-ring the serial number of the '1alve. valve. 8 B Allen*Head Cap Allen-Head C3;l 5c:!w Sc;ew bexes boxes only) 9 Tra~el Stop Travel 49 a*Ring Follower IC-ring O-Ring 10'ring 10 10 Set Screw Screw pac~ing boxes packing boxts only) onl,() 1 13 14 KPv Pk KAV PocKing Packing Follower Nut Packing follower Siud Follower Stud 50 so 51 51 Hex Head Bolt (O.rir.g Hex packing bo,es
!:polcor Block Spacar 10-ring onl'(1 boxes only) 15 Packing Follower Packing Follower ~2
- 5. Washer Washer 16' 16' PaCl<ing Packing RingRing .~
53
~w Ccmpr.ssion Ring Ccmpression Ring I17i '* P3clting Washer PackingWasher (Sp~cir.cJtions B-(Specifications 8*1:-
I-t.a Q8 Retainer Bushing Bushing B*2. C-1, B-2. C*l, and C*2 ani'll C-2 only) 19 Inboard 6ushing Bushing 54 Adj:Jsting Sel Screw Adjusting Set Screw 20 Bushing Buahing Spec!/ications B-1. B*!, Specifications 8-1, B-2. 21 eearing Bracket Bearing Bracket C'l, C-I, and C*2 C-2 onlv) only) 22 lock Washar LockWashar
'Recommended Spare Part
, Recommended Spa," 7
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( A Galveston-HoUston Galveston-Ho\)ston Company Company 1- I or Y Heavy-Duty Product Heavy-Duty Product Series: Series: Pneumatic Pneumatic Actuators Actuators (( C
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Galveston-Houston Company AA Galveston-Houston Company Headquarters Headquarters P.O. P.O. Box80x 508 508 Waller, Texas 77484 Waller, Texas 77484 Tel: 713/463-5100 Tel: 713/463-5100 Fax:713/463-5103 Fax: 713/463-5103 Tlx: 6868048 TIx: 6868048 ON-Bettis GH-BeHisActuators Actuators& Ii Controls ControlsLtd. Lid. Brunel Way BruneI Way Fareham, Hants Fareham, Hants P015 POlS 5SA, 5SA, ENGLAND ENGLAND Tel: Tel: 0489 885333 0489885333 Fax: 0489885200 Fax:0489 885200 Tlx:47493G TlIx: 47493G GH-Betti8, Ltd. ON-Bettis, Ltd. 5638 563888th 88thStreet, Street,BayBay#3 #3
- Edmonton, Edmonton,Alberta AlbertaT6E T6E 5R85R8 CANADA CANADA Tel:403/465-5251 Tel: 403/465-5251 Fax: 403/468-2112 Fax: 403/468-2112 Tlx: 0373573 Tix: 0373573 Compagnie Auxiliare Industrielle (CAI)
Compagnie AuxUiare Indu8trielle (CAl) 57, 59 Rue Etienne-Marcel 57, 59 Rue Etienne-Marcel 93100 Montreuil, France 93100 Montreuil, France Tel: Tel: 48 48575702 0241 41 Fax: 48 59 27 98 Fax: 48 59 27 98 TlIx: 230409 Tlx: 230409 Important: Due to GH-Bettis' continuing commitment to engineered (( Imponant: product Due to GH-Bettis' continuing commitment to engineered advancement, data presented herein is subject to change. product advancement, data presented herein is SUbject to change. Catalog Catalog#30.00-1A
#30.00-1A o1080 e 1989Gatve on-Houstor, Company, Galvea1on-Hou81on Company, All Allrights right'resered.
r""""'ed. GHB GHB69017/5M,4.89 890171511.114-89
CA/4 C - " -- :J
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lf4etl -2 6 T.Series T-Series Max. Max. Actuator Actuator Spring Spring Size __ Allowable Allowable Actuator Appr. Appx. WI.Wt. Size _ Actuator Spring Spring SIZB Size .,-..
,I ;-T Operating Operating If 1 Manual Manual Actuator Actuator Displ. per Displ. per Stroke Stroke SR5 ISR4 SR5 SR4 ISR3 SR3 I SR2 SR2 I S~ti II( SR1.l PressurB*'
Pressure- SR5 SR5 SR4 I SR3 I SR4 SH3 I SR2 SR2 IfSRil1 It SRl Override Override Model Model in3 I ft* in' ft Max. Operating Mar. Operating Pressure* Pressure* (psigj (psi~' (psigl (psigl) Appr. Appx. WI.Wt. of ofActuator Actuator {Ibsl (lbs)F - (Obs) (Ibs) T-310-SR (Ibs) T-3l0-SR Ijý6ý~'6 ~ ti3x132 T-312-SR T-JI2-SR 665 665 385
.385 150 150 155 155 165 165 175 175 200 200 225 225 423 423 418 418 412 412 512 512 580 580 T-316-SR T-J16-SR .1 066 i ___1 5,., ___' ......... .... 560 T-419-SR T-4l0-SR 661 661 383 383 290 290 315 315 315 315 315 315 - 325 325 378 378 373 473 473 542 542 533 533 100 100 T-412-SR I T-412.SR 5946 '.877 125 2Q5o ,135 13 135 '50 4 45357531 553 T-416-SR 1516
' T-416*SR 1516 .877
.877 125 125 135 135 135 13L 135 1__135 135 1 150 150 1457457 7 553 62162 612 621 6612
"- T-420-SSR T-420-SR FT-510-t T-510-SR SR 905 .524 -
2..399 j(1~~388 415 415 420 420 500 550 550 550
.4526.P14- 626; 6~~1<65 815 815 BOO 970 1 1170 800 1170 I
T-512-SR T*512*SR *1296 750 *,*,t 0:.. 4'0',.0 " ...."" . "'860-10*301"230, 875. T-516-SR T-516-SR 2080 2080 1.204 1204 175 180. 180 220 240 . 250 - 11033 033 11 016 016 1193 1193 1425 1425 T-520-SR 1 120 120 T-812-SR I T-B12-SR 11885 885 1091 1091 360 360 400 400 400 400 - 400 400 980 1163 1163 1135 11335 335 T-816-SR 3025 1.751
- 250 ......250'; *
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150 1 233 1419 1I39 1626 Maximum operating pressure is the pressure required to produce
- Maxin1um permanent deformation permanent deformation of the torque-producing mechanism of the the the maximum rated torque of the actuator. . actuator. Maximum pneumatic test pressure pressure is 1.25 limes times the max-max-Maximum allowable operating pressure
** Maxin1um pressure is the maximum maximum static imum allowable operating operating pressure when applied applied to both sides of pressure that may be applied to aa fully stroked pressure stroked actuator actuator against the the the cylinder simultaneously.
travel travel stops. stops. Pressures Pressures applied to only one end of the cylinder in in tt Except Except when maximum operating pressure is higher. excess excess of of the maximum allowable the maximum allowable operating operating pressure pressure may result result in Sizing Information Information The The following information is following information turer. Adjustments Adjustments are are usually charts in in accordance accordance with their designed to aid deSigned to aid in sizing in sizing BettisBettis made made relative relative to differential differential pres- guaranteed guaranteed minimum minimum break break or run run heavy-duty pneumatic heavy-duty pneumatic actuators actuators sure, extreme extreme temperatures, temperatures, un- un- ' output torque. (mid-stroke) output
- - to to specific specific valve valve requirements.
requirements. usual loadings usual loadings and and operating operating speed Bettis spring-return spring-return Scotch-yoke Scotch-yoke Bettis f: An An accurate accurate maximum maximum torque torque re- reo requirements. requirements. For accurate accurate torque torque actuators actuators may be selected selected usingusing L. quirement quirement must must be be obtained. obtained. Most Most requirements, requirements, all information information per- the published, the published, guaranteedguaranteed mini- mini-valve valve manufacturers manufacturers publish publish normal normal tinent to the the valve valve application, application, mum, endingending torque torque output output values values valve valve stemstem torque torque requirements requirements including including size, model, model, figure figure except when the except the maximum maximum require-and torque correction and torque correction factors factors for for number number and and nominal nominal pressure pressure rat- ment is at an intermediate ment intermediate positionposition unusual unusual applications applications or or extreme extreme ing, ing, must must be be furnished furnished to to the the valve valve of the piston of piston stroke. In these cases, cases, operating conditions. Normal stem operating conditions. Normal stem manufacturer. manufacturer. select an select an actuator actuator having having an an ending ending torque for a properly applied and torque for a properly applied and When When an an accurate accurate maximum maximum torque at least torque least 25.percent 25.percent greatergreater maintained valve is generally maintained valve is generally torque torque requirement requirement is is obtained, obtained, fur- fur- than the than the torque torque requirement requirement for for the the defined as the maximum torque defined as the maximum torque ther ther consideration consideration must must be be given given to to intermediate position. intermediate position. Note: Note: TheThe 25 25 required to rotate the valve element required to rotate the valve element the the valve valve type, type, designdesign and and applica-applica- percent adjustment percent adjustment isis not not to to bebe con-con-(ball, disc, plug, etc.) from its fully (ball. disc, plug, etc.) from its fully tion tion to to determine determine whether whether the the re-re- sidered aa "safety sidered "safety factor." factor." This This end-end* closed position when the element is closed position when the element is quirement quirement is is valid valid only only at at the the be-be- ing torque ing torque adjustment, adjustment, applied applied to to against the full valve-rated differen-against the full valve~rated differen- ginning ginning and/orand/or end end of of each each stroke stroke the spring-return, the spring-return, Scotch-yoke-type Scotch-yoke-type tial pressure. Because the features tial pressure. Because the features oror at at anan intermediate intermediate position. position. actuator, assures actuator, assures an an intermediate intermediate of each valve make and model are
*) of each valve make and model are GH-Bettis GH-Bettis double-acting double-acting Scotch- Scotch- position torque position torque outputoutput equalequal to to or or unique, torque correction factors unique, torque correction factors yoke yoke actuators actuators can can then then be be appro-appro- greater than greater than the the requirement.
requirement. (See (See must be provided by the manufac-mUst be provided by the manufac- priately priately selected selected from from torque torque output output page 7, page 7, fig. fig. 2.) 2.) 11 11
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T-816-SR T-812 T-816*SR-SR -- 133'h 1331h 1234/2 123'11 1324 1/2115¥. 132'11 42';";, 421/4, 15 15 30 30 16Y. 230'..PM/ 23'1',. 7'~. 8 2 , 4¥,. 4+"6 4 ~ U/, 25 W . ~ 14/,- ~ T-820-5R lOY.. 25'¥'1 14V" V., f-3, T-4,1-5, T-3, T-4, Spring-Return with M7 Hydraulic T-5, T-8 Spring-Return Hydraulic Override Override . RELIEF- ~ 0 - - - . . RELIEF VALVE VALVE
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MOUNTING MOUNTING PAD PADDETAIL DETAIL (A OF CYLINDER OFCVlINDEA Spring Size Spiing SIz8 Actuator Adualor SRI I 5)82 SRI SR2 TSR3 I SAl I5841 SR4 SR5 5)85 M Model Dimension A A B C C ID E E F f S G H J K L.L 1NPT) INPT) T-310-SR-M7 f.310*SR-M T-312-SR-M7 841A B4V. 754/ 75'10 7776' , 77V. 77Y. 71/4 8O~ 80%, 38'Y. JB'V1. 61/4,Y 1~ 12% 113 11 11 36%1. 36% 37% 37'l>1t 3Y'. 3\1~ 2%, 34 ~ V. 10'/, 3'Y" 3'Y, 1/
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AlldimenSIOns All dimensions are In in Inches. inches. I Accessory Mounting Mounting Pad Detail T-8 3,944-8E00 +-+- 3.944+/- 3.'442: 01D,A
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(4 HOLES) Certified Certified dimensional dimensional drawings drawings available available on request. Contact on request. Contact factory factory with with correct correct model model designation designation and serial number. and serial number. 19 19
FILE G ILBE RT/CO GILBE MM RT/COMMONWEALTH FILE TELEPHONE AND ONWEALTH -----
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TELEPHONE AND CONFERENCE MEMORANDUM CONFERENCE 4
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BY' 7 DATE-13Y TELEPHOZE C LL~ WORK ORDER WORK ORDER NO.__ NO.iJr-Pf>V()tJ.3 JPl,CONFERENCE D "
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& WEBSTER WEBSTER ENGINEERING ENGINEERING CORPORATION CORPORATION QA..LC 3 EXECUTIVE EXECUTIVE CAMPUS. CAMPUS. P. 0. O. BOX 5200 CHE~RY CHERRY HILL. NEW JERSEY JERSEY 08034 gJ*-F'tc PAe-,d-r- -F t::;:,..1IA..C +-\M.E'"..s-r ,
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or-1<6 DATE September 21 199 J. O. NO. QJ.o~O 242 P. O. NO. LTR NO. STP- 2030 VIA VIA REF. FPhiladelphia DEAR SIRS: SIRS:
'Philadelphia Electric Electric Company Company Attention: Mr. Mr. G. V. Cranston FOLLOWING ARE (3 THE FOLLOWING 0 0 SEPARATELY:
ATTACHED: DI SENT SEPARATELY: TO Manager 0off N Manager uc 1ear E Nuclear ngl.neen.ng D Engineering ep t . Dept. MICROFILM Document Control Center 61B-3 c/o Document 61B-3 _- COPIES _- PRINTS _- PRINTS REPRODUCIBLES _ - REPRoaUCIBLES APERTURE CARDS APERTURE CARaS EACH OF OF Chesterbrook Blvd. 965 Chesterbrook Blvd. _Wayne, PA 19087-5691
~ayne, 19087-5691 0 E- DRAWINGS aRAWINGS C3 0 SPECIFICATIONS SPECIFICATIONS I3
~ rn13 DOCUMENTS aOCUMENTS 0[3 NOTES OFOF CONFERENCE STATUS STATUS PLEASE NOTE PLEASE SENT FOR YOUR YOUR 0[] FINAL FINAL o APPROVED 0] APPROVED L 00LI REVISIONS REIiISIONS 00I OMISSIONS OMISSIONS 0
[] APPROVAL APPROVAL fl] [] COMMENT COMMENT PRELIMINARY F-0 PRELIMINARY o APPROVED AS REVISED ,A "ENEO APPROIIED AS REIiISED 'AS DEFINED SPECIFICATION
.- SPECIFICATION IN 0 OMN ADDITIONS ADDITIONS 0 CR TO CORRECTiONS CORRECTIONS 0 USE USE USE 0 INFORMATION INFORMATION INORMATION 0 LINO COMMENT NO COMMENT o UNACCEPTABLE 0I UNACCEPTABLE 0Q3 COMMENTS COMMENTS 0Q 0 0 FILES PILES 0C3 CONCURRENCE CONCURRENCE o NOTED SUGGESTIONS AS NOTED SUGGESTIONS 00 _. 0 YOUR ATTENTION IS DIRECTED TO THE FOLLOWING:
YOUR ATTENTION FOLLOWING: RELEASED FOR: 0I 0 FABRICATION [I 0 PURCHAse PURCHASE OF NECESSARY NECESSARY MATERIALS MATERIALS 0 0I PLEASE.REIiISE ANO SUBMIT PLEASE-REVISE AND SUBMIT _ _ _ _ PRINTS PRINTS -- _ _ _ REPROOUCIBLES REPRODUCIBLES _ _ - _ MICROFILM MICROFILM APERTURE APERTURE CARaS. CARDS. 0 PLEASE 13 PLEASE SUBMIT SUBMIT _- _ _ PRINTS PRINTS _ - _ _ REPRoaUCIBLES REPRODUCIBLES _ _ - _ MICROFILM APERTURE CAROS MICROFILM APERTURE CARDS OFOF LI DOCUMENTS o ODDCUMENTS DRAWINGS L LI DRAWINGS o SHOP SHOP DETAIL DETAIL O-1 0 PLEASE PLEASE RETURN RETURN ONE ONE COPY EACH OF THIS MATERIAL MATERIAL BEARING BEARING YOUR APPROVAL APPROIIAL OR COMMENTS. COMMENTS. C 0 PLEASE PLEASE ACKNOWLEDGE ACKNOWLEDGE RECEIPT OF THIS MATERIAL MATERIAL BY SIGNING ANO RETURNING THE ENCLOSED AND RETURNING copy OF THIS FORM. ENCLOSED COPY FORM. 00 wE TRUST WE TRUST THAT THAT THESE NOTES ARE THESE NOTES ACCORDANCE WITH ARE IN ACCORDANCE WITH YOUR YOUR UNDERSTANDING: UNDERSTANDING: IF NOT. PLEASE PLEASE ADVISE ADIiISE US. US. SHOULD ANY SHOULD REIiISION TO DOCUMENTS ANY REVISION DOCUMENTS OR DRAWINGS RETURNED HEREWITH INVOLVE RETURNED HEREWITH INVOLVE A PRICE INCREASE. THE SUPPLIER PRICE INCREASE. SUPPLIER MUST MUST NOTIFY STONE & NOTIFY STONE a IMPORTANT IMPORTANT WEBSTER PURCHASING DEPARTMENT WEBSTER PUR,cHASING DEPARTMENT WITHIN TEN (101 WITHIN TEN (\01 DAYS EllEN THOUGH A DEFINITE DAYS EVEN CANNOT BE OEFINITE ESTIMATE CANNOT GIVEN AT BE GIllEN AT THE OTHERWISE. THE THE TIME. OTHERWISE. THE PURCHASER WILL CONSIDER THE PURCHASER MADE WITHOUT REVISIONS MADE THE REVISIONS COST. WITHOUT COST. TASK NUMBER 9182128249 SGIG GENERIC ISSUES RESPONSE TO ITEM lA DRAFT RESPONSE IA SSFI ACTION ITEM NO. SFIP92-08, Rev. SSFI ACTION ITEM NO. SFIP92-08, Rev. 0 0 PEACH BOTTOM BOTTOM ATOMIC POWER STATION The Subject The Subject Draft response to Draft response Item la to Item la is is being delivered to being delivered to Mr.Mr. E. E. Epstein. Epstein. discussion with Per discussion Per with E. E. Epstein, Epstein, no revision to no revision Calculation PM-375 to Calculation PM-375 is is to to bebe performed performed at at thisthis time.time. Calculation Calculation PM-375 PM-375 will will be revised in be revised in the future to the future to incorporate this incorporate this item item (Item(Item la) and other la) and other SSFI SSFI open open items. items. If should have you should If you have any questions, please any questions, please call call the undersigned the undersigned at at (609) 482-3866. (609) 482-3866.
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1/ [1 ,1---.,.. M. K. K. Allen Senior Senior Task Task Manager Manager Copy to: GVCranston GVCranston FCook FCook EEpstein (orig. EEpstein (orig. enc) enc) JHufnagel JHufnagel 16-81 A029.5G
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~~E"" L. oF~ Page of SSFI ACTION ITEM J)!<Af r _
---- Action Item No.: SFIP92~8,SFIP92-08, Rev. 0 PART IIII - RESPONSE RESPONSE (Item 1a la only) 1.
