ML20129H792
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{{#Wiki_filter:/ 'm a J % Beatric Generating Plant 13007-1 o u _ _a_ M oi 14 y',,,( g,g ( i VGlD 1 i VCT GAS CONTROL AND RCS CHEMICAL ADDITION i FOR INFORMATION ONLY i 1.0 PURPOSE i This procedure provides instructions for. Volume Control Tank (VCT) gas control operations and for Reactor j Coolant System chemical addition. Instructions are i l included in the following sections: ? 4.1 Aligning VCT Hydrogen Purge - Normal Operation 4.2 Establishing A Nitrogen Blanket In The VCT i f 4.3 Transferring From A Nitrogen To A Hydrogen Atmosphere In The VCT l 4.4 Transferring From A Hydrogen To A Nitrogen Atmosphere In The VCT - Nitrogen Supplied From N2 l Supply Header f 4.5 Transferring From A Hydrogen To A Nitrogen Atmosphere In The -VCT - Nitrogen Supplied From The l d t GWPS t 4.6 0xygen or Ammonia Removal From VCT Gas Space 4.7 Reactor Coolant System Chemical Addition 2.0 PRECAUTIONS AND LIMITATIONS i 2.1 Do not smoke, strike sparks or allow open flames in the vicinity of hydrogen lines. 2.2 When a Reactor Coolant Pump is operating, maintain a ( minimum backpressure of 15 psig on the No. 1 seal by maintaining a pressure of at least 18 psig in the Volume Control Tank. ExplosivemixturesofoxykenandhdrogenintheVolume Control Tank satst be avoi ed at alf times. 2.3 The oxygen concentration must not exceed 5% by volume when + hydrogen is present. l 9611040044 960827 PDR FOIA KOHN95-218. PDR
~. PNX;EDunE NO. Revision PAGE No. VEGF 13007-1 2 2 of 14 ~ j i 2.4 The reactor coolant temperature sust be less than 180*F j when adding hydrazine. For oxygen scavenging, the reactor coolant temperature should be between 150*F and 180*F. 2.5 When adding hydrazine the Domineralizers should be bypassed and letdown flow diverted directly to the Volume Control Tank. 3.0 PREREQUISITES OR INITIAL CONDITIONS i A level is established in the VCT and makeup is 3.1 i available. l 3.2 The Gaseous Waste Processing System (GWPS) is available for wasta processing. 3.3 The Auxiliary Gas Systems - Nitrogen and Hydrogen - are i available to supply cover gas to the VCT. 3.4 The Nuclear Sampling Systems - Liquid and Gaseous - are available for sampling the VCT. 3.5 The Reactor Makeup Water System'is aligned to supply i water to the Chemical Mixing Tank. l 3.6 The Nuclear Sampling Panel 1-1215-P5-NSP has been aligned by the Chemistry Department. 4.O INSTRUCTIONS 5 4.1 ALIGNING VCT HYDROGEN PURGE - NORMAL OPERATION l CAUTION If the VCT oxygen concentration limit is approached, the. oxygen j content should be lowered per Subsection 4.6. i Non If a nitrogen atmosphere ( exists in the VCT, align the tank for hydrogen purge operation per Subsection 4.3. 4.1.1 REQUEST Chemistry to verify, by sample analysis, that the oxygen concentration in the VCT gas space is less than SI by volume. W l
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- nocs W ho.