- 1. The potential concern/question presented has been reviewed concern/question presented reviewed and the following response response is is provided:
The potential discrepancy addressed in Item 1a discrepancy addressed I a is that the Fisher Model95H Model 95H Pressure Control valve valve (PCV) with a 1 Inch inch orifice will allow increased flow through through the failed regulator regulator and subsequently subsequently lose the required nitrogen Inventory from the CAD tank for the combined limiting demand nitrogen Inventory demand of the the SGIG and the CAD systems for dual unit operation. A review of the piping arrangement of the PCV portion of the SGIG system (Refer. Dwg. M-372, . A Sh. 1)
- 1) shows that there there are 3/4 Inch Isolation isolation valves upstream upstream and downstream downstream of the PCV. These valves have an orifice size of 0.312 Inches orifice siz9 inches (Refer. NUPRO Catalog #N-390-3). #N-390-3).
evaluation (Attachment I)I)was made An evaluation made to determine determine the Impact on the required nitrogen inventory Inventory to sustain a failed PCV for a 4-hour 4-hour period using the PCV with a 1 Inch inch orifice. The evaluation evaluation determined that the isolation valves (in determined (In series) at the Inlet inlet and outlet of the PCV are the limiting limiting components of system flow in In the event of a failed PCV regulator. 1he ihe evaluation concludedconcluded that the calculated results on Section G on pages pages 22 and 23 of Calc. PM-375PM-375 are not affectedaffected by the useuse of Fisher of Model 95H Fisher Model valve with 95H valve with 11 inch inch orifice. orifice.
- 2. Additional documents/information documents/Information are providedprovided In in support of Item Item 1,1, above Qist}.
(list). Attachment Attachment II - Evaluation of Impact Impact on N2 N2 Inventory Using PCV With 1 Inch Orifice Orifice Drawing Drawing M-372, Sh. 1, 1, Rev. 44 Nupro Catalog No. N-390-3, April 1990. Nupro 3. 3.' Item reviewed for for hardware hardware nonconformance nonconformance requiring requiring Implementation implementation of NGAP~3N001, NGAP-03N001, Control Control of Hardware nonconformances. nonconformances. NCR issued: () NCR Issued: ( ) Yes, (X)(X)No. NCR No. (not applicable) Approval Approval Signature/Date. SignatureJDate . ACfOn.MC
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DR-Afr SSA ACTION ITEM Action Item No.: SFIP92-08, Action Item No.: SFIP92-08, Rev. Rev. 0 PART IIII - RESPONSE RESPONSE (Item 1a la only)
- 1. potential concern/question The potential presented has been reviewed and the following response is concern/question presented provided:
The potential discrepancy discrepancy addressed in Item Item 1a is that the Fisher Model 95H Pressure Control valve (PCV) with a 1 inch orifice will allow (PC'V) increased flow through the failed regulator and subsequently allow increased nitrogen inventory from the CAD tank for the combined lose the required nitrogen combined limiting demand of the SGIG and the CAD systems for dual unit operation. operation: arrangement of the PCV portion of the SGIG system (Refer. Dwg. M-372, A review of the piping arrangement M-372. . downstream of the PCV. These Sh. 1) shows that there are 3/4 inch Isolation valves upstream and downstream have an orifice size of 0.312 Inches valves have #N-390-3). Inches (Refer. NUPRO Catalog #N-390-3). determine the impact evaluation (Attachment I)I) was made to determine An evaluation Inventory impact on the required nitrogen inventory 4-hour period using the PCV with aa 1 Inch orifice. The evaluation to sustain a failed PCV for a 4-hour evaluation isolation valves (in series) at the Inlet and outlet of the PCV are the limiting determined that the Isolation determined limiting components of system flow in the event of a failed PCV regulator. lhe components evaluation concluded The evaluation concluded that the calculated results on Section Section GG on pages 22 and 23 of Calc. affected by the use Caic. PM-375 are not affected valve with 1 Inch orifice. of Fisher Model 95H valve
- 2. Additional documents/Information Additional documents/information are provided in supportsupport of Item 1, above above (list).
Qist). Impact on N, Attachment I - Evaluation of Impact Nz Inventory Using PCV With 1 Inch Orifice Orifice M-372, Sh. 1. Drawing M.372. 1, Rev. 44 N-390-3, April 1990. Nupro Catalog No. N-390-3.
- 3. Item reviewed for hardware nonconformance requiring hardware nonconformance requiring imp/ementation NGAP-03N001, Control implementation of NGAP-03N001, of Hardware nonconformances. NCR issued: (( )) Yes, (X)
Hardware nonconformances. (X) No. NCR No. (not applicable) Signature/Date Approval Signature/Date Approval naC10mC
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STONE &WEBSTER STONE e. WEBSTER ENGINEERING ENGINEERING CORPORATION CORPORATION C 6L(- ýpv::ý,-1:5' CALCULATION CALCULATION SHEET SHEET
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CALCULATION CALCULATION IDENTIFICATION IDENTIFICATION NUMBER NUMBER ( J.O. OR J.O. OR w.O. W.O. NO. NO. DIVISION & DIVISION f, GROUP GROUP I CAgy ITON OPTIONAL TASK
. lOPTIONAL TASK CODE CODE PAGE,~
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STONE a. WEBSTER ENGINEERING a WEBSTER ENGINEERING CORPORATION CORPORATION CALCULATION SHEET CALCULATION SHEET
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I--5MP..c(_. 0ýr*m.. TP4LE0 CI, / -C,,,, PQ/m0oVFCE .Ulsr)E THE fLow* nl-R00Grr \HE: fC-VFbfZT1ON. UNCq-4At 0\ ~. ~'/~ Ew PT..(fOS'c~F .UtJPE\e.. A m-ILED pcV CONl)11l0N REM~INS UNCA-tANQ:-o P-r'T.IS'O.SCFM 25 25 26 26 IN\IFIIOPCy T ALJ EO P _*.k.V .........Ph. OA AL"l14o~.l}\E. UIY\\T\~G CoMFONENTS Af2E"THt\SOLA-I10N .... . VAL\}E?£ ~t-.l~IES) ~ .. TH-A-N PGv'.O~IF.lce 27
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29 29 30 30 CoI~acatr~..L>f}~ CALCU~ RbSULTS ON ?Abe) 22.. ~.~ 3I 31 32 32 0F OLe. OF CNc -A PM --?7G, ~ 75 ME ARE t-.bT N 1'OT Arff:Gl"E.'O* o,7En P-"/. BY. Th4e ll-l-E" USe- U*-- OF AS~ ~T012- MODEL 'lS\-I \'A'Th 95pel 9tUTO$?-fz M~ODE qsw '-Arm* ," I" oRIFtcl-. oRIl=t CE"o 33 33 34 34 35 35 36 36 37 37 38 38 39 39 40 40 41 ( \ 42 42 43 43 44 44 45 45 46 46
N 390-3 'V~C
~~
II ..... *
~"U;'
l "U"sERiES SERIES N*390*3 April,1990 April, 1990 lIt/. i BELLOWS SEALED BELLOWS SEALED VALVES VALVES 1~~-11I~4 Ib~
/ I -2.~~J1 '-
( .., N j i (
-E A SWAGELOKI SWAGELOKP COMPANY NUPRO Company NUPRO COMPANY Company 4800 E. 345th Street 4800 Willoughby, Ohio 44094
<Jl990s..g,,,*Co.d~hts_
(l.~.c f?~~.C *T7r*4-CM0X I~ FEATURES I BENEFITS FEATURES/BENEFITS "12U" SERIES The NUPR~ 7M NUPROO "U" "U" Series Series Bellows Valve Valve pro-safety, reliability and vides safety, and versatility in the most difficult applications. The "U" Series sec-ondary containment system system prevents prevents leakage leakage to atmosphere to atmosphere in the event of of a bellows failure. Pressures to Pressures to 2500 Temperatures to 2500 PSIPSI (17,200 to 12000F (17200 kPa) 12000F (649°C) (6490C) kPa)
.."4I//B/
4/6/8U" 1" SERIES S HERIES 6
*a steel construction 316 stainless steel
- SFlow coefficients (Cv)
Flow coefficients (Cv) from from 0.36 0.36 to to 5.3 5.3 v Hardened
*i SWAGELOK'"
** Tube
** Tube SWAGELOKO Tube Filling and 6mm and 6mm to 12mm Tube socket 12mm socket weld Tube bull butt weld weld ends:
weld ends: Fitting ends: 1/4" ends: 1/4" ends: 3/S" 1/4" to 3/8" to to 3/4" to 1" 1" 3/4" 1/2" 114" to 1/2" 1/2--.--for stainless steel actuator strength and wear resistance Upper packing provides Bi secondary containment in the event I
*I Tube extensions: 1/4" 1/4" to to I" 1" 0.0.
O.D. x 3" long ron ng of a bellows failure
*- CAJON'"
CAJON Male VCR Metal Gasket Face Male VCR'" Face Seal Seal Fitting ends: 1/4" Filling 1/4" and 1/2" 1/2" Acme power transmission threads Acme threads for longer cycle lite for life and ---+-i1~
** CAJON\!)
CAJON Male Male VCQ VCCO O-Ring Face Seal lower operating lower operating lorque torque Fitting ends: 1/4" and 1/2" Fitting 1/2"
-I
** Choice Choice otof Stellite Stellite or Kel-F Kel-F stem insert Union bonnet construction for safety materials materials
** Regulating Regulating style style insert available for "4U" "4U Actuator backstop increases Series. *'*'*Ball bellows cycleand life
** Air Air actuators available actuators available
** Bonnet Bonnet tube available tube extensions available double pin design
*a 100%
100% helium helium leak tested leak tested provides positive stem retraction Conventional bellows in beeilows in "4/6/8U" - system pressure "4/6/SU" ppressure Choice of welded acts on inside of bellows "~~~"-----~; of welded
~ *'G or gasketed or gasketed body-to-bonnet*
body-to-bonnet . seal for versatility Inverted bellows bellows
~===--In in "12U" -
"12U" system pressure
((I bottom mounting acts on outside of bellows bellows S ity in "4/6/8U" Non-rotating Non-rotating stem stem tip for increased shut-off cycle life life 0 K Side or panel mounting capability in "12U" "12U" MODEL FEATURES "UW" Series "UG" Series "UG" Series AII-wekled, hermetically sealed for tempera- "UK" Series "UK" Series Metal-to-metal Mera/-to-metal shut-off shut-off for temperatures to for temperatures to Leak-tight shut-off in vacuum, cryogenic, cryogenic, or tures to 1200OF (6490C) 6S0 o F (343°C) 650OF (3430C) pressurized pressurized systems to 200°F 200OF (93°C) (930C) LOWER lOWER BODY-TO-BELLOWS BODY*TO*BELLOWS LOWER SECONDARY SEAL BOOYTO*BELLOWS LOWER BOOY-TO*BEllOWS SECONDARY SEAL SUBASSEMBLY SUBASSEMBLY SEAL SEAL SECONDARY SEAL SUBASSEMBLY SEAL 316 STAINLESS SECONDARY SEAL SUBASSEMBLY SEAL 316 STAINLESS STEELSTEEL ALL ALL WELDED WELDED l16 STAINLESS STEEL SILVER PLATED O.RING 316 STAINLESS STEEL TFE COATED O*RING CONSTRUCTION CONSTRUCTION O*RING 316 STAINLESS STEEL a*RING STEEL O*RING K, f* Stellite SreUire stem packing packing
*, Welded METAL MEIAL STEM stem insert insert and Welded body-to-bonnet SlEM TIP body-la-bonnet seal containment containment of of system TIP Grafoil secondary and Gratoil seal for system fluid fluid secondary far absolute absolute
- Stellite Slellite stem packing packing
*" Gasketed METAL stem insert STEM body-to-bonnet seal Gasketed bOdy-tO-bonnet field maintenance maintenance
*" Replaceable Replaceable bellows subassemblies subassemblies bellows and TIP insert and Grafoil Grafoi! secondary secondary sea! for tor easy and insert/adapter insert/adapter IIEl-F STEM YKEL-F
- KeI-F packing packing
"* Gasketed STEM INSERT Ke/-F stem INSERT FOR stem insert fOR SOFT Gasketed body-to-bonnet easy field easy SOFT SEAT insert and TFE field maintenance
"* Replaceable maintenance .
Replaceable bellows bellows and subassemblies '" .. subassemblies SEAT SHUT-OFF SHUT'OFF TFE secondary metal seal body-to-bonnet metal seal for and insert/adapter insert/ adapter 0 22
1LEF'ET(, C -
~~tv1~'-1*
ICAL DATA.,. ~1 oy TEMPERATURE GRADIENT GRADIENT 0 0 0 600 F(315 C) 135 F(57*C) 3 9000F (4820C) 140F (60-C) K 4u1 0.11 in. 0 0.36 0.36 (1.8 cm 3) 12000F (649"C) 150 F (660C) 6U-MM 200°F 3 6U "UK" 200°F "UK" in.3 0.25 in. 0.2S lOU-MM 1.00 (930C) (93°C) (4.0 cm3) (4.0cm 3) WORKING WORKING PRESSURE PRESSURE IN PSIG PSlG 8U 650OF 2500 PSI "UG" 6S0°F "UG" (343-C) in.333 0.27 in. 12U-MM 1.2 1.2 (17,200 kPa) (17.200 (343°C) (4.4 cm 3)) (4.4cm "UW",2oooF
"*UW" 1200"F 1.46 in. 3 12U 3.1 (6490C)
(649°C) (23.9cm 3 ), TEMPERATURE i tritirmVi uIt @ a in.33 1.22 in. PRESSURE PRESSURE (PSIG)*(PSIG)o 12UA* 12UA" 5.3 S.3 (20.0 cm 33 )) (20.0cm L L ___________ - 100 0 F(38°C) 100°F (380C) 2500 2500 2500 2500
*. N,,_
"A7designates designates angle angle paUern pattern valve.
vaWe. 200°F (93°C) (930C) 2500 2500 2500 300°F (149-C) 2500 300-F (149°C) 2500 2500 4000 F(204°C) 400°F (2040 C) 2500 2500 2500 500°F (2600C) 2500 500OF (260°C) 2500 COEFFICIENT vs. TURNS FLOW COEFFICIENT TURNS OPEN 6000 F(315°C) 600°F (315 0 C) 2500 2500 2*1;2 ...-_--.-.-----,.---~-----_.,_..._-____, 650°F 650-F (343°C) (3430C) 2500 2500 700°F 700-F (371°C) (371C) 2120 2*1/4 +---I--+I------I--------,~---__l 0 750°F 750 F (399°C) (3990C) 1740 1740
- 20OF (- 280C) to' SOooF 800OF (427°C)
(427-C) 1360 850°F 850-F (454°C) (454oC) 980 980 0 1*314 90QoF 900 F (482°C) (48200) 600
<J) 950°F 950-F (510°C)
(5100C) 540 540 Z
~ 1-112 1000°F OOO°F (538°C)
(538-C) 480 480 U-- 10SooF (565°C) 1050OF (56500) 425
~ 1-114 0: 1100 1100F 0 F (5930C)
(593°C) 360 ex: w cz 1150°F 1150-F (621°C) (621-C) 300 co 1 0
- 1200°F 1200OF (649(649°C) C) 250
- l Z 0 Z 314 1500 1500°F F (815°C)
(8150C) 50 1Todetermine kPa. multiply
*To multiply PSIG PSIG by 6.89. To Todelermine determine Bar. multiply multiply PSIG P51G by by 112 information
.0689. For complete informal ion on ANSI Class Class ratings, refer to Technical Bulletin refer 10 Buffelin
((3~ No. 4. NO.4. 1'4 0 .5 234 6 FLOW COEFFICIENT COEFFICIENT (Cv) FLOW CURVES FLOWCUAVES Air Air Water 100 100 100 80 s0 80 60 60 60 40 40 40
<J) 20 CL e, e, 20 2-0.
Q. 0-0 0 0 cc 0:: cc 0:: 0 10 0 10 w cc w S 0:: 8 c:: 8
~ *n
- l cc Vl 6 --------- II>
II> 6 Vl
--.--- 6 w
Q_ W 0:: I>. c: Q_ I>. 22 4 66 8 10 10 20 40 40 eo 60 80100 100 200 400 600 .2 .4 .6.8
.6 :'.0
.8 1.0 22 4 66 8B 10 ID 20 40 60 AIR FLOW (SCFM)
(SCFM) @ @ 7070'FF (21 (21'C)
'C) (DtSCH*ARGE (DISCHARGE TO TO ATMOSPHERE)
ATMOSPHERE! WATER FLOW (GPM)@ WATER (GPM) rd 70oF70'F (21'C) (21°C) K. 33
PAGE- Y. ~
~,C ,b.-~tzNI I 018 \.qDt=1B ,
.,XI MATERIALS OF CONSTRUCTION MATERIALS CONSTRUCTION "12U" 0 iB "4/6/8U" "4/6/8U" 2 Kýý 2 2 Bt'fft 1A 0
, .. 1A IPA bet bcrew I i/ri* N A" zee" uina. .-
( 15 Cap Nut Handle AluminumlB2111 I 18-8SSICommercial 0 3 D4 3 G
..=ts 2
3 4 Gland Nut Gland 316SS/A2763 316SSIA276 []4 U35 a 4 s 5 6 Packing UK Spacer TFEJMIL.P.19468A, (3) / UGraloillCommercials 316SSIA276 R3-e6 1 6
~7 9
7 Jam Nut 316SS/A2763 CCil6 6 Q 400 a Panel Mounting Nut 316SS/A276 ~7 1i?"aS8 9 Bonnet Nut 10 Bonnet 11 Lower Seal 0-Ring 12 Actuator 13 Pin (2) 316SM/A2760 316SSIA2768 316SS/A5804 440CSS/A2764.7
<7.18 lJ9 Ll 416SSICommercial 14 Ball Bearing 440CSS/Commercial 15 Stem Extension 440CSSTA276 -
10 16 Stem 17 Bellows 347SS/A269" 316SS/A276 316SS/A240 110 10 QI 18 Weld Ring 316SS/A276 19 Adapter 316SSIA276 20AInsert UG/UW Stellite #6/Commercial 208[nsert UK Kel-F 6060/AMS-3650A 21 O-Ring UK UG 316SS/A5808 316SS/A5800 Oil ( 22 Body Wetted Wetted parts numbered numbered in red.
,316SS/A276 a
LUBRICANTS LUBRICANTS 1 Green anodized 2 Green paint
~3 Molybdenum Molybdenum disulfide dry film disulfide dry film
*4 Silicone base lube Silicone base lube 12 Molybdenum disulfide 55 Molybdenum base paste disulfide base paste 12 66 Silver plated 77 Molybdenum Molybdenum disulfide base dry disulfide base dry film film and paste and paste 8
6 TFE coated TFE coated 13-13- -13
- 13 113ý 13 ..... I 1-13
.....13 14 Gl14
~:~D- 18 t_~19 Welded' 17 Subassemblies 18 .
19-20A' (;) 20B
'Q G 21 '
. . -19 lB 208 K !'JU~RD 22 NUI=>~c:J
.0=>
22 a 4
PA~~eJibA
~,c.
9-Eiý* C /rC'1~: DIMENSIONS DIMENSIONS c.F 5N N 2-010.32 TAPPED HL 114' DEEP Bottom View Bottom View "4/6/8U" SERIES SERIES 0.281 7.1 61h SS-6UW (port) (port) 3/8 SWAGELOK 6% 11/ 3T/ Vh 1% ,,/1, S-U-SS-UTW
-WTW (port) 0.281 (port) 7.1 (port) 7.1 (port) 3/8 M 12 3/8 1/2 TSWAEO TSWT TW 61h6%lkV 6% 6/a, 1'/= - l'h 11%1%/ -
WA/ %
%/ 2`
2'/, SS-8UW 0.312 7.9 1/2 SWAGELOK 6% 68/a 1'/, V 3' '1 1'/= / - - - 1/2 TSW SS-SUW-TW 0.312' 7.9 3/4 MTW 6% 6% il - 1/, 17s 2/ SS-6UW-MM 0.172 4.4 6mm SWAGELOK 672 5Wa 1 2'h 1 1 , - - - SS-10UW-MM 0.281 7.1 I0mmSWAGELOK 6`h 6h 1/ 3/ 11/ 1 (port) (port) 1 SS-12UW-MM 0.312 7.9 12mm SWAGELOK 6% 6/ 1%/, 1 % 1%/, - - - Afldimensions All dimensiOns are are in In inches (except where mm is indicaled) inc:hes (""cep! indicated) -lor
- for reference subject to change relerence only, subjecllo change..
DimensiOns shown with
- Dimensions nuts finger-lighl.
SWAGELOK nuls wilh SWAGELOK finger-tigrtt. 1-----4"----* ( ,5 "12U" SERIES "12U" SERIES r----;."~===+.._-r-r_ z.ý PANELOR PANEL OR BRACKET MOUNTING BRACKET MOUNTING PANEL MOUNTING 1,2" MAX.THICKNESS 1,2" MAX. THICKNESS USE USE 1*31-3 16" 16" DIA. OIA.HO~f HOLE liZ" MAX. THICKNESS USE 1*3116" DIA. HOLE.,
~1~6~~U~;:~~---+I-7-1--d' SlOE MOUNTING - 2 1 OHRU DRILL HOLES I 1.\,.* 17.6'" THRU HOLES-'-
LOCATED AS SHo,vN I ' LOCAT(O AS SHOWN 3*3;;6'" IN*r DIA.
;TYP' L I ,
ORDERING ORDERING INFORMATION INFORMATION ~'------'. 17
!i;464"-
H
..... :"'1,."
;12 A Numbers shown above All Ordering Numbers above specify specify aa "UW""UW" 2--.16-
---2*7'16"-- .-! \.21"6 4 "' -
Series valve. To orderorder aa "UK" "UK" or UG" Series valve, or""UG" valve. --2*:r-1 2"- replace the UW in in the valve Ordering Number with UK or Ordering Number "12U" "12U" Examples: SS-4UK UG. Examples: UG. SS-4UK SS-12UG-TW "12UA" TESTING CLEANING CLEANING & & PACKAGING PACKAGING All "U" "U" Series Bellows Sealed Valves are helium leak Series Bellows All All valves with VCR valves with VCR Special Special CleaninQ Packaging Cleaning and Packaging tested to a rate of 44 x 10. 10-99 standard c.c.1 sec. at the seat. standard c.c./sec. seat, envelope and all seals, seals. and veoVCO ends ends to NUPRO SpeCification NC-i 1. Specification NC*l1. envelope All other valves Standard Cleaning and Packaging Standard Packaging to NUPRO Specification NC*l0 Specification Oplion~1 S~ecial NC-IO. Optional Special Cleaning Cleaning and Packaging to NUPRO SpeCIfication Specification NC-1!. NC-11.
. VALVE VALvE OPTIONS OPTIONS A~rIP'vWrAS I Welded lUbe Tube Extensions Extensions
-'ill ~ C~ 1">.Ge:"~f" ill I
~ NUP~O0 rill ~
- *a Factory Factory weldedwelded toto Bonnet Bonnet Port Tubes Tubes -TW style ended valves
*TW valves r..Jup t~
- S Socket Socket weldedwelded or butt butt welded f i c===')
TUBE '_ _ -- ---.J
~ TUBE e)lJ ION)It1 1" *.3 (optional 3 inches long lengths up to 12 inches)
TUBE UBE T-- SOCKET WELD BODY BOOV BUTT t 1"r--.-4. (optional lengths up to 12 inches) WELD WELD ( *a 316 stainles5.$teel stainless4teel WelD WELD ordera valve with welded tube extensions, To order replace -TW extensions, replace *TW in in the valve OrderingNumber Ordering Number with the desired designatorlisted below. desireddeSignator below. PARTIAL SECTION PARTIAL SECTION
- PARTIAL Examples: SS-4UK-TH3 SS-6UG-TP3 Examples: SS-4UK*TH3 SS*6UO*TP3 ONE 14" ONE TUBE 1,4" TUBE ~~,"ITWO TWO 114" TUBE*
1/4" TUBE EXTENSION EXTENSION WELDED EXTENSIONS WELDED EXTENSIONS WELDED THE BONNET (T"I) TO THE CTll TO THE BONNET (T21 (T23 Monitor Monitor bellows integrity* integrity - Vacuum Vacuum insulate insulate bonnet bonnet area* area* Provide Provide heating heating or cooling coolingjacket *a Pressurize Pressurize bonnet bonnet area to increase effective increase effective 114' O.0. x .049' wall -4U-TW -TH3 -- pressurerating pressure rating(see (see note below) -4U-TW - TN3 318* 0.O0.x .065' wall -6U-TW -TN3 -
** Available Available with either either one or two bonnet bonnet port tubes tubes
** 316 stainless steel tube port tube is 1/4" 1/4" 0.0.
O.D. x 1" 1" long long .6U-TW -- TP3
** "4/6/8U" "4,168U" tubes are are welded to bonnet; "12U" "12U" tubes are threaded threaded toto 1/2' 0.D.x .065' wall -8U-TW -TP3 -
bonnet -8U-TW --- TV3 To orderordera valve with with bonnet port porttubes, tubes, use T1 TI for one tube, tube, oror T2 for for two 3/4' 0.0. x .083" wall -12U-TW -3 --R tubes, as tubes, as a suffix to the valve Ordering OrderingNumber Number. Examples: SS*4UG*T1 Examples: SS-4UG-T1 SS*12UG*TWT2 SS-12UG-TWT2 Wel .d. x .065 wall a *c
-12U- -S -itR3 NOTE:
NOTE: When When pressurizing above the bellows bellows through the bonnet Welded CAJON VCRP and VCOý Face Seal Fittings port(s), be sure the system or bellows external bellows pressure the external pressure belore bellows internal pressure is greater before operating the valve. The maximum greater than maximum Welded CAJON VCR and veo Face Seal Fittings pressure rating above the bellows bellows is 1000 PSi kPa~ You may PSI (6800 kPa). ** Factory Factory welded to increase increase the bellows bellows internal or system system pressure pressure by 60%60 cIi! 01 of the pres-pres* -TW style ended valves
*TW sure supplied above above the bellows. This proportional proportional factor is necessary ** Socket Socket weldedwelded NUI=OFQQ because because of force distribution distribution and areas within the valve. or butt welded welded
** VCR or VCO gland, High Temperature Model and and female nut nut On '.'UW"'"UW"Series valVes valves only - for temperature temperatureapplications applicationsabove 900OF 900°F (4820C)
(482°C) ** 316 stainless stainless steel
- Special high*temperature high-temperature lubricant prevents seizing of actuator actuator veo To order a valve with VCR or VCO Fittings. Fittings,replace the*TWthe -1W in the threads threads valve Ordering Ordering Number with with the the desired designatorlisted below.
desired designator below
" Extends temperature
- Extends temperature rating to 1500°F 1500-F at 50 PSI (8160C (816°C at 340 kPa) Examples: SS-4UK*V51 Examples: SS-4UK-V51 SS-8UG*V19 SS-8UG-V19 self*lubricating fluids such as liquid metal
( with self-lubricating order a high temperature oJi order temperaturemodel "UW" Series valve, insert insert HT into the valve Ordering OrderingNumber Number. Examples: SS*8UWHT40 Examples: SS-8UWHT40 SS*12UW*TWHT SS-12UW-TWHT 1/4' Female CAJON VCR -4U-TW -V13
-61.1W -V16 TFE SecondarySecondary Packing Material. Material. 1/2' Female CAJON VCR
-8U-TW -V19 On "UG" and "UW" "UW" Series Series valves only - for temperatures temperaturesfrom cryogenic 1/4' Female CAJON VCO -4U-IW -V52 cryogenic to 400°F 4000F(204"C)
(2040C) 8U-TW NV58 Replaces the Grafoil Gratoil secondary secondary packing packing 1/2" Female CAJON VC0 U mdn-- d-V53 To order ordera "ua" "UG" or "UW" "UW" SeriesSeries valve with TFE TFE secondary packing, secondary packing, uses mnodified body and gland for shortest inlet-o-outlet dimension. insert*TF insert .TF after after the valve series designatorin series designator in the the valve Ordering OrderingNumber. Number Uses modified body and gland 'or shortesl inlel-lo-QUIIeI dimension. Examples: SS-4UG-TF SS*4UG*TF SS*8UW*TF4C SS-8UW-TF4C Regulating Regulating Style Insert Insert
~-<;~
~'- On "4LIG" "4UG" and "4UW" '4UW" Series only - for greater greater
~
controlwith 10° flow control 10' tapered taperedstem insert insert
.".. . 316 stainless stainless steel steel matenal material SAFE VALVE SELECTION . _ orderaa valve with a regulating To order regulatingstyle insert, insert,
'- insert insert an R into the the valve Ordering OrderingNumber.
Number. When selecting selecting a valve. valve, the total system system design must be considered considered Examples: SS-4URG SS-4URW-TW Examples: SS-4URa SS-4URW*7W to ensure safe, trouble-free trouble-free performance. Valve function, material compatibility, adequate compatibility. adequate ratings, ratings. proper installation, operation, operation. and maintenance are the responsibility maintenance responsibility of the system designer designer and user. Alloy 600 Bellows Material On On "4/6/8U" "416IBU" SeriesSeries only only - for certain certain corrosive applicationssuch as corrosive applications boiling waler. water, heavy heavy water, water. and pressurized pressurizedwater reactor systems systems Replaces the standard 347 stainless stainless steel steel bellows CREDITS CAECIIS Xei-F
)(fl*~ TM3M
- TM 3MComoany Coon SWAGELOK I'MC-eIjsa fissnConWey erawforl! flll1rl9 To order SWAGELOI< - rM ComDany To order a valvevalve with an alloy alloy 600 bellows, insert insertIN in the valve IFI 17W7P - 1M 17*7Prt TMArl"lCO A~rMs CAJON.
CAJON. VCR. VCR. VCO VCO TMC~ari
- TM Csonany CitOn COfTli,1iny
- TM Slell!! -1w TM CWATCos.
CltlOl CorD. GkatsI TMI GulOll - TM unsr Cab5,e Union ~rtllOf! OrderingNumber. Number.Examples: Examples: SS-8UG*TWIN SS-8UG-TWIN SS-4UW*IN4C SS-4UW-IN4C Ordering
",.,,: Yo", """ . .,th"",. S... & SeNO' A.p'~'"''
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AIR CURVE i t.S h 800 1000 1200 1400 1600 1800 2000 2200 41 DOWNSTREAM PRESSURE PSIG (0 PSIG"'14.7 PSIA) FLOW FORMULAS FOR GASES (( Recommended by the Fluid Controls Institute, Inc. (4) SPECIFIC GRAVITY TABLE FOR GASES Q=16.05C. Where: Q=FJow in SCFM C. = Valve flow coefficient SG = Specific gravity of gas (Air @ 14.7 PSIA and 70°F = 1.0) H =Absolute temperature of flowing gas (OF +460)
~p =(PI - P2) Pressure drop (PSI)
PI = Inlet pressure (PSIA) P2 =Outlet pressure (PSIA) tRefer to "USEFUL CONVERSION DATA" on reverse side of "Tech* nical Information" tab for converting *C to of.
*When outlet pressure is approximately one half or less of the inlet pressure (P 2 =.53P 1) this condition becomes known as a critical pres*
sure and then formula (5) must be used. Formula (5) is exactly the same as formula (4) except that .53XP) is substituted for P2* Flow calculations and charts for gases differ from those for liquids due primarily to the compressibility of gases. The above chart shows the flow rates in standard cubic feet per minute (SCFM) of 70°F air flowing through a valve having a C. =' 1. From this chart, sizing of a valve can be readily accomplished. Corrections for gases having specific gravities other than air and flowing at temperatures other than 70°F can be made by using formulas (4) or (5).
Calculation Calculation PM-0375 PM*0375 Attachment Attachment II Computation 01 11-- Computation of System System Leakage Leakage (ECR (ECR 09-00416) 09-00(16) 77 day Leakage Estimate day Leakage Estimate 77 day day 7day 7day Drop Drop Makeup Makeup to to Estimated Estimated rolling rOiling rolling rOiling Fill Cycle Data Point Level pals per Day Volume Delta DeUa V V DW DW Leakrage Leakage total ave avq Fill Cycle oata Point level psiS per Day Volume 1018/ 8/4/2008'.. 51 180 453041 453041 Total Total Volume Volume (sct) (sci) 81939.4 81939.4 51 180
.8/5/2008 50 185 11 443458 443458 9583.8 95838 9583.8 9583,8 Days Days 14 50 185
, .6/2008. ::';:.!:=; 49.5 187.5 0.5 439323 4134.3 4134,3 4134.3 4134.3 Average Average Volume/day Volume/day 5852.816 5852.816 49.5 187.5 0,5 439323
.8/712008 4 49 187.5 0.5 435218 4105.2 4105,2 4105.2 4105,2 Avg7day Avg 7 day rolling rolling total lotal 41597.0 41597,0 49 187.5 0,5 435218
.8/2008.' 45 187,5 4 398822 36396.4 38396.4 Max 7 day Max 7 day rolling rolUng total 10lal 62654.3 62654,3 45 187.5 4 398822 38396.4 36396.4 819(2008..:: 45 187,5 0a 398822 398822 0.0 0.0 1512.209 1512.209 -1512.2
-1512.2 Max Max 11 Day Day Drop Drop (in)(in) 4 45 187.5 8/10/2008;; 44 187.5 11 388875 9946.9 9946,9 9946.9 9946,9 Avg Avg 1 DayDay Drop Drop (in)
(in) 0.642857 0,642857 44 187,5 388875 81112008 .. " 44 187.5 0 388875 0.0 0.0 8/122D2008 44 43.5 187.5 190 0.5 a 388875 383750 0.0 5125.0 0,0 62654.3 62654.3 8950.6 8950.6 43,5 190 0.5 383750 5125.0 5125.0 5125.0 58195.5 58195.5 8313.6 8313.6 8/13/2008 43 190 0.5 378800 5150.0 5193.0 59211.2 8458.7 43 190 0.5 378600 5150,0 5150,0 59211,2 8458.7
.8/1412008 43 195 0 378475 125.0 756.700 -631.7 54474.3 8/15/2008:.:.
43 42 195 195 a 11 378475 125.0 756,700 '631,7 54474,3 7782.0 7782,0 42 195 368008 368008 10468.8 10468,8 10468.8 10468.8 28546.7 28546,7 4078.1 4078.1 8/16/2008"::" 42 200 00 367888 118.8 118.8 ,18.8 118,8 30177.7 4311,1 42 200 367888 30177.7 4311,1 "8042 42 200 00 367888 367888 0.0 0.0 0.0 0.0 20230.8 20230,8 2890,1 2890,1 200 8/18/200 . 42 200 00 367888 0.0 0,0 945.636 -945.6 19285.2 2755,0 42 200 367888 945.636 *945.6 19285.2 2755,0 811912008:l . 51 180 -9 453041 - Total 51 180 *9 453041 Total Volume Volume(act) (scf) 87500.5 87500,5 8:2012008 51 180 00 453041 0.0 0.0 568.655 568,655 -568.7
*568,7 Days 14 51 180 453041 Days 14 8/21/200 50.5 180 0.5 448836 4205.3 568.800 3636.5 Average 50,5 180 0.5 448838 4205.3 568.800 3636,5 Average Volume/clay Volume/day 6250.034 6250,034
'/22/2008 50 185 0.5 443458 5378.4 5378.4 Avg 50 185 0.5 443458 5378.4 5378.4 Avg 77day day rolling rolling total total 57033.5 57033,5
' /23/2008 49.5 190 0.5 439198 4259.5 4259.5 49,5 190 0,5 439198 4259.5 4259,5 Max77day Max dayrolling rolling total total 65332.5 65332.5 8/24/200'8 49 49 190 0.5 435092 435092 4105.9 4105,9 4105.9 4105.9 MaxI 1Day Max DayDropDrop (in)
(in) 44 190 0.5 812512008 . 49 190 0a 435092 0.0 0.0 0.0 0.0 Avg Avg 11Day Day Drop Drop(in) (in) 0.678571 49 190 435092 0,678571 2 8/26/2008 45 190 44 398725 36367.3 36367.3 53179.0 7597.0 2 45 190 398725 36387.3 36367.3 53179,0 7597,0 8/27/2008444 190 1 388800 9925.0 9925.0 63672.7 9096.1 44 190 1 388800 9925,0 9925.0 63672,7 9096,1 8/2812008:.: 43.5 195 0.5 383613 5187.5 5187.5 85223.6 9317,7 43.5 195 0.5 383613 5187,5 5187.5 65223,6 9317.7 8/S-,-29/2008. 43.5 200 0 383475 137.5 137.5 59982.7 8569.0 43.5 200 0 383475 137,5 137,5 59982,7 8569.0
'8/3/2008.'...: 43 200 0.5 378350 5125.0 1043.595 4081.4 59804.6 8543.5 S 8/31/'2 . 43 200 0,5 378350 5125.0 1043.595 4081.4 59804.6 8S43.5 43 200 0 378350 0.0 947.436 -947.4 547512 9/1/2008 43 42 200 205 1 a 378350 367769 0.0 10581.3 947.436 *947.4 10581.3 54751.2 7821.6 7821.6 42 205 1 387769 10581,3 10581.3 65332.5 65332,5 9333.2 9333,2
" 2/2008:
. 41.5 205 0.5 362413 5356.3 5356.3 34321.5 4903.1 41,5 205 0.5 362413 5356.3 5356,3 34321.5 4903.1 9/3/2008.::. 52 175 -10.5 461674 - - Total
" 9/312008" " 52 175 *10.5 461674 TotalVolume Volume(set) (scf) 90283.1 90283,1 9/4/20086 9/4/2008, ',' , 52 175 00 461674 0.0 0.0 Days 16 52 175 461674 0.0 0.0 Days 16 955`2008 51 1B0 1 453041 8632.1 8632.1 Average 91512008, ",,' 51 180 453041 6632.1 6632,1 AverageVolume/day Volume/day 5642.692 5642,692 "9/62008.. 51.5 180 -0.5 457187 -4146.0 -4146.0
,"'~~;'i' 51.5 180 -0.5 457187 -4146,0 -4146,0 Avg Avg77daydayrolling rollingtotal total 51995.0 51995.0 9/7/2008. 51 180 0.5 453041 4146.0 4146.0 Max 51 180 0,5 453041 4146.0 4146,0 Max77day dayroling rollingtotal lotal 69070.4 69070.4 9/8/2008 50.5 180 0.5 448836 4205.3 2462.316 1743.0 Max
" 9/812008,' ", ... ~.