navmon aos wo. 2 3 of 14 i .JP 13007-1 4 4.1.2 VERIFY that a hydrogen atmosphere exists in the VCT as 4 i follows: 1 VCT Hydrogen Manifold Isolation 1-1208-U4-107 is l a.. i -
- OPEN, 5
b. VCT Nitrogen Manifold Isolation 1-1208-U4-108 is i
- CLOSED, Wasta Gas Decay Shutdown Tank Supply To VCT, I
c. l-1208-U4-352, is CLOSED. i 4.1.3 ENSURE that VCT Hydrogen Regulator 1-PCV-8156 is set to a 18 psig or greater l 4.1.4 . ENSURE the Gaseous Wasta Processing System in operation, aligned to a Normal Gas Decay Tank, per 13201-1, " Gaseous Wasta Processing System". f 4.1.5 ENSURE that the VCT Purge Flow Controller 1-HIC-1094 is set at zero. i 4.1.6 OPEN the VCT TO GWPS ISO VLV l-PV-ll5. ( 4.1.7 ADJUST the VCT Purga Flow Controller 1-HIC-1094 to 0.7 scfm. 4.1.8 VERIFY that VCT pressure is 18 psig or greater on l-PI-Oll5. I '4.2 ESTABLISHING A NITROGEN BLANKET IN THE VCT I Mn This subsection should be used to establish a nitrogen blanket if the VCT has been opened to atmosphere. 4.2.1 CLOSE the VCT Hydrogen Manifold Isolation 1-1208-U4-107. VERIFY that VCT Nitrogen Regulator 1-PCV-8155 is set to < 4.2.2 15-20 psig. 4.2.3 OPEN the VCT Nitrogen Manifold Isolation 1-1208-U4-108. Independent Verification required. 4.2.4-REQUEST Chemistry to verify, by sample analysis, the VCT oxygen concentration. I'
PnocsouRE No. ngyeoN PAGE NO. VEGP 13007-1 2 4 of 14 4.2.5 If oxygen concentration is greater than 5%, PERFORM the following: CLOSE VCT NITROGEN MANIFOLD ISOLATION a. 1-1208-U4-108, b. REMOVE cap and OPEN GWPS Vent Header Sample Line Vent 1-1208-X4-374, CAUTION Do not exceed VCT pressure of 65 psig. START manual makeup to the VCT per 13009-1, "CVCS c. Reactor Makeup Control System", d. RAISE level in the VCT to t'5 - 100%, then STOP
- makeup, CLOSE GWPS Vent Header Sample Line Vent l
e. 1-1208-I4-374, 3 f. OPEN VCT NITROGEN MANIPOLD ISOLATION l-1208-U4-108, OPEN Chemical Volume Control System (CVCS) Drain g. VCT To Recycle Holdup Tank (RET) 1-1208-U4-123 and LOWER VCT level to 45 - 50% then CLOSE drain, h. REPEAT Sub-subsection 4.2.4 and 4.2.5 until the l VCT oxygen concentration is less than 5% by i
- volume, i.
VERIFT l-1208-U4-123 is CLOSED. Independent verification required, i j. VERIFT 1-1208-X4-374 is CLOSED and cap installed. j. Independent verification required. f 4.2.6 SET the VCT Nitrogen Regulator 1-PCV-8155 to at 18-20 psig, i PLACE the CVCS Reactor Makwup System in AUTO per 4.2.7 13009-1, "CVCS Reactor Makeup Control System". 4 I,
emocsouna no. Leviseow pasa no. VEGF 1300, --: 2 5 of 14 \\ 4.3 TRANSFERRING FROM A NITROGEN TO A HYDROGEN ATMOSPHERE IN THE VCT CAUTION If the VCT oxygen concentration limit is approached, the oxygen i content should be lowered per Subsection 4.6. NOTE This procedure should be performed in conjunction with unit heacup. t 4.3.1 ALIGN a Shutdown Gas Decay Tank (S/D GDT) to receive VCT purger If a S/D GDT is not in service, ALIGN the system a. per 13201-1, " Gaseous Waste Processing System", b. If the S/D GDT is in service supplying Unit 2, ALIGN the Unit 2 system to receive Unit 1 VCT purge p'er 13201-2, " Gaseous Waste Processing System. CAUTION VCT pressure must be maintained at greater than 18 psig to maintain adequate backpressure on Reactor Coolant Pump Seals. l 4.3.2 MONITOR VCT pressure indicated by 1-PI-115. If VCT pressure approaches 18 psig, CLOSE VCT TO a. GWPS ISO VLV l-PV-ll5, i l b. INCREASE the setpoint on the inservice VCT Nitrogen Regulator 1-PCV-8155 or A-PCV-7891 prior to re-establishing flow. s 4 4.3.3 OPEN the VCT TO GWPS ISO VLV 1-PV-115. ADJUSTtheVCTPurSeFlowController1-HIC-1094tolow of slightly 4.3.4 establish a purge. i { ', i <*eans
as no. emocsouna no.
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6 of 14 VEGF 13007-1 I 4.3.5 RAISE VCT level to approximately 951 as follows: If Reactor Coolant System heacup is in progress, a. ALLOW the reactor coolant expansion to raise the VCT level by placing Letdown To VCT or Holdup Tank J Valve 1-LV-ll2A in the VCT position, b. If