50.5 180 0.5 448836 4205.3 2462,316 1743.0 Max11Day DayDrop Drop(in) (in) 44 9/9/2008 50 180 0.5 443705 5131.0 5131.0 91912008:" 50 180 0.5 443705 5131,0 5131.0 AvgI 1Day Avg DayDropDrop(in)(in) 0.625 0.625 911012008 48 180 2 427012 16693.2 16693.2 32199.3 4599.9 9/101200if 48 180 2 427012 16693.2 16693.2 32199,3 4598,9 3 ,. 9/1/2008 48 180 0 427012 0.0 1040.698 -1040.7 31158.6
- '~' S,911'i/2008' "91122008 48 44 180 180 4 0 427012 389100 0,0 1040.698 -1040.7 31158.6 4451.2 4451.2
" ",' 9i1:?J2008" . 44 180 4 389100 37911.9 37911.9 37911.9 37911.9 60438.5 604J8.5 8634.1 8634.1 91312.008 44 180 0 389100 0.0 0.0 64584.4 9226.3
,. '9/14/2008.
9i131200a"" 44 180 0 389100 0.0 0,0 64584.4 9226.3
" , " . 9/15/2008,,k. 9i1 412008:,'.j,. ,.;., 43.5 43.5 43 185 185 185 0.5 0.5 0.5 383888 383888 378725 5212.5 5212.5 5162.5 5212.5 5212.5 5162.5 65651.0 65651.0 9378.7 9378.7 69070.4 9867.2
, ".' .~, 9O12008 ,9/,15!2q<l8:,;" ,,' ..
43 43 185 185 0 0.5 378725 5162.5 5162,5 69070.4 9867.2
" 9/17/2m8*9/1612008 ..:'," 378725 0.0 0,0 0.0 63939.4 9134,2 42.5 43 185 0 378725 0.0 63939.4 9134,2 190 0.5 373400 5325.0 5325.0 52571.2 75102
*, /18/2008 g!17/2ocia., .', 42,5 42 190 200 0.5 0.5 373400 367888 5325.0 5512.5 5325,0 5512.5 52571,2 7510.2 9/18/2008 ,'.' 367888 5512.5 5512,5 59124.4 59124,4 8446.3 8446,3 9/19/2008 - 4242 200 200 0 0.5 367888 0.0 0.0 21212.5 3030.4
*9/20/2008-.
911 sii!008z. . "'.. H 5042 200 190 -80 367888 443210 -0,0 -0,0 21212.5 3030.4 Total Volume (sct) 74235.1 912012008,',' " ,'...*,"",::.: 9/21/20018' 50 190 -8 443210 Total Volume (scf) 74235,1
- ' 50 190 0 443210 0.0 0.0 Days 12 9/21/2008'..' - .. ' 50 190 0 443210 0.0 0.0 Days 12 9/22/2008 0 50 190 0 443210 0.0 1325.102 -1325.1
. - ',9/2~2iI08 '. 50 190 0 '443210 0.0 1325.102 -1325.1 Average AverageVolume/day Volumelday 6186.262 6186,262 9/23/2008- 49 190 1 435092 8118.0 8118.0 Avg 9/2J12008, Hi.
9/24/2008 49 190 1 435092 8118,0 8118,0 Avg77daydayrolling rollingtotal totat 53720.3 53720.3 48.5 190 0.5 430818 4274.8 4274.8 i.",,' .'",.. ~/24/20(!8'1 25/2008. .' 48,5 190 0,5 430818 4274,8 4274,8 Max Max7 7day dayrolling rolUngtotaltotal 64860.3 64860.3
*9/26 '912512008'.; ;. . 45 195 3.5 398531 32286.3 32286.3 Max 1 Day Drop (in) 3.5 4 /2:8 44.545 195 195 0.53,5 398531 393656 32286.3 4875.0 32286.3 4875.0 Max1 1 Avg DayDrop Day Drop (in) 3.5 9/2&2008::' . , (in) 0.666667 4 44,5 195 0.5 393656 4675.0 4875.0 Avg 1 Day Drop (in) 0,668667
. ~9/28/2008,
?912712008. 44 200 0.5 388500 5156.3 5156.3 53385.1 7626,4 d
9/27/2008'; " ,'" 44 200 0,5 388500 5156.3 5156,3 53385.1 7626.4 43.5 200 0.5 383475 5025.0 5025.0 58410.1 8344,3 9/28t20oil:',' 9/29/2008 43.5 43 200 200 0.50.5 383475 378350 5025.0 5125.0 5025.0 5125.0 58410,1 8344,3 64860.3 9265.8
!ii29i2008::"
9/30/008 43 200 0,5 378350 5125.0 5125,0 64860,3 9265.8 43 205 0 378225 125.0 125.0 56867.3 8123.9
, 9/3012008' 10/1/2008. 43 205 0 378225 125.0 125.0 56867.3 8123.9
. 42.5 210 0.5 372900 5325.0 5325.0 57917.5 8273.9
":,011/2008; 42.5 210 0.5 372900 5325,0 5325,0 57917.5 8273.9 10/2J2008 H
, , 101212008 42 210 0.5 367650 5250.0 5250.0 30881.3 4411.6
.10/32008 42 210 0,5 367650 5250.0 5250,0 30881.3 4411.6 49.5 180 -7.5 439699 Total Volume (set) 78064.2
- ,>1013/2008.' . "" , ' 49,5 180 439699
...'10/4/2008.,
* .... 101412008. ;.:-. ,":
49.5 180 0-7.5 439699 0.0 474.018 -474.0 Total Volume (scf) Days 78084.2 1010
.1 49,5 180 0 439699 0,0 474,018 *474,0 Days
. 0/5/2008 49 180 0.5 435596 4103.0 4103.0 Average
", .1016/2008
,'101512008':
48'549 180180 0.50,5 435596 4103.0 4103,0 AverageVolume/day Volume/day 7806.425 7806.425
.lOt&2008 ,,~ 431309 4287.4 663.457 3623.9 Avg 7 day rolling total 67857.9
'. H 07/2008 48,5 180 0.5 431309 4287,4 663.457 3623,9 Avg 7 day rOiling totat 67857,9 48 180 0.5 427012 4296.8 758.622 3538.2 Max 7 day rollingtotal 5 .
iOriI2008,: 10/812008 4748 180180 10,5 427012 418040 4296.8 758.622 3538,2 Max 7 dayrolling total 74435.3 74435.3
* ' 101812008' ,
8971.9 8971.9 Max I Day Crop (in) 4 S1/0/2008, 47 180 1 418040 B971 ,9 8971,9 Max 1 Day Drop lin) 4 43 180 4 378850 39190.0 39190.0 . Avg 1 Day Drop (in) 0.85
;' ,: 101912008,,' 43 180 4 378850 39190,0 39190,0 Avg 1 Day Drop (in) 0.85 10/10/2008:: . 42.5 185 0.5 373525 5325.0 568.967 4756.0 63709.0 9101.3 1&1012008:; " "
10/11/2008. 42,5 185 0.5 373525 5325,0 568.967 4756.0 63709,0 9101.3 42.5 185 0 373525 0,0 1707.286 -1707.3 62475.8 8925.1
- lq111/2008 ,.,'
10/12/2008. 42.5 185 0 373525 0.0 1707.286 -1707.3 62475,8 8925.1 41 185 1.5 357463 16062.5 16062,5 74435.3 10633.6 1011212008 10/13/2008"41 41 185 1.5 357463 16062.5 16062,5 74435.3 10633.6
*ioi.131200B", ' 185 0 357463 0.0 0.0 70811.4 10115.9 10/14/2008 41 185 0 357463 0,0 0.0 70811.4 10115,9
, . 10114/2008' 50 185 -9 443458 - Total Volume (sdf) 80949.6 10/15/200 50 185 *9 443458 Total Volume (scf) 80949,6
.= 50.6 185 -0.5 448506 -5048.3 -5048.3 Days 13
'IOJ15t2008:
10/018/2008 50,5 185 -0.5 448506 *504B,3 '5046,3 Days 13 50 185 0.5 443458 5048.3 5048.3 Average Volume/day i QjI612008::; , i0/17/2008:4 49.550 185185 0.50.5 443458 439449 5048,3 4009.0 5046.3 4009.0 Average VOlume/day 6226.891 6226.891 1011712008', 49,5 4009.0 Avg 7 day rolling total 61112.5 10/18/,008. :. 49 185185 0.50.5 439449 4009.0 Avg 7 day rolling total 61112,5 435344 4104.4 4104.4 Max 7 cay rolling total 73595.3 1011812008'" ", 49 185 0,5 435344 4104.4 4104.4 Max 7 day rolling total 73595.3
. 1.0/19/2008. . .-
"10/1912008:':; 4949 185 00 435344 0.00,0 759.201 -759.2 185 435344 759,201 -759,2 Max Max 1 1Day DayDropDrop (in)lin) 55 6 10/20/2008" lo120i200B. ' 4444 185 55 388950 46394.2 46394.2 Avg 185 388950 46394.2 46394.2 Avg1 1DayDayDropDrop(in)(in) 0.692308 0,692308
'10.21/2008*-.- 4444 190 00 288800 150.0 2223.332 10/21i2008<', ;
10/22/2008 190 388800 150,0 2223,332 -2073.3 *2073.3 51675.2 51675,2 7382.2 7382.2 43 190 1 378600 10200.0 758.932 9441.1 66164.5 9452.1 10/2212008.:,: ' 43 190 378600 10200.0 758.932 9441.1 66164.5 9452,1 10/23/2008 42 190 1 368125 10475.0 1416.640 9058.4 70174.6 10024.9 1012312OCis.' " 10/24/2008 41.5 42 190190 0.5 1 368125 362750 10475.0 1416,640 9058,4 70174,6 10024,9 5375.0 5375.0 71540.5 10220.1 10/25/2008 1()I24/2008 " . ' 41,5 41.5 190190 00.5 362750 362750 5375.0 0.0 5375.0 71540,5 10220,1 0.0 67436.1 9633.7 1012512008:' . 41,5 190 0,0 0.0 0.5 0 10/21/2008 362750 67436.1 9633.7 41 190 357350 5400.0 5400.0 73595.3 10513.6 10/2612008 41 190 0.5 357350 5400.0 5400,0 73595.3 10513.6 Page Page 1 of 1 of99
Calculation PM*0375Attachmenl CalculationPM-0375 Allachmentll leakage(ECR SystemLeakage
- ComputationofofSystem II - Computation (ECR09-00416) 09-00416) 7 7day LeakageEstimate dayLeakage Estimate 10/2612008'.* .> ," ....,
10/2612008. 4141 190 190 0o 357350 357350 0.0 0.0 0.0 0.0 27201.1 27201.1 3885.9 3885.9 . 10/27/2008 5252 180 180 -11
*11 461274 461274 - Total VolUme(scf)
TolalVolume (set) 93391.5 93391.5
.1028/2008:, 51.5 180 180 0.5 0.5 457187 457187 4088.6 4086.6 4086.6 4086.6 Days Days 13 13 51.5 10/29/2008 5151 180 180 0.5 0.5 453041 453041 4146.0 1701.260 4146.0 1701.260 2444.7 2444.7 Average Volume/day Average Volume/day 7183.961 7183.961 10/30/2008.49.5 49.5 180 180 1.5 1.5 439699 439699 13342.4. 3892.135 13342.4. 3892.135 9450.2 9450.2 Avg Avg7day rollingtotal 7 dayrolling total 54734.9 54734.9 10/31/200.i. 49.5 49.5 185 185 0o 439449 439449 250.5 250.5 250.5 250.5 Max77day Max dayrolling roilingtotal total 71703.3 71703.3 11//2008 4949 185 185 0.5 0.5 435344 435344 4104.4 4104.4 4104.4 4104.4 Max Max11Day Drop(in)
DayDrop (in) 33
.2/2008 47.5 47.5 180 180 1.5 1.5 422818 422618 12726.0 4637.399 12726.0 4637.399 8088.6 8088.6 Avg
.Avg11Day DayDrop Drop(in) (in) 0.846154 0.846154 7 11/3/2008 4747 180 0.5 418040 4578.2 4578.2 33003.2 4714.7 180 180 0.5 0.5 418040 413363 4578.2 4677.5 4578.2 4677.5 330OJ.2 33594.1 4714.7 4799.2
."11/4/2008...........46.5 46.5 180 0.5 413363 4677.5 4677.5 33594.1 4799.2 11/5/2008, 4545 185 185 1.5 1.5 398919 398919 14443.8 14443.8 14443.8 14443.8 45593.2 45593.2 6513.3 6513.3 11//2008 . 4242 185 185 33 368244 368244 30675.0 30675.0 189.199 189.199 30485.8 30485.8 66628.7 66628.7 9518.4 9518.4 11/7/2008-, 41.5 41.5 182.5 182.5 0.5 0.5 362919 362919 5325.0 5325.0 5325.0 5325.0 71703.3 71703.3 10243.3 10243.3 8/2008 41.5 41.5 185 185 0o 362863 362863 56.3 56.3 56.3 56.3 67655.1 67655.1 9665.0 9665.0 I i9/2008 4141 185 185 0,5 0.5 357463 357463 5400.0 5400.0 5400.0 5400.0 64966.5 64966.5 9280.9 9280.9 1/10/2008. 49.5 49.5 180 180 -8.5
*a.5 439699 439699 Total TotalVolume Volume(sct)(sef) 72791.6 72791.6 48.5 8111112008 48.5 175 175 11 431554 431554 6144.7 8144.7 6238.894 6238.894 1905.8 1905.8 Days Days 89 11112/2008. 4848 180 180 0.5 0.5 427012 427012 4542.4 4542.4 1414.492 1414.492 3127.9 3127.9 Average AverageVolume/day Volume/day 8087.952 8087.952 1 I 3/2008i - 47.5 47.5 180 180 0.5 0.5 422618 422618 4393.7 4393.7 4393.7 4393.7 Avg Avg77day rollingtotal dayrolling tolal 65681.8 65881.8 8............1 /2008 , 47 47 180 180 0.5 0.5 418040 418040 4578.2 4578.2 4578.2 4578.2 Max Max77day dayrolling rollingtotal total 67757.8 67757.8 8 11/15/2008 47 180 0o 418040 0.0 0.0 Max 1 Day Drop (in) 3 47 180 418040 0.0 0.0 Max 1 Day Drop (in) 3 II 16/2008 45 45 185 185 22 398919 398919 19121.3 19121.3 19121.3 19121.3 Avg I Day Drop Avg 1 Day Drop (In) (in) 0.944444
'I 17/2008,,B 0.944444
, 42 185 3 368244 30875.0 30675.0 63802.0 9114.6 42 185 3 368244 30675.0 30675.0 63802.0 9114.6 11/18/2008* 41.5 41.5 185 185 0.5 0.5 362863 362863 5381.3 5381.3 1791.640 1791.640 3589.6 3589.6 65485.7 65465.7 9355A1 9355.1 11/i19/20,08, 4141 185 185 0.5 0.5 357463 357463 5400.0 5400.0 5400.0 5400.0 67757.8 67757.8 9679.7 9679.7
.,11/20/2008.. : 51 51 180 180 -10
*10 453041 453041 - - TolalVolume Total Volume(scf) (scI) 86791.3 86791.3 11/21/2008. 5151 180 180 0o 453041 453041 0.0 0.0 0.0 0.0 Days DayS 14 14 1.122/2008 i 5151 180 180 0o 453041 453041 0.0 0.0 1608.147 1608.147 .1608.1 Average Volume/day 6199.38
*1608.1 Average Volume/day 6199.38 11/23/2008 5050 180 180 11 443705 443705 9336.3 9336.3 471.842 471.842 8864.5 8864.5 Avg 7 day rolling total Avg 7 day rolling total 47653.6 47653.6
.1,1/24/2008 50 185 185 0o 443458 247.4 247.4 Max 7 day rolling total 70922.1 50 443458 247.4 247.4 Max 7 day rolling total 70922.1 3.5 11/25/2008 49.5 49.5 185 185 0.5 0.5 439449 439449 4009.0 4009.0 4009.0 4009.0 Max I1Day Max Drop (in)
Day Drop (in) 3.5 1 26/2008. 49 190 0.5 435092 4356.4 4356.4 Avg 1 Day Drop (in) 0.696429 49 190 0.5 435092 4356.4 4356.4 Avg 1 Day Drop (in) 0.696429 99 11/27/2008 49 49 190 190 0o 4.35092 435092 0.0 0.0 0.0 0.0 15869.2 15869.2 2267.0 2267.0 1128/2008 484S 190 190 11 426524 426524 8568.4 8568.4 8568.4 8568.4 24437.6 24437.6 3491,1 3491.1 11/29i2008 47.5 47.5 190 190 0.5 0.5 422136 422136 4387.5 4387.5 4387.5 4387.5 304.33,2 30433.2 4347.6 4347.6
. 1/3/2008 . 4444 195 195 3.5 3.5 388650 388650 33486.4 33486.4 33488.4 33488.4 55055.1 55055.1 7865.0 7865.0
" 12/1*/208:. 43.5 43.5 200 200 0.5 0.5 383475 383475 5175.0 5175.0 756.030 756.030 4419.0 4419.0 59226.7 59226.7 8461.0 8461.0 12/212008.- 42.5 42.5 200 200 11 373150 373150 10325.0 10325.0 3117.521 3117.521 7207.5 7207.5 624Z5.1 62425.1 8917.9 8917.9 3/2008 4242 200 200 0.5 0.5 367888 367888 5262.5 5262.5 471.603 471.603 4790.9 4790.9 62859.6 62859.6 8979.9 8979.9 4/2008 41.25 41.25 200 200 0,75 0.75 359825 359825 8062.5 8062.5 8062.5 8062.5 70922.1 70922.1 10131.7 10131.7
. . . :. /125/2008 Ii~~~:;:;>":;.':
J6/200.8 - 55 55 55 55 180 180 160 180
-13.75
*13.75 0o 484546 464546 484546 484546 0.0 0.0 0.0 0.0 Total Days DayS Volume (sct)
Total Volume (set) 106216.8 106216.8 17 17
- '1V712OOa-' ..: .' .. , 54.5 "127/008- 54.5 180 180 0.5 0.5 480816 480816 3730.2 3730.2 3730.2 3730.2 Average Volume/day Average Volume/day 6248.047 6248.047 12/82008 121si2008 : .. . 53 180 180 1.5 469269 11547.0 189.175 11357.8 Avg 7 day rolling total 48192.3 53 1.5 469269 11547.0 189.175 11357.8 Avg 7 day rolling total 48192.3
", ',_ . ': 1-iJ9/2008~. ',~, :~.:
S' O.N/-
'," 53 180 0o 469269 0.0 0.0 Max 7 day rolling total
- 121HY2008 ..,,::.:" .
12/110/208, 52.5 53 52.5 180 182.5 182.5 0.5 0.5 469269 465089 465089 0.0 4180.3 4180.3 0.0 4180.3 4180.3 Max 7 day rolling tolal Max 1 Day Drop (in) SitJi9J6!iB 3 I,,' Max 1 Day Drop (in)
'. ;:. 1211.1i2008~'**
12/111/2008 ,,. 5252 182.5 182.5 0.5 461074 461074 4014.5 4014.5 23282.8 3326.1 Avg 1 Day Drop (in) 0.7547083 182.5 0.5 0 401074 4014.5 0.0 0.0 4014.5 Avg 1 Day Drop (in) 0.764706 52
- ~:~~~~;:. "::
12/1212008 52 182.5 461074 0.0 0.0 23282.8 3326.1
..... 112/13/2008 5252 182.5 182.5 0 461074 461074 0.0 0.0 4628.866 4628.866 -4628.9
-4628.9 18653.9 18653.9 2664.8 2664.8 10
- ~:~~~::'
10 .. 11/2008 . . 50.5 50.5 177.5 177.5 1.5 1.5 449001 449001 12073.0 12073.0 12073.0 12073.0 26996.7 26996.7 3856.7 3856.7
'. .12/15/2008 50 180 180 0.5 0.5 443705 443705 5296.1 . 5296.1 5296.1 20934.9 2990.7 50 5296.1 20934.9 2990.7 12.11/2008 12/'1612008',* ",. 48 180 180 22 427012 427012 16693.2 16693.2 1135.450 15557.7 36492.7 5213,2 48 1135.450 15557.7 36492.7 5213.2 12f.17126mf:*::. ... '!.:.
1P117/208 O " '45
'45 180 180 33 399113 399113 27899.4 27899.4 60211.8 8601.7 27899.4 27899.4 60211.8 8601.7 1216/2008
* '. 12118/2008 '" ,.'.. ':';:, ':,.; . 4444 180 180 11 389100 389100 10012.5 10012.5 1134.476 1134.476 8878.0 65075.4 9296.5 8878.0 65075.4 9296.5 12/19/2008W.....
.1211912008:',,'" :; ......
. , .:.'. 4444 186 185 0o 368950 388950 150.0 150.0 150.0 150.0 65225.4 65225.4 9317.9 9317.9
.; 1/20/2008.:
1,2i2oi2008:t: ; ' : : , 43.5 185 185 0.5 383818 5062.5 5062.5 74916.8 10702.4
'12/21/2008, 43.5 43 190 0.5 0.5 383888 378600 5062.5 5287.5 5062.5 5287.5 74916.8 68131.3 10702.4 9733.0
- 1212112008" ;. 43 190 0.5 378600 5287.5 5287.5 68131.3 9733.0 1222/2008 , 42 190 1 368125 10475.0 3116.356 7358.6 70193.8 10027.7 12i22i20oii.' ......:' 42 190 1 368125 10475.0 3116.356 7358.6 70193.8 10027.7 Total Volume (sot) 12/23(20.8 50.5 180 -8.5 448836 80618.7 1212312008. '. ...: 50.5 180 '8.5 448836 T01al Volume (sef) 80618.7
,12/2/2008. 50.5 180 0 448836 0.0 587.438 -567.4 Days 16
*'i2l24f20oa, 50.5 180 o 448836 0.0 567.438 *567.4 Days Volume/day 16 12/25/2008 .
"1212si200S' , 50 185 0.5 443458 5378.4 5378.4 Average 5038.667 50 185 0.5 443458 5378.4 5378.4 Average
.. 12/26/2008 50 186 0 443458 0.0 0.0 Avg 7 dayVolume/day rolling total 5038.667 47039.4 1212612008*.
w12/27/200 . 50 50 185 185 o 0o 443458 443458 0.0 0.0 0.0 0.0 Avg 7 day rolling total Max 7 day rolling total 47039.4 65107.7 12127120oa!<" 50 185 443458 0.0 0.0 Max
- 12/28/2008'.,-
121281200e',._ 49.5 185 0.5 439449 4009.0 4009.0 Max 1 Day rolling 7 day Drop (in) lotal 65107.7 2.5 49.5 185 0.5 439449 4009.0 4009.0 MaxI1 Day Day Drop Drop (in) (in) 2.5
* '292008 12129120'08:.* .. 49 190 0.5 435092 4356.4 4356.4 Avg 0.53125 49 190 0.5 435092 4356.4 4356.4 Avg 1 Day Drop (in) 0.53125
'" "', 1i2/P30/2008:; 213012008'; 48 48 195 195 11 426280 426280 8812.4 8812.4 21988,8 3141.3 8812.4 8812.4 21988.8 3141.3 11 11 12/31/2008: 46.5 195 1.5 412556 13723.6 13723.6 36279.9 5182.8 12i31/200S: . ": . 46.5 195 1.5 412556 13723.6 13723.6 36279.9 5182.8 1/1/2009
'1l1i2009.: 44 200 2.5 388500 24056.3 24056.3 54957.7 7851.1 44 200 2.5 388500 24056.3 24056.3 54957.7 7851.1 1/2/2009 li2J20cie:' ..' 44 200 0 388500 0.0 0.0 54957.7 7851.1 44 43 200 200 o
11 388500 378350 0.0 10150.0 0.0 10150.0 54957.7 65107.7 7851.1 9301.1
'" . , .1/13/2009 .'11312009,.-,:,'. 43 200 376350 10150.0 10150.0 65107.7 9301.1 1/42009 " 43 200 0 378350 0.0 0.0 61098.6 8728.4 1/412009;;' 43 43 200 205 0 o 378350 378225 0.0 125.0 0.0 125.0 61098.6 56867.3 8728.4 8123.9
,::;.',~" 1/5/2009
*llsi20Q9.':* 43 205 o 378225 125.0 125.0 56867.3 8123.9
,. .,'. "I~~:/,;, 1/6/2009 1:*72009.- .:'
42.5 42.5 42 42 210 210 210 210 0.5 0.5 0.5 0.5 372900 372900 367650 367650 5325.0 5325.0 5250.0 5250.0 5325.0 5325.0 5250.0 5250.0 53379.8 53379.8 44906.3 44906.3 7625.7 7625.7 6415.2 6415.2
. . ~.; :'. 1/8t2009;' 8/2009 42 42 210 210 0 a 367650 367650 0.0 0.0 0.0 0.0 20850.0 20850.0 2978.6 2978.6
.1/9/2009.
* .1/912009* . ,.. 52 185 -t0 460874 Total Volume (scd) 97658.2 52 185 *10 460874 TOlal Volume (set) 97658.2
.'/, 1/10/2i09 1I1oi2009" :.' ."0:.,;: ...*. 52 185 0 460874 0.0 472.579 -4726 Days 14 52 185 o 460874 456437 0.0 4437.6 472.579 *472.6 4437.6 Days Average Volume/day 6975.585 14
... :. : 1/11/2809-1/1.'112009', 51.5 51.5 190 190 0.5 0.5 456437 4437.6 4437.6 Average
-111212009**:**..
.1/1229 i .:.' 51 190 0.5 452337 4099.7 4099.7 Avg 7 dayVolume/day rolling total 6975.585 45877.8 51 190 0.5 452337 4099.7 4099.7 Avg 77 day 1/13/2009
'1/1312009;"':' . ' . 51 190 0 452337 0.0 0.0 Max day rolling total rolling total 45877.8 69061.4 V114/20091.
,.,"lil412000' .,:.::"
51 50 190 190 o 1 452337 443210 0.0 9126.9 0.0 9126.9 Max 71 Day Max day rolling Drop (in) tolal 69061.4 2.5 50 190 1 443210 9126.9 9126.9 Max 1 Day Drop (in) 2.5 1/15/2009
* '111512009 49.5 190 0.5 439198 4012.1 3022.260 989.8 Avg I Day Drop (in) 0.785714 49.5 190 190 0.5 1.5 439198 426524 4012.1 12674.3 3022.260 2258.842 989.8 10415.5 28596.8 4085.3 Avg 1 Day Drop (in) 0.785714 12 1/18/2009. . 48 12 , 1/1612009.':.*'-' 48 190 1.5 426524 12674.3 2258.642 10415.5 28596.8 4085.3
- lIiii2000" .
1/17/2009 48 48 190 190 0 o 426524 426524 0.0 0.0 0.0 0.0 29069.4 29069.4 29019.3 4152.8 4152.8 4145.6 1/18/2009 ........
- 1/1812009 47.5 190 0.5 422136 4387.5 4387.5 47.5 190 0.5 422136 4387.5 4387.5 29019.3 4145.6 1/19/2009 1/19/2009'.: .. 47 190 0.5 417580 4556.4 4556.4 29476.0 4210.9 47 190 0.5 417580 4556.4 4556.4 29476.0 4210.9 1/20/2009.. 45 190 2 398725 18855.0 18855.0 48331.0 6904.4 1120/2009*, 45 190 2 398725 18855.0 18855.0 48331.0 6904.4 Page 22 of Page 0199
Calculation Calculation PM-0375 Attachment IIII--Computation PM-0375 Allachment Computation 01ofSystem Leakage (ECR System Leakage (ECR 09-00416) 09-00416) day leakage 77 day Estimate Leakage Estimale
;,' 't'. '1/21/2009,'
1/21/2009!-. 112/2009 .-
. 42.5 42.5 42 42 195 195 190 190 2.5 2.5 0.5 0.5 373275 373275 36B125 368125 25450.0 25450.0 5150.0 5150.0 25450.0 25450.0 5150.0 5150.0 64654.1 64654.1 66814.4 68814.4 9236.3 9236.3 9630.6 9830.6
, ; 1122120097'.:
- '::: ;::.:;;:- 112312009"';
1/2-/2009 . ,
..*.:.*.i.-.';' .:. . ::. 41 185 9865.9 41 185 11 357463 357463 10662.5 10662.5 10662.5 10662.5 69061.4 69061.4 9865.9
-1/24/2009 . . 8 53 53 180 180 -12
-12 469269 469269 Total Total Volume Volume (scI)
(sol) 75378.2 75378,2
' /2520.092 53 53 180 190 o0 469269 469269 0.0 0.0 2446.106 2446.106 -2446.1
-2446.1 Days Days 13 13 1/26/2009: ,.V 52 52 180 180 11 461274 461274 7994.9 7994.9 1223.540 1223.540 6771.4 6771.4 Average Average Volume/day Volume/day 5798.321 5798.321 1/27/20M09-. ,' . 51.5 51.5 180 180 0.5 457187 457187 4086.6 4068.6 4086.6 4086.6 Avg Avg 77 day rotting lotal day roiling Uotal 39427.8 39427.8
. 128/209- " 51 51 180 180 0.5 453041 453041 4146.0 4146.0 4146.0 4146.0 Max Max 77 day day roiling roling tolal total 62820.4 62820.4 1729/2009,-." 51 51 180 190 o 0 453041 453041 0.0 0.0 0.0 0.0 Max 1 Day Drop Max 1 Day Drop (in) (in) 3.5 3.5 13.'".;:'. :1/3012009 . , 50.5 50.5 185 185 0.5 448506 448506 4535.5 4535.5 4535.5 4535.5 Avg Avg 1I Day Day Drop Drop (in)
(in) 0.692308 0.692308 13 11/31/2009 50 185 443458 5048.3 3163.1 50 185 0.5 443458 5049.3 5048.3 5049.3 22141.6 22141.6 3163.1 2, /1009;* ., . 50 50 186 185 o 0 443456 443458 0.0 0.0 0.0 0.0 24587.7 24587.7 3512.5 3512.5 2/0/2009 49.75 49.75 187.5 0.25 187.5 0.25 441329 441329 2129.0 2129.0 2129.0 2129.0 19945.3 19945.3 2849.3 2849.3 S2/3/209 48 48 185 185 1.75 1.75 426768 426768 14560.8 14560.9 14560.8 14560.8 30419.5 30419.5 4345.6 4345.6 2/4/2009 44.5 44.5 190 190 3.5 393825 393825 32942.9 32942.9 1421.114 1421.114 31521.8 31521.8 57795.4 8256.5 8256.5 2/5/2009 44 44 190 190 0.5 388800 388800 5025.0 5025.0 62820.4 62820.4 8974.3 8974.3 2/6*2009 44 44 190 190 o 0 388800 388800 0.0 0.0 0.0 58284.8 58284.8 8326.4 8026.4 27/2009: 54 54 180 180 -10
-10 477026 477026 -- Total Total Volume Volume (scI)
(sct) 101341.7 101341.7 2/:s2009 54 54 180 180 o 0 477026 0.0 0.0 0.0 Days Days 18 t8 2/9/2009 - 54 54 180 180 o 0 477026 477026 0.0 0.0 1702.075 1702.075 -1702.1
-1702.1 Average Volume/day Volume/day 5630.092 5630.092 2'.1O2009 53 53 180 180 1 469269 469269 7757.4 n57.4 7757.4 7757.4 Avg Avg 77 day roiling rolling total total 48203.8 48203.8 2/11/2009 52.5 52.5 160 180 0.5 0.5 465301 3967.8 3967.8 3967.8 3987.8 Max Max 77 day rolling rolling 101al total 73183.3 73183.3 2/12/2009 52 52 180 180 0.5 0.5 461274 4027.2 4027.2 4027.2 4027.2 Max 1 Day Day Drop Drop (In)(in) 44 2/13/2009 52 52 180 180 o0 461274 461274 0.0 0.0 Avg 11Day Avg Day Drop (in) (in) 0.666667 0.666667 2/.1412009 : 52 52 180 180 o0 461274 461274 0.0 0.0 14050.3 14050.3 2007.2
.2/15(2009 51 51 185 185 1 452689 452689 8584.7 8584.7 8584.7 8584.7 22634.9 22634.9 3233.6 14 14 2/1.'1612009 50.5 50.5 185 185 0.5 448506 448506 4183.3 4183.3 1133.153 1133.153 3050.2 27387.2 27387.2 3912.5 3912.5 2/1712009 50 50 185 0.5 443458 443458 5048.3 5048.3 24678.1 24678.1 3525.4 3525.4 2/18/2009 46 46 185 185 44 408469 408469 34988.9 34988.9 55699.3 55699.3 7957.0 7957.0 2/191/2009 45.5 45.5 185 0.5 403763 403763 4706.3 4706.3 4706.3 4706.3 56378.3 56378.3 8054.0
.:... 2/2012009 45.5 45.5 185 o 0 403763 403763 0.0 0.0 0.0 56378.3 8054.0 8054.0 2/21/2009 43.5 43.5 180 180 2 384025 19737.5 19737.5 2932.535 16805.0 73183.3 10454.8 10454.8
- 2/22/2009'- 43 43 185 185 0.5 378725 5300.0 5300.0 69898.6 9985.5 9985.5 23/22009 z.., 42.5 42.5 185 185 0.5 0.5 373525 5200.0 5200.0 5200.0 72046.4 72048.4 10292.6 10292.6 2/24/2009. 42 42 185 185 0.5 0.5 368244 5281.3 1791.893 1791.893 3489.4 70489.5 10069.9 10069.9 2/2512009 42 190 190 o0 368125 116.8 118.8 118.8 118.8 35619.3 5088.5 5086.5
." '. 2/26/2009
~;~~~:~<.:'"
2/27/2009: 55 55 54 54 180 180 180 180
-13
-13 11 484546 464546 477026 477026 7519.8 7519.8 Total Total Volume (scf)
Days (scI) 96672.8 96672.8 14 14
':;'V:,~=:" o "228/200" 54 54 175 175 0 477535 477535 -508.2
-508.2 -508.2 Volume/day Average Volume/day 6905.203 6905.203 3/1/2009- 53.5 53.5 175 175 0.5 473657 3877.9 3877.9 Avg 7 day rOiling rolling lotal total 46750.1 31212009' 3/2/2009 53 53 175 175 0.5 0.5 469721 469721 3936.1 3936.1 3936.1 3938.1 Max 7 day day rolling total 69308.0 3/3/2009 - 52.5 175 0.5 465726
*.,31312~~: 52.5 175 0.5 465726 3994.4 3994.4 3590.910 3590.910 403.5 403.5 Max 11 Day Max Drop (in)
Day Drop (in) 55 3/4/2*0019
'. 314/2009'***" 51 51 175 175 1.5 1.5 453394 453394 12332.6 12332.6 12332.6 12332.6 Avg I1 Day Drop (in) (in) 0.857143 0.857143 15 15'. :. 31512009:
3/5/2009. 51 51 175 175 o 0 453394 453394 0.0 0.0 0.0 0.0 27561.6 27561.6 3937.4
' 3/6/2009 50.5 175 0.5 449166 449166 4227.3 4227.3 4227.3 3467.0 3467.0
~~g::,:.,.":,,,
."'. '3/7/20]09Ei
- 50 50.5 50 175 175 175 0.5 0.5 443953 443953 5213.7 5213.7 5213.7 5213.7 24269.1 29991.1 29991.1 4284.4 4284.4
.'3i8l2<ici~::":
3//20d9: . 50 50 175 175 o0 443953 0.0 0.0 26113.2 3730.5 3730.5 3/9/2009.
.' '. 319/2009, 46 45 175 175 5 399306 399306 44646.3 44846.3 1233.340 1233.340 43413.0 65590.1 65590.1 9370.0 9370.0
- al .
102009.:." 311012009:' 44.5 44.5 175 175 0.5 0.5 394331 394331 4975.0 4975.0 853.634 853.634 4121.4 4121.4 69308.0 69308.0 9901.1 9901.1
- 311 i/20<i9' '.,0 .
3/11/2009 44 44 175 175 0.5 0.5 389250 389250 5081.3 5081.3 5081.3 5081.3 62056.7 62056.7 8865.2 8865.2 31i2i2009; . - 43 q3/122009.175 43 175 1 378975 378975 10275.0 10275.0 3220.401 3220.401 7054.6 69111.3 69111.3 9873.0 9873.0 3/13/2009 .: S
" .,.'. 311312009*: 51.5 51.5 175 175 -8.5
*8.5 457563 457563 Total Volume (sof) (scI) 80231.6 80231.6
% , 3/14/2009:
311412009" . 51.5 51.5 175 175 0o 457563 457563 0.0 0.0 759.364 759.364 -759.4
-759.4 Days It 11
.- . '3115/2009'i.
31509- . 51.5 51.5 175 o 0 457563 457563 0.0 0.0 0.0 Average Volume/day Volume/day 7293.777
,,:~!i~m;";
3/1612009:".' 51 51 175 0.5 0.5 453394 453394 4169.1 4169.1 1228.083 1228.083 2941.0 2941.0 Avg 77 day rolling rolling total lotal 66510.5 66510.5 3/17/2009'.::-:- 50 50 180 180 11 443705 443705 9688.5 9688.5 9688.5 9688.5 Max Max 77 day day rolling rolling total tOla1 73241.5 73241.5 16 3/18/200 g: : .'. 50 50 180 180 0o 443705 443705 0.0 0.0 0.0 0.0 Max Maxu 1 Day Drop Drop (in) 4.5 4.5 16 . ,3/19/2009.:*31912009 . ..... 1 45.5 180 4.5 403975 39730.1 39730.1 45.5 180 4.5 403975 39730.1 39730.1 Avg 1 Day Avg Day Drop Drop (in) 0.863636 0.863636
- 31201200!! .; .: :.,. .
D/2012009" 45 45 180 180 0.5 399113 399113 4862.5 4862.5 2934.530 1928.0 1928.0 53528.3 53528.3 7646.9 7646.9
" 3/21/200
- ii2ii2009" . 43.5 43.5 180 180 1.5 1.5 384025 384025 15087.5 15087.5 3314.408 3314.408 11773.1 11773.1 66060.7 66060.7 9437.2 9437.2 312212009:: .". ". .,
3/22/2009: 43 43 185 185 0.5 0.5 378725 378725 5300.0 5300.0 5300.0 5300.0 71360.7 71360.7 10194.4 10194.4
.3/23/2009
'. .. 31231*<i09.,.- . . 42.5 42.5 185 185 0.5 0.5 373525 373525 5200.0 5200.0 378.196 378.196 4821.8 4821.8 73241.5 73241.5 10463.1 10463.1
".' , *. 3/24/2009 312412009 6- .. . 42 42 185 185 0.5 0.5 368244 368244 5281.3 5281.3 472.851 472.851 4808.4 4808.4 68361.4 68361.4 9765.9 9765.9
" '.' 3/25/2009:
312512009" "" ... .-: :"'- 51.5 51.5 175 175 -9.5
-9.5 457563 457563 - Total Total Volume Volume (Sct)(sct) 85010.0 85010.0
'. :' .3/26/2009
,312612009 . 51.5 51.5 175 175 0o 457563 457563 0.0 0.0 567.094 567.094 -567.1
-567.1 Days Days 14 14
... 3/2/2009.
. .3127/2009:" 51 51 180 180 0.5 0.5 453041 453041 4521.3 4521.3 4521.3 4521.3 Average Volume/day Average Volume/day 6072.145 6072.145 3/25/2009..
<312812009.
3/29/2009, 51 51 180 180 0a 453041 453041 0.0 0.0 0.0 0.0 Avg Avg 77 day day rolling rolling total total 54785.5 54785.5 3129/2009. 50.5 50.5 180 180 0.5 0.5 448836 448836 (4205.3 14205.3 4205.3 4205.3 Max Max 77 day day rolling rolling total 101al 69016.2 69016.2 3/2009 48.5 180 22 431309 17527.4 2471.707 15055.7
.;, 31:l0i:W09:"':> 48.5 180 431309 17527.4 2471.707 15055.7 Max 1 Max 1 Day Day Drop Drop (in)(in) 3.5 3.5 3/31/2009 "3131)2009';:: 45 45 175 175 3.5 3.5 399306 399306 32002.5 32002.5 1039.249 1039.249 30963.3 30963.3 Avg 1 Day Drop Avg 1 Day Drop (in) (in) 0.714286 0.714286 17 17 411/2Q()9.i;;: .: ... <..,
", '". 4/1/20089!1' 44.5 44.5 177.5 177.5 0.5 0.5 394247 394247 5059.4 5059.4 5059.4 5059.4 59237.8 59237.8 8462.5 8462.5
." . 4/2/2009
**41212009*:*:....* . 44 44 180 180 0.5 0.5 389100 389100 5146.9 5146.9 665.121 665.121 4481.8 4461.8 64286.7 64286.7 9183.8 9183.8
..... 4i3i2009t ." .
4/3/2009i: 43.5 43.5 180 180 0.5 0.5 384025 384025 5075.0 5075.0 5075.0 5075.0 64840.4 64840.4 9262.9 9262.9 44/412009
;*/4/260.0 . 43 43 180 180 0.5 0.5 378850 378850 5175.0 5175.0 1993.839 1993.839 3181.2 3181.2 68021.5 9717.4 9717.4 68021.5
. 4/6/2009::!
4/612009'- " 42.5 42.5 180 180 0.5 0.5 373650 373650 5200.0 5200.0 -5200.0 69016.2 9859.5
*5200.0 69016.2 9859.5
.4/7/2009 4/712009' . , 42 42 185 185 0.5 0.5 368244 368244 5406.3 5406.3 5406.3 5406.3 59366.8 59366.8 8481.0 8481.0
- 44/812009' O/8/2009 42 42 185 185 0o 368244 368244 0.0 0.0 661.275 661.275 -661.3
*661.3 27742.3 27742.3 3963.2 3963.2
-- . ..:. -: 4/9/2009 41912009,.' :". . 41.5 41.5 192.5 192.5 0.5 0.5 362694 362694 5550.0 5550.0 2460.674 2460.674 3089.3 3089.3 25772.2 25772.2 3681.7 3681.7 4/10/2009.. 52.5 52.5 190 190 -11
-11 464451 484451 -TotaVolume(sot) 78103.6
* .' 41 10I200!l.', ',c', -850.1 3132.798 -3982.9 Total Volume (sct)
Days 78103.6 13 1/.2009 52.5 180 0 465301
. 4/1 411.112009 ' . 52.5 180 o 465301 -850.1 3132.798 *3982.9 Days Average Volume/day 5 13 307.971
' 52 180 0.5 461274 4027.2 755.170 3272.0
. ':'::*41121:i00!f:
-4/12/2009 . " ',:,,'
52 180 0.5 461274 4027.2 755.170 3272.0 Average Volume/day 6007.971 4/13/2009 411312009,'* *t.::; 51 51 180 190 1 453041 453041 8232.5 8232.5 2655.036 2655.036 5577.5 55n.5 Avg 7 day rolling tOlal Avg 7 day rolling total 60654.3 60654.3 4/14/2009. 50 180 11 443705 9336.3 9336.3 Max 411412009'- 50 180 443705 9336.3 9336.3 Max 77 day day rolling rolling total total 71330.0 71330.0 4115/2009:: .' 4/15/2009. 49.5 49.5 180 180 0.5 0.5 439699 439699 4006,0 4006.0 1700.422 170Q.422 2305.6 2305.6 Max Max 11DayDay Drop Drop (in)(in) 4 18~ .~4116/2009F. 49 180 0.5 435596 4103,0 1425.985 2677.0 Avg 18
.41161'2009;, . 49 180 0.5 435596 4103.0 1425.985 2677.0 Avg 11Day Day Drop Drop (in)(in) 0.107143 0.107143 4/17/2009 4117/2009 .. ' 48 46 175 175 11 427256 427256 8340.2 8340.2 8340.2 8340.2 27525.7 3932.2 27525.7 3932.2 411 ai20ci9:
4/18/209" 44 44 175 175 44 389250 389250 38006.0 38006.0 38008.0 38006.0 69514.5 69514.5 9930.6 9930.6 Page Page 33of 9 019
Calculation PM*0375 Calculation PM-0375 Attachment Attachment II* Computation atofSystem II -Computation System Leakage Leakage (ECR (ECR09*00416) 09-00416) day Leakage 77day Estimate LeakageEstimate 4419/2009. :.. 43.5 43.5 175 175 0.5 0.5 384163 384163 5087.5 5087.5 5087.5 5087.5 71330.0 71330.0 10190.0 10190.0
,.,. ;.. :.:;. . 4/.19/2069.', ... : '.",::;:
- ' .:4i~0/2g09.,.
' ..20/2009 -:.:' j 4343 175 t75 0.5 0.5 378975 378975 5187.5 5187.5 5187.5 5187.5 70940.1 70940.1 10134.3 10134.3
. 4/21/20096.
. ",4121/2009":': M i{ .- 4343 180 180 00 378850 378850 125.0 125.0 125.0 125.0 61728.7 61728.7 8818.4 8818.4
- 4/22/200 .** 42.5 42.5 180 180 0.5 0.5 373650 373650 5200.0 5200.0 5200.0 5200.0 64623.1 64623.1 9231.9 9231.9
." :"':'.:":".': 4'1.2'221 3/22009009m.'.' '.:r ;"'" .
4 4/23/2009 .~:~, 1 .: ..*..,'_
- "'" .. 42.5 42.5 180 180 00 373650 373650 0.0 0.0 3028.023 3028.023 -3028.0
*3028.0 58918.1 58918.1 8416.9 8416.9 4*24/2009 . 5151 180 180 -8.5
'8.5 453041 453041 Total Total Volume Volume (sct)
(sct) 89508.3 89508.3
. 4125/2009 5151 180 180 00 453041 453041 0.0 0.0 1609.053 1609.053 -1609.1
*1609.1 Days Days 1212 4/26/2009 . so50 175 175 1 443953 443953 9088.9 9088.9 9088.9 9088.9 Average Average Volume/day Volwme/day 7459.029 7459.029 4/27/2009 49.5 49.5 177.5 177.5 0.5 0.5 439824 439624 4128.2 4128.2 4128.2 4128.2 Avg Avg 77 day day rolling rolling total total 59110.4 59110.4 K .* 4/28/2009 : 4848 177.5 177.5 1.5 1.5 427134 427134 12690.4 12690.4 12690.4 12690.4 Max Max77dayday rolling rolling total total 71358.6 71358.6 4/2912009 4545 180 180 33 399113 399113 28021.5 28021.5 2832.895 2832.895 25188.6 25188.6 Max 1 Day Drop Max 1 Day Drop (in) (in) 33 19 19 -, 4/30/2009 44 44 180 t80 11 389100 389100 10012.5 10012.5 10012.5 10012.5 Avg 1I Day Avg Day Drop Drop (in)
(in) 0.833333 0.833333 5/112009 43.5 43.5 180 180 0.5 0.5 384025 384()25 5075.0 5075.0 5075.0 S()75.0 64574.5 64574.5 9224.9 9224.9 5/2/2009 4343 180 180 0.5 0.5 378850 378850 5175.0 5175.0 5175.0 5175.0 71358.6 71358.6 10194.1 10194.1 5/3/2009 ' 4343 180 180 00 378850 378850 0.0 0.0 662.758 662.758 -662.8
*662.8 61606.9 61606.9 8801.0 8801.0 5/4/2009: 42.5 42.5 180 180 0.5 0.5 373650 373650 5200.0 5200.0 5200.0 5200.0 62678.7 62678.7 8954.1 8954.1 5/5/20091- : : 42 42 180 t80 0.5 0.5 368363 36B363 5287.5 5287.5 853.416 853.416 4434.1 4434.1 54422.4 54422.4 m4.6 7774.6 5/612009.. 41 41 180 180 11 357575 357575 10787.5 10787.5 10787.8 10787.5 40021.3 40021.3 5717.3 5717.3
' 5f7/2009, 52 52 180 180 -11
*11 461274 461274 - - Total Total Volume (sct)(sct) 75052.3 75052.3 5/8/2009* 52 52 180 180 0 00 461274 461274 0.0 0.0 0.0 0.0 Days Days 11 11 912009 52 180 461274 0.0 0.0 Average Volume/day 6822.936 52 180 0 461274 0.0 0.0 Average Volumelday 6822.936 5/1020 51 180 180 1 453041 453041 8232.5 8232.5 8232.5 8232.5 Avg 7 day Avg day rolling rolling tolal total 57294.1 51 511*/112*09 51 51 180 180 00 453041 453041 0.0 0.0 1319.546 1319.546 -1319.5
*1319.5 Max 77 day rolling Max total rolling lolal 68139.3 68139.3 S /2009,50 50 180 180 11 443705 443705 9336.3 9336.3 2740.365 2740.365 6596.0 6596.0 Max 11 Day Max Day Drop Drop (in)
(in) 3 20 20 . 513/2009 49.5 180 0.5 439699 4006.0 760.747 3245.3 Avg 11 Day Drop (in) 49.5 180 0.5 439699 4006.0 760.747 3245.3 Avg (in) 0.618182 0.818182 5/14/2009 48 48 180 180 1.5 427012 12687,2 12687.2 12687.2 12687.2 29441.4 29441.4 4205.9 4Z05.9
- 5. /1,5/2009 45 45 180 180 3 399113 27899.4 27899.4 27899.4 57340.8 57340.8 8191.5 8191.5 6/200 : 44 44 180 180 11 389100 10012.5 10012.5 10012.5 67353.3 67353.3 9621.9 9621.9
. /17/2009 43.5 43.5 180 180 0.5 0,5 384025 5075.0 5075.0 5075.0 5075.0 64195.8 64195.8 9170.8 5/18/2009-. 43 43 180 0.5 0.5 378850 378650 5175.0 2551.027 2551.027 2624.0 2624.0 68139.3 68139.3 9734.2 5/191/209.: 51.5 180 -8.5 457187
'5/1912009, .**.*.:.'r.:.*.. 51.5 180 *8.5 457187 Total Volume (sel)
Total (sct) 80916.0 512012009' 5/20/200§ ;;, :'.:, 51 51 180 180 0.5 0.5 453041 453041 4146.0 473.398 3672.6 Days Days 13 13
.5/21/200
, .... ,:. 5121/2009,*,.:*, ,":~." ' 505 50.5 180 180 0.5 0.5 448&36 448836 4205.3 4205.3 4205,3 4205.3 Average Volume/day Average Volume/day 6224.308 6224.308 5/2i22009-.
'S/22l2009 . :*:*" .'i';:*: 50 50 180 180 0.5 0.5 443705 443705 5131.0 5131.0 5131.0 Avg 7 dayday rolling rolling total 50080.3 50080.3 5/2312009.-. 50 185 0 443458 247.4 247.4 Max 77 day day rolling total 62720.3 512312009 ,: 50 185 0 443458 247.4 247.4 Max rolling lotal 62720.3 5124/2009;:.:: .
512412009 48 48 1B5 185 22 426768 426768 16689.8 16689.8 16689.8 16689.8 Max 1 Day Drop (in) 33 21 S 5/252009
.. si2512009':: 45 185 185 3 398919 27849.2 27849.2 Avg 11 Day Drop Drop (in)
(in) 0.692308 0.692308 21 56/20 44.5 185 0.5 393994 4925.0
, 512612009 .",.' .,'.",' 44.S 185 0.5 393994 4925.0 4925.0 4925.0 62720.3 8960.0 8960.0 5/27/2009-:;."., .,'..
. '. 5/27/2009 44.5 44.5 185 185 0 0 393994 393994 0.0 0.0 0.0 0.0 59047.7 59047.7 8435.4 8435.4 58/29*129"
'512812009' 44.5 44.5 185 185 0 0 393994 393994 0.0 0.0 0.0 54842.4 54842.4 7834.6 7834.6 r '-
?/2912~::,.
i5/20099 - 30/209. _~;:' l' :/:.. 44.5 44.5 44 185 185 00 393994 393994 0.0 0.0 49711.4 7101.6 7101.6 44 190 190 0.5 0.5 388800 388800 5193.8 5193.8 5193.8 54657.7 54657.7 7808.2 7808.2 513012!)cJ9:::.- """'if '"
... 5/31/2009* 43 5131/2009',' ,.'.. 43 190 190 11 378600 378600 10200.0 10200.0 1705.966 1705.966 8494.0 46461.9 6637.4 6637.4 6/1/2009,1.
611/2009:[:': . . 42.5 42.5 200 200 0.5 0.5 373150 373150 5450.0 5450.0 942.057 942.057 4507.9 4507.9 23120.7 23120.7 3303.0 3303.0
- /2.12009:: ,'"- 52 180 -9.5 461274 Total 52 180 *9.5 461274 TOlal Volume Volume (scf)
(sci) 89811.1 89811.1 6/3/2009 52 52 180 180 0a 461274 461274 0.0 0.0 0.0 0.0 Days Is 15 9./4*/,09 52 52 180 180 0a 461274 461274 0.0 0.0 1611.599 1611.599 -1611.6
*1611.6 Average Average Volume/day 5987.407 5987.407 6/5/2009 . , *, 51 51 180 180 11 453041 453041 8232.5 8232.5 8232.5 Avg 77 day rolling 10taltotal 49382.9 49382.9
-,6/2009 ,, 51 175 0 453394 -352.2 -352.2 Max,7dayrollngroral 67418.4 51 175 0 453394 *352.2 ,352.2 Max 7 day rolling total 67418.4 6/7/2009 . s50 50 175 175 11 443953 443953 9441.1 9441.1 1421.638 1421.638 8019.4 8019.4 Max1 Max 1 Day Drop Drop (in) 4
.68/2009 "o., .. s-50 175 0 443953 0.0 0.0 Avg 50 175 0 443953 0.0 0.0 Avg 11 Day Day Drop (in)
Drop (in) 0.7 0.7 i9*62009 ,, 49.5 175 0.5 439950 4003.0 4003.0 18291.2 2613.0 22 = /10/2009: 49.5 175 0.5 439950 4003.0 4003.0 18291.2 2613.0 22 49 175 0.5 435848 4101.5 4101.5 22392.7 3199.0 6- /11/2009.4 49 175 0.5 435848 4101.5 4101.5 22392.7 3199.0 48 175 1 427256 8592.1 8592.1 32596.4 4656.6 48 175 1 427256 8592.1 8592.1 32596.4 4656.6
-. 6/12/2009. : 44 44 175 175 44 389250 389250 38006.0 38006.0 38006.0 38006.0 62369.8 62369.8 8910.0 8910.0 6/13/2009 44 44 180 180 00 389100 389100 150.0 150.0 150.0 150.0 62872.0 62872.0 8981.7 8981.7 6/14/209 43.5 43.5 180 180 0,5 0.5 384025 384025 5075.0 5075.0 1420,055 1420.055 3654.9 3654.9 58507.5 8358.2 58507.5 8358.2 6/15/2005- 43 43 180 0.5 378850 5175.0 5175.0 5175.0 63682.5 9097.5 180 0.5 378850 5175.0 63682.5 9097.5 6/16/2009 43 185 0 378725 125.0 3488.587 -3363.6 56315.9 8045.1 6/-17/209 43 41.5 185 165 0 378725 125.0 3488.587 *3363.6 56315.9 8045.1 1.5 362863 15862.5 658.508 15204.0 67418.4 9631.2 41.5 185 1.5 362863 15862.5 658.508 15204.0 67418.4 9631.2
' 8/18/2009:, 51.5 180 -10 457187 Total 611812009" ... '. ,,': '. 51.5 180 *10 457187 Total Volume Volume (scf)
(sct) 72206.6 72206.6 6I19i2oos'** . 6/19/2009
/i2/2009'
.612012009 .
51.5 51.5 51 180 180 180 00 457187 457187 0.0 0.0 0.0 0.0 Days Days 1I. 11. 51 180 0.5 0.5 453041 453041 4146.0 4146.0 4146.0 4146.0 Average Average Volume/day Volume/day 8564.235 6564.235 6/21/2009. 50.5 185 0.5 448506 4535.5 4535.5 Avg 6!21i2009 .. 50.5 185 0.5 448506 4535.5 4535.5 Avg 77 day day rolling rolling total tOlal 56080.9 56080.9
/22/2009 50 185 0.5 4434S8 23 6I22I2009!, ,' " .
..6/23/2009".: 50 185 0.5 443458 5048.3 5048.3 5048.3 5048.3 Max Max 77 day day rolling rolling total total 63525.1 63525.1
. 612312009.: ..,. 49.5 185 0.5 439449 4009.0 1230.836 2778.2 Max 23 49.5 185 0.5 439449 4009.0 1230.836 2n8.2 Max 11 Day Day Drop Drop (in)
(in) 33 6/24/2009: 612412009:,*' ',,' " 49 185 0.5 435344 4104.4 4104,4 49 185 0.5 435344 4104.4 4104.4 Avg I1Day Avg Day Drop Drop (in) (in) 0.727273 0.727273
. 6/25/2009 612512009:, 47.5 47.5 185 185 1.5 1.5 422377 4223n 12966.9 12966.9 12966.9 12966.9 33579.3 33579.3 4797.0 4797.0 6/26/2009":I'-= 44.5 44.5 185 185 33 393994 393994 28383.5 28383.5 28383.5 28383.5 61962.8 8851.8
&2612009>.. ::. 61962.8 8851.8
.. *6/27l2licJg'
/27/2009 . 44 44 185 185 0.5 0.5 388950 388950 5043.8 5043.8 5043.8 5043.8 62860.6 62860.6 8980.1 8980.1
.., .6/28/2009;
. 612812009" ,:.,- 43.5 43.5 150 190 0.5 0.5 383750 383750 5200.0 5200.0 5200.0 5200.0 63525.1 63525.1 9075.0 9075.0 6/29/2009:
612912009". ,:~. 43.5 43.5 190 190 00 383750 383750 0.0 0.0 0.0 58476.9 8353.8 0.0 58476.9 8353.8 6/30/2009,: 53 190 -9.5 468366 Total
", " 613012009:'.' 53 190 *9.5 468366 Total Volume Volume (scf)(sct) 76599.2 76599.2
'. .., -.. ,..7/1/2009 7/112009*' 53 53 175 175 00 469721 -1354.9
*1354.9 2174.873 -3529.8 Days 469721 2174.873 *3529.8 Days 10
.' ,,"... 7/0/2009p..... *
*'71'212009' 52 175 1I 461674 8047.0 2169.927 5877.0 Average 52 175 461674 8047.0 2169.927 5877.0 AverageVolume/day Volumelday 7659.919 7659.919
- '" . ll:3l2009!' .7/3/2009'. 51.5 175 0.5 457563 4110.9 1879.083 2231.8
/2009 51.5 51 175 0.5 457563 4110.9 1879.083 2231.8 Avg Avg 77day rOIling total day rolling total 65699.9 65699.9 24
.. *.".*7i4l20 7/5/2(009-99::, ... ; ,
51 50 175 175 175 0.5 0.5 1 453394 453394 443953 4169.1 4169.1 9441.1 1229.588 4169.1 4169.1 8211.5 Max 7 day rolling totaj Max 7 day rolling total Max I Day 72020.1 72020.1 24 .71512009; . . ' '. 50 175 1 443953 9441.1 1229.598 8211.5 Drop Max 1 Day Drop (in) (in) 3.5 3.5 71/62009 48.5 177.5 1.5 431432 12521.0 12521.0 Avg 71612009:.- .:.:;. 48.5 177.5 1.5 431432 12521.0 12521.0 Avg11 DayDayDrop Drop (in)(in) 1 7M2009 , 45 180 3.5 399113 32319.1 32319.1 61799.7 8328.5
- ,:~7e}~:':.",.
'.7J8/2009...
45 45 45 180 175 175 3.5 00 399113 399306 32319.1
-193.8
*193.8 1324.171 32319.1
-1517.9 61799.7 63811.5 8828.5 9115.9 399306 1324.171 *1517.9 63811.5 9115.9
*7/9/2009 71912009: . 44 44 175 175 1 389250 389250 100S6.3 10056.3 2822.490 2822.490 7233.8 7233.8 65168.3 65168.3 9309.8 9309.8
'. 7/10/2009 7I1oi2009::" 43 43 180 180 11 378850 378850 10400.0 10400.0 1316.352 1316.352 9083.6 9063.6 72020.1 72020.1 10288.6 10288.6 7/11/209" : 52.5 182.5 -9.5 465089 -Total Volume (ac) 103863.1 7/1112009 '., 52.5 182.5 *9.5 465089 Total Volume (sct) 103863.1
'7i1212009: '. :'.... 57/12/2009 2 182.5 0.5 461074 4014.5 4014.5 Days 20 52 182.5 0.5 461074 4014.5 4014.5 Days 20 7/13/2009* - . 52 185 00 460874 199.8
~~~!~:::
199.8 Average 7114/2009;.. 52 185 460874 199.8 199.8 Average Volume/day Volumelday 5193.156 5193.156
" 51t5 185 0.5 456812 4062.3 4062.3 Avg 51.5 185 0.5 456812 4062.3 4062.3 AVg 77day day rolling rollingtotal 10tal 40964.0 40964.0 Page Page44of019 9
Calculation PM-0375 Calculation PM-0:i75 Attachment Attachment"II -- Computation Computation of of System Leakage (ECR System Leakage 09-00416) (ECR 09-00416) 77 day day Leakage Leakage Estimate Estimate 7/15/2009. 1 51 51 185 t85 0.5 0.5 452689 452689 4122.8 4122.8 4122.8 4122.8 Max Max 77 day day rolling rotling total 62217.0 62217.0
-7/12/2009 51 51 187.5 187.5 00 452513 452513 176.1 176.1 176.1 176.1 Max Max 1 Day Day Drop (in)(in) 4 50 50 190 190 11 443210 443210 9303.0 9303.0 9303.0 9303.0 Avg I1 Day Avg Day Drop Drop (in)
(in) 0.575 0.575 07/12009
' 46 46 190 190 44 408225 408225 34985.3 34985.3 1039.893 1039.893 33945.4 33945.4 55823.7 55823.7 7974.8 7974.8 0711929,. 45.5 45.5 190 190 0.5 0.5 403550 403550 4675.0 4675.0 756.286 756.286 3918.7 3918.7 55728.0 55728.0 7961.1 7961.1 25 . " . -. 7/2 W720/2009
;/2009.i:i!':. :* 45 45 190 190 0.5 0.5 398725 398725 4825.0 4825.0 4825.0 4825.0 60353.2 60353.2 8621.9 8621.9
-71242009 25 44.5 44.5 190 190 0.5 0.5 393825 393825 4900.0 4900.0 4900.0 4900.0 61190.9 61190.9 8741.6 8741.6
.-:.::7/24/2009 *:": :,;:' 44 44 190 190 0.5 0.5 388800 386800 5025.0 5025.0 5025.0 5025.0 62093.1 62093.1 8870.4 8870.4 44 44 200 200 00 388500 368500 300.0 300.0 300.0 300.0 62217.0 62217.0 8888.1 8688.1 43.5 200 0.5 383475 5025.0 5025.0 5025.0 57939.1 57939.1 8277.0 8277.0
.: 7/25"20 9, l'..i
! ; :,- : :. 43.5 200 0.5 383475 5025.0 43.5 43.5 200 200 0a 383475 383475 0.0 0.0 0.0 0.0 23993.7 23993.7 3427.7 3427.7 43.5 43.5 200 200 00 383475 383475 0.0 0.0 0.0 0.0 20075.0 20075.0 2867.9 2867.9 43.5 43.5 200 200 00 383475 383475 0.0 0.0 0.0 0.0 15250.0 15250.0 2178.6 2178.6
.. . .7/28/200 .9.. ..- ,::
.! -7/29/2009 :".:i",* 42.5 42.5 210 210 1 372900 372900 10575.0 10575.0 1412.868 1412.868 9162.1 9162.1 19512.1 19512.1 2787.4 2787.4 7:.
- .;/30/200.i;'b: 41.5 41.5 210 210 1 362300 362300 10600.0 10600.0 10600.0 10600.0 25087.1 25087.1 3583.9 3583.9 7/,::::*31/2009i::.. .:: 41 41 210 210 0.5 0.5 356900 356900 5400.0 5400.0 54O0.0 5400.0 30187.1 30187.1 4312.4 4312.4 41 41 215 215 00 356788 356788 112.5 112.5 1228.965 1228.965 -1116.5
-1116.5 24045.7 24045.7 3435.1
', -:. /1/2009;.
2/2(009 :* 8./::,:;:"" :. L'F
- ;¢*!:*: 52.5 52.5 175 175 -11.5
-115 465726 465728 52 175 0.5 461674 4052.6 1130.294 26 52 175 0.5 461674 4052.8 1130.294 2922.3 2922.3 26 8'3/2009 51,5 175 0.5 457563 4110.9
. 6/4/2009.
- o ::i::i! =i::i; 51.5 175 0.5 457563 4110.9 4110.9 4110.9 51.5 51.5 175 175 00 457563 457563 0.0 0.0 0.0 0.0 Average Average 6774.8 6774.8 Max Max 46394.2 46394.2 Using Using Leakage Leakage == 80,422 80,422 Summary (7 Days Summary (7 Days of of leakage) leakage) Total Tolal N2 N2 required required == 320,000 320.000 (200,000 (200,000 for forCAD, CAD, 39,578.215 39,578.215 for for SGIG, SGIG, 80,421.6 80.421.6 Leakage)
Leakage) Total Volume (scf) 2,135,135 Total Volume (sci) 2.135.135 Total Days 337 CAD Total Days 337 CAD++SGIG SGIG Average Volume/day (tot/day) 6,336 Using Average Volume/day (tot/day) 6.336 USing 38"38' N2 N2 == 322,000 322.000 (322,000 (322,000 at at250psig) 250psig) Average Volume/day (avgd ind) 6,453 Required Average Volume/day (avgd ind) 6.453 Required CAD CAD ++ SGIG SGIG AmOunt= Amount= 320,000 320,000 0.62% 0.62% Avg 7 day rolling total 53,498 Margin Avg 7 day rolling total 53,498 Margi~..above aboveavgavg(38')= (38:~ 28,924 28,924 8.98% 8.98% Max 7 day rollingtotal 74.917 Margin ab" Max 7 day rolling total 74917 **.*{*'*Margih above ove Max(38'ýý= Max*(38')'=: 7,505., : .'2.33/* 7,505 ..** ....
.'2.3:ij.;>:' .. -.
Using Using38.5" 38.5' N2N2== 327,800 327,800 SCF SCF atat250 250psigpsig Required Required CAD CAD ++ SGIG SGIG Amnount= Amount= 320,000 320,000 2.38% 2.38% Margin Margin above above avg (38.5')= avgt38.5) (38.5')= 34,724 34,724 10.59% 10.59'10 Ma'*tn above Max = 13,305M-v 4.'06%'), - .' ~ ',,'
- Maraln.above Max i38.5:i= 13305',; 4.'o6%', :.
SGIG SGrGOnlyOnly Using Using 22" 22'N2N2== 124,000 124.000 SCP SCFatat250250psigpsig Required SGIG Required SGIGamount amount(scf)(set)== 120,000 120.000 3.23% 3.23'10 Margin above avg (scf) Margin above avg (set)== 30,924 30,924 24.94% 24.94%
* ,,-;,.'.MMara;;' aboVeMaxscf) argin abov Max'tsCfl='* 91505 9505 - . '7.67%."
'7.67%.:':'
Page Page5 5of019 9
Calculation PM-0375 Attachment IIII-- Computation Computation of System (ECR 09-00416) System Leakage (EGR Containment Makeup Makeup 3 132.8336 0.2 1 0. t4 t "-T 3 896.318 132.8336 9.019 1553,217 34792.060 1228.670 0.28 0.36 3 0.08 551.581 132.3673 8.760 956.579 21427.369 756.700 1 0.3 0.4 3 0.1 689.476 132.51719 8.843 1195.421 26777.429 945.636 0.29 [ 0.35 2
- .: 2 1 :.
0.06 413.685 131.19139 131.i04139 8.106 718.863 16102.525 16106.615 568.655 1 0.29 0.35 0.06 413.685 8.023 719.045 568.800 029 0.4 2 0.11 758.423 130.5913 .773 1319.255 29551.322 1043.595 0.3 0.4 3 0.1 689.476 1 131.39291 328.218 1 1197.696 1 26828.387 947.436 1 0.29 0.45 2. 0.16 1103.161 130.8914 327.940 1917.941 42981.888 1517.185 0.3 0.4 3 0.1 689.476 132.83361 329.019 1194.782 26763.123 945.131 0.29 0.4 3 0.11 758.423 132.23391 328.686 1315,593 29469.276 1040.698 0.28 0.42 3 0.14 965.266 131.97599 328.542 1675.121 37522.709 1325.102 0.28 0.33 3 0.05 344.738 131.0181 328.010 599.228 13422.709 474.018 0.28 0.35 3 0.07 482.633 131.168 328.093 838.706 18787.023 663.457 0.26 0.34 3 0.08 551.581 130.8682 327.927 959.008 21481.788 758.622 0.27 0.33 3 0.06 413.685 130.86821 327.927 719.256 16111.341 568.967 0.27 0.45 3 0.18 1241.056 130.7346 327.853 2158.257 48344.966 1707.286 0.25 0.33 3 0.08 551.581 130.4185 327.677 959.740 21498.167 759.201 0.3 0.53 2 0.23 1585.794 119.63999 321.689 2810.613 62957,737 2223.332 0.27 0.35 3 0.08 551.581 130.62701 327.793 959.400 21490.570 758.932 0.3 0.45 2 0.15 1034.214 133.27501 329.264 1790.839 40114.786 1416.640 0.3 0.48 2 . 0.18 1241.056 132.82501 329.014 2150.639 48174.320 1701.260 0.26 0.41 3 0.15 1034.214 129.4603 327.145 1802.440 40374.654 1425.817 0.26 0.35 .22 0.09 620.528 132.9916 329.106 1075.017 24080.386 850.391 0.28. 0.37 3 0.09 620.528 129.4603 327.145 1081.464 24224.793 855.490 0.33 0.41 3 0.08 551.581 129.4603 327.145 961.301 21533.149 760.436 0.3 0.39 " 2 . 0.09 620.528 133.2917 329.273 1074.473 24068.194 849.960 1 0.29 0.4 3 0.11 758.423 130.05999 327.478 1320.445 29577.958 1044,536 4 0.29 0.5 -2 0.21 1447.899 133.2917 329.273 2507.104 56159.119 1983.241 0.27 0.35 3 0.08 551.581 130.05999 327.478 960.323 21511.242 759.662 0.47 0.49 3 0.02 137.895 132.29231 328.718 239.175 5357.521 189.199 1" 0.28 0.45 3 0.17 1172.109 132.3089 328.727 2032.931 45537.654 1608.147 0.31 0.46 2- 0.15 1034.214 134.1918 329.773 1788.073 40052.829 1414.452 0.26 0.6 3 0.34 2344.217 132.3089 328.727 4065.862 91075,308 3216.294 0.25 0.4 2 0.15 1034.214 134.175 329.764 1788.123 40053.963 .1414.492 0.3 0.49 2. 0.19 1310.004 134.1918 329.773 2264.892 50733.584 1791.640 0.27 0.44 3 0.17 1172.109 132.30889 328.727 2032.931 45537.655 1608.147 0.3 0.35 .2, 0.05 344.738 133.74169 329.523 596.477 13361.075 471.842 0.27 0.35 3 0.08 551.581 132.89201 329.051 955.732 21408.387 756.030 0.27 0.5 3 0.23 1585.794 132.7586 328.977 2748.347 61562.979 2174.076 0.3 0.4 2 0.1 689.476 133.89171 329.607 1192.651 26715.392 943.445 0.3 0.35 2 0.05 344,738 134.04179 329.690 596.175 13354.318 471.603 0.28 0.3 3 0.02 137.895 132.36729 328.760 239.145 5356.842 189.175 0.27 0.4 2 0.13 896.318 133.5917 329.440 1551.231 34747.581 1227.099 0.26 0.45 3 0.19 1310.004 132.36729 328.760 2271.875 50890.003 1797.164 0 0.27 0.44 3 0.17 1172.109 132.6087 328.894 2031.901 45514.593 1607.333 0.3 0.46 2 .. : 0.16 1103.161 134.1918 329.773 1907.278 42723.018 1508.749 0.27 0.43 3 0.16 1103.161 132.6087 328.894 1912.378 42837.264 1512.784 0.28 0.4 3 0.12 827.371 132.1589 328.644 1435.374 32152.377 1135.450 0.28 0.4 3 0.12 827.371 132.66709 328.926 1434.142 32124.780 1134.476 0 0.29 0.35 3 0.06 413.685 132.36729 328.760 717.434 16070.527 567.525 0 0.27 0.29 2: 0.02 137.895 134.34179 329.857 238.349 5339.028 188.546 0.28 0.39 3 0.11 758.423 132.36729 328.760 1315.296 29462.633 1040.463 0 0.29 0.43 .2 0.14 965.266 134.34179 329.857 1668.446 37373.197 1319.822 0.27 0.33 3 0.06 413.685 132.45881 328.810 717.323 16068.042 567.438 0.28 0.33 3 0.05 344.738 132.817 329.009 597.408 13381.937 472.579 0.28 0.39 3 0.11 758.423 132.30891 328.727 1315.426 29465.540 1040.566 0.3 0.39 2.. . 0.09 620.528 135.692 330.607 1070.139 23971.115 846.532 Page Page 66 of of9 9
PM-0375 Attachment IIII-* Computation of System Leakage (ECR 09-00416) Calculation PM*0375 Containment Containment Makeup 1/15/09 22:00 1/15/09 22:00 0.28 0.4 0.4 3 0.12 827.371 132.30891 328.727 1435.010 1435.010 32144.226 32144.226 1135.163 1135.163 1/16/09 1/16/09 1 :00 1:00 0.27 0.27 0.51 .... 2.
- 2. 0.24 1654.742 135.3169 135.3169 330.398 2855.504 63963.290 63963.290 2258.842 2258.842 18:00 1/24/09 18:00 0.27 0.27 0.41 .2:2> 0.14 965.266 135.692 135.692 330.607 1664.661 1664.661 37288.401 37288.401 1316.827 1316.827 1/25/09 5:00 1/25/09 0.28 0.4 . 2::
2 0.12 827.371 827.371 135.39189 135.39189 330.440 330.440 1427.572 1427.572 319n.613 31977.613 1129.279 1129.279 1/26/09 1/26/09 9:00 0.27 0.4
.. . 2**
- 2. .. 0.13 896.318 135.3169 135.3169 330.398 330.398 1546.731 1546.731 34646.782 1223.540 1223.540 2/4109 10:00 2/4/09 0.27 0.42 3 0.15 1034.214 131.40931 131.40931 328.227
.328,227 1796.494 40241.463 1421.114 1421.114
- c. 2. :..
219/09 10:00 0.27 0.45 .. 2 0.18 1241.056 1241.056 132.54159 132.54159 326.656 328.856 2151.669 48197.366 48197.386 1702.075 2/16/09 18:00 0.28 0.4 3 0.12 0.12 627.371 827.371 133.3583 133.3583 329.310 329.310 1432.470 32087.319 1133.153 1133.153 2121/093:00 2/21/09 3:00 0.28 0.45 3 0.17 1172.109 1172.109 134.10789 329.727 2026.769 2026.769 45399.624 1603.273 1603,273 2121/09 2/21/09 4:00 0.29 0.43 ......... 2::** 2: ..... 0.14 965.266 130.125 327.514 1680.380 37640.522 1329.263 1329.263 2124/09 2/24/09 11:00
- 00 0.28 0.47 3 0.19 1310.004 134.1079 329.727 2265.212 50740.756 50740.756 1791.893 1791.893 3/3/09 12:00 0.26 0.52 0.52 3 0.26 1792.637 134.01629 134.01629 329.676 3100.243 69445.437 2452.442 3/3/09 23:00 23:00 0.28 0.4 0.4 2 0.12 627.371 827.371 130.59129 130.59129 327.773 327,773 1439.186 1439.188 32237.806 32237.806 1138.467 1138.467 3/9/09 22:00 0.27 0.4 0.4 2' 2 0.13 696.316 896.318 130.59131 327.773 1559.120 1559.120 34924.269 34924.289 1233.340 1233.340 3/10/09 9:00 3/10/099:00 0.26 0.35 ..**.. 2 ..* 0.09 620.528 130.74129 130.74129 327.856 1079.116 1079.116 24172.209 853.634
.c 3/12/09 4:00 3/12109 0.27 0.48 22. 0.21 1447.699 1447.899 130.5913 130.5913 327.773 327,773 2518.579 56416.160 1992.318 1992.318 3/12/09 6:00 3/12109 0.27 0.4 0.4 3 0.13 896.318 896.318 133.1168 133.1168 329.176 1552.475 1552.475 34775.431 1228.083 3/13/09 1 1:00
- 00 0.28 0.36 2 0.08 551.561 551.581 130.2913
. 130.2913 327.606 327.606 959.947 21502.804 759.364 3/16/09 13:00 3/16/09 0.29 0.29 0.42 3 0.13 896.318 896.318 133.11679 133.11679 329.176 . 1552.475 1552.475 34775.431 1226.083 1228,083 3/20/09 7:00 0.28 0.28 0.44 3 0.16 .* 1103.161 1103.161 133.4166 133.4166 329.343 329.343 1909.772 1909.772 42778.885 1510.722 1510.722 312010913:00 3/20/09 13:00 0.29 0.44 . *:-:.**2:. 2 0.15 0.15 1034.214 1034.214 130.29131 130.29131 327.606 327,606 1799.900 1799.900 40317.757 1423.608 1423.808 3/21/098:00 3/21/09 8:00 0.27 0.35 3 0.08 0.08 551.581 132.9669 132.9669 329.093 329.093 955.611 21405.680 21405.680 755.934 3/21/0911 3/21/09 :00 11:00 0.29 0.44 . 2*::.
2 0.15 1034.214 1034,214 129.97501 129.97501 327.431 327,431 1800.866 1800.866 40339.394 1424.572 1424.572 3/21/09 15:00 3/21/09 0.26 0.38 3 0.12 0.12 827.371 132.9669 132.9669 329.093 329.093 1433.416 1433.416 32108.521 32108.521 1133.902 1133.902 3123/09 21 :00 3/23/09 21:00 0.26 0.3 3 0.04 275.790 132.6087 328.894 478.094 478.094 10709.316 378.196 3/24/09 6:00 3/24109 0.25 0.3 3 0.05 344.738 344.738 132.47531 328.820 597.753 597.753 13389.662 472.851 3/25/09 3:00 3/25109 0.29 0.35 3 0.06 0.06 413.685 132.81699 132.81699 329.009 329.009 716.889 716.889 16058.324 567.094 567.094 3/30/099:00 3/30/09 9:00 0.29 0.45 0.45 .2..2 0.16 1103.161 1103.161 129.3912 327.106 1922.828 1922.828 43071.352 1521.050 1521.050 3/30/09 23:00 3/30109 0.26 0.26 0.36 0.36 2.1 2 0.1 689.476 129.3912 129.3912 327.106 1201.768 1201.768 26919.595 26919.595 950.657 3/31/09 9:00 3/31/099:00 0.29 0.29 0.4 3 0.11 758.423 758.423 133.05851 133.05851 329.144 1313.762 1313.762 29428.259 29428.259 1039,249 1039.249 4/2/09 0:00 4/21090:00 0.43 0.5 2 0.07 482.633 129.69119 129.69119 327.273 840.809 840.809 18834.121 665.121 4/4/09 22:00 4/4109 0.29 0.5 2.
- 2. 0.21 1447.899 130.114129 130.14129 327.523 2520.501 56459.223 1993.839 1993.839 4/8/09 14:00 0.28 0.35 0.35 3 0.07, 0.07. 482.633 482.633 133.1168 133.1168 329.176 329.176 835.948 18725.232 18725.232 661.275 4/9/092:00 0.28 0.45 0.45 3 0.17 1172.109 133.1168 133.1168 329.176 2030.159 45475.563 1605.954 4/9/09 5:00 4/9/095:00 0.28 0.28 0.37 0.37 .. 22 - 0.09 620.528 129.9913 327.440 327.440 1080.490 1080.490 24202.968 .854.720
'.854.720 4/11/09 21:00 4/11/0921 :00 0.25 0.25 0.34 0.34 3 0.09 620.528 133.26671 133.26671 329.259 329.259 1074.518 1074.518 24069.209 849.996 849.996 4/11/09 23:00 4/11/0923:00 0.26 0.5 :2 1 0.24 1654.742 129.075 129.075 326.931 326.931 2885,792 2865.792 64641.743 2282.802 "2282.602 4/12/09 6:00 4/121096:00 0.26 0.34 0.34 3 0.08 551.581 133.5665 133.5665 329.426 954.644 21384.035 21364.035 755.170 755.170 4/13/092:00 0.26 0.36 3 0.1 689.476 689.476 133.1168 133.1168 329.176 1194.211 1194.211 26750.331 944.679 944.679 4/13/09 4113/09 10:00 0.29 0.47 :. 2 0.18 1241.056 129.67501 129.67501 327.264 327.264 2162.140 48431.926 1710.357 1710.357 4/15/0923:00 4115109 23:00 0.27 0.45 3 0.18 1241.056 133.1168 133.1168 329.176 329.176 2149.580 2149.580 48150.596 1700.422 1700.422 4/16/09 1111:00
;00 0.29 0.44 0.44 2..
2.: 0.15 1034.214 1034.214 129.3912 129.3912 327.106 327.106 1802.651 40379.393 1425.985 1425.985 4/23/09 4123/09 23:00 0.28 0.45 3 0.17 0.17 1172.109 1172.109 133.35829 133.35829 329.310 2029.332 2029.332 45457.036 1605.300 1605.300 4/23/09 4123/09 16:00 0.28 0.43 22"" 0.15 0.15 1034.214 130.74129 130.74129 327.856 1798.527 40287.015 1422.723 1422.723 4/24/09 4124/09 11:00 11 :00 0.27 0.37 3 0.1 689.476 689.476 133.2667 133.2667 329.259 329.259 1193.909 1193.909 26743.565 26743.565 944.440 944.440 4/25/09 4125109 9:00 0.28 0.35 2
- 2. am 0,07 482.633 482.633 130.1413 130.1413 327.523 327.523 840.167 840.167 18819.741 18619.741 664.613 664.613 4129/09 6:00 4/29/09 6;00 0.27 0.33 3 0.06 413.685 134.61589 134.61589 330.009 714.718 714.718 16009.694 16009.694 565.377 565.377 4/29/09 9:00 4129/09 9;00 0.29 0.4 N 2 , 0.11 758.423 131.1914 131.1914 328.106 1317.915 1317.915 29521.295 29521.295 1042.535 1042.535 4/29/09 10:00 0.27 0.4 3 0.13 896.318 134.61589 134.61589 330.009 1548.557 1548.557 34687.670 34687.670 1224.983 1224.983 5/3/09 23:00 0.43 0.5 2 0.07 0.Q7 482,633 482.633 131.79149 131.79149 328.440 837.822 18767.209 16767.209 662.758 662.758 5/5/09 1:00 5/5/091:00 0.4 0.49 . '*2' 2" 0.09 620.528 130.8914 130.8914 327.940 1078.842 1078.842 24166.062 24166.062 853.416 853.416 5/11/09 0:00 5/11/090:00 0.27 0.41 33 0.14 0.14 965.266 134.46599 134.46599 329.926 329.926 1668.097 1668.097 37365.381 37365.381 1319.546 1319.546 5/11/09 2:00 5/11/092:00 0.28 0.45 . 22 0.17 1172.109 131.4914 131.4914 328.273 328.273 2035.744 2035.744 45600.655 45600.655 1610.372 1610.372 5/12/09 15:00 5/12109 0.26 0.41 33 0.15 0.15 1034.214 134.1662 134.1662 329.759 329.759 1788.150 1788.150 40054.557 40054.557 1414.513 1414.513 5/12/09 23:00 5112109 0.28 0.42 22 0.14 965.266 965.266 131.64149 131.64149 328.356 328.356 1676.069 1676.069 37543.945 37543.945 1325.852 1325.852 5/13/09 6:00 0.29 0.37 3 0.08 0.08 551.581 551.581 129.2193 129.2193 327.011 327.011 961.695 961.695 21541.965 21541.965 760.747 760.747 5/18/09 10:00 5/18/0910:00 0.29 0.42 0.42 22 0.13 0.13 896.318 896.318 131.64148 131.64148 328.356 328.356 1556.350 1556.350 34862,235 34862.235 1231.148 1231.148 5/18/09 22:00 0.26 0.4 3 0.14 965.266 965.266 134.31609 134.31609 329.842 329842 1668.519 1668.519 37374.815 37374.815 1319.879 1319.879 5/19/09 2:00 5/19/092:00 0.32 0.33 0.33 . 2 0.01 0.Q1 68.948 131.7915 131.7915 328.440 328.440 119.689 119.689 2681.030 2681.030 94.680 94.680 5/19/09 7:00 7:00 0.33 0.37 0.37 22 . 0.04 275.790 275.790 131.7915 131.7915 328.440 328.440 478.755 478.755 10724.119 10724.119 378.719 378.719 5/31/09 23:00 5/31/0923:00 0.29 0.47 0.47 22 0.18 0.18 1241.056 1241.056 131.1914 131.1914 328.106 328.106 2156.588 2156.588 48307.573 48307.573 1705.966 1705.966 6/1/09 3:00 6111093:00 0.32 0.42 0.42 3 0.1 689.476 689.476 134.76581 134.76581 330.092 330.092 1190.897 1190.897 26676.090 26676.090 942.057 942.057 6/4/09 15:00 0.28 0.45 0.45 - 2 0.17 1172.109 1172.109 131.0414 131.0414 328.023 328.023 2037.295 2037.295 45635.410 45635.410 1611.599 1611.599 6/7/09 7:00 6171097:00 0.29 0.44 2 0.15 0.15 1034.214 131.1914 131.1914 328.106 328.106 1797.157 1797.157 40256.311 40256.311 1421,638 1421.638 6/14/09 11 :00 6/14/09 11:00 0.28 0.33 2 0.05 344.738 131.84999 131.84999 328.472 328.472 598.385 598.385 13403.823 13403.823 473.352 473.352 6/14/09 23:00 0.29 0.39 0.39 . 2' 2 0.1 0.1 689.476 689.476 131.84999 131.84999 328.472 328.472 1196.770 1196.770 26807,646 26807.646 946.703 946.703 Page Page 7 of9 of 9
Calculation Calculation PM-0375 AttachmentAttachment 11- Computation of 11- Computation (ECR 09-00416) of System Leakage (ECR 09-0041 6) Containment Makeup Containment Makeup 6/16/09 0:00 6116/09 0.26 0.38 3 0.12 827.371 827.371 136.05701 136.05701 330.809 330.809 1425.977 1425.977 31941.894 1128.017 1128.017 6/16/09 6:00 0.29 0.4 2, :. 2'. 0.11 758.423 131.64151 131.64151 328.356 328,356 1316.911 1316.911 29498.813 29498.813 1041.741 6/16/09 16:00 0.3 .0.34
.0.34 2 0.04 275.790 131 .641 51 131.64151 328.356 328.356 478.877 478.877 10726.841 10726.841 378.815 378.815 6/16/09 18:00 0.28 0.38 3 0.1 0.1 689.476 689.476 136.05701 136.05701 330.809 330.809 1188.315 1188.315 26618.245 940.014 940.014 6/17/09 13:00 0.25 0.32 0.32 3 0.Q7 0.07 482.633 135.60719 135.60719 330.560 330.560 832.449 18646.858 18646.858 658.508 658.508 6/23/09 9:00 0.3 0.43 0.43 2 " ..
2- ' 0.13 896.318 328.440 131.7915 1328.440 1555.955 1555.955 34853.388 34853.388 1230.836 1230.836 6/30/09 22:00 6/30/09 0.29 0.52 0.52 .2' 2 0.23 1585.794 132.54161 328.856 2749.355 2749.355 61585.547 2174.873 2174.873 7/2/09 712109 11:00 11 :00 0.28 0.28 0.38 33 0.1 689.476 135.45731 135.45731 330.476 1189.513 1189.513 26645.080 26645.080 940.962 7/2/09 22:00 71210922:00 0.29 0.29 0.42 2 2.. ' 0.13 0.13 896.318 132.69159 132.69159 328.940 1553.589 34800.405 34800.405 1228.965 1228.965 7/3/09 23:00 7/3/0923:00 0.28 0.48 3 0.2 1378.951 1378.951 136.35679 136.35679 330.976 2375.433 2375.433 53209.702 53209.702 1879.083 1879.083 7/5/09 11:00 11 :00 0.3 0.4-3 0.43 2 '.. 0.13 0.13 896.318 132.3916 132.3916 328.773 1554.377 34818.046 34818.046 1229.588 1229.588 7/8/09 6:00 7181096:00 0.29 0.43 ". 2.'
- 2. 0.14 965.266 132.3916 132.3916 328.773 1673.944 37496.357 37496.357 1324.171 1324.171 7/9/09 1:00 7/9/091:00 0.26 0.26 0.39 3 0.13 896.318 896.318 136.71 459 136.71459 331.175 331.175 1543.105 34565.547 34565.547 1220.671 1220.671 7/9/09 14:00 0.27 0.27 0.38 3 0.11 758.423 758.423 136.71 459 136.71459 331.175 1305.704 29247.771 29247.771 1032.875 1032.875 7/9/09 23:00 7/9/0923:00 0.3 0.36 ::
- 2, 2." 0.06 413.685 413.6B5 130.8914 130.8914 327.940 327.940 719.228 719.22B 16110.708 16110.70B 568.944 7/10/09 4:00 7/101094:00 0.27 0.41 33 0.14 965.266 135.90709 135.90709 330.726 330.726 1664.059 1664.059 37274.928 1316.352 1316.352 7/18/09-23:00 7/1810923:00 0.31 0.42 :. '2.'*
2., 0.11 758.423 132.6916 132.6916 328.940 32B.940 1314.576 1314.576 29446.496 1039.893 7/19/09 9:00 0.32 0.32 0.4 "
.2'
.2- . 0.08 551.581 551.581 132.69162 132.69162 328.940 328,940 956.055 21415.633 756.286 7/28/09 10:00 7/2810910:00 0.28 0.28 0.43 3 0.15 1034.214 1034.214 134.85761 134.85761 330.143 330.143 1786.069 1786.069 4007.954 40007.954 1412.868 1412.868 7/31/09 23:00 7/31/0923:00 0.28 0.28 0.41 . 2 . 0.13 896.318 896.31B 132.6916 132.6916 328.940 328,940 1553.589 34800.404 1228.965 1228.965 8/1/09 8:00 10.28 811/098:00 0,28 0.4 3 0.12 827.371 134.8576 134.8576 1330.143 330.143 1428.856 1428.856 32006.364 1130.294 1130.294 Total Usage = 165911.6 Usage =165911.6 Avg per day == 463.4 463.4 Average Average Fill Fill == 1144.2 1144.2 Page 88 of Page of9
Calculation PM-0375 AHachment Calculation Attachment II II *. Computation Computation of System Syslem Leakage (ECR (ECA 09-00416) 09*00416) Level and and Pressure Pressure 10 to N2 Conversion Table Table Pressure Pressure 170 170 172,5 172 175, 175I In.5 177.5 '180" 180" 182.5 185' 185 187,5 187.5 190, 190 192,5 192.5 195 195 197,5 197.5 200 202,5 202.5 205.' 205:". 207,5 207.5 210 212.5 212,5 215 215 217.5 217,5 220: 220 250 LeVel Level " .- ' ,,' ". ," ~ , ", ".. >', " ', ' ' ' ", , ,.... ,:' '
, 33 265700 26'5550 265550 265400 265250 265250 265100 264950: 264800,264650 264950 264800 264500 264350 264650: 264500 264200 264050 263900 263750 263600 263450 263300 263150 2~000, 264350 ,264200 263000 262850~62700 262850 262700 260900q 260900; 33,25268650268506 33.25 268650 268506 268363 268363 268219',268075 268219 268075 267931 26793~ '267788,267644 267788 267644 267500267500 267356 2672q267213 267069 266925 266781,266638 266494, 26~350 26678!;.266638 266494 266350 266206 266063 ~659,1,9 266206 ,266063 26577~" 264050 265919 265775 264050 271600 271463,271325 33.5 271600 271463,;:!71325'271 )138'211950 27111882 2711913270775 71050 270913 270F775 2706311 ?705oo 270363270225 270638:270500 270363 270225 270088 270688269950 269950 269813i269675 269538 2~9400 26981,3.269875 269538 269400 269,2!13:?~9125>2689882688sg:f'-
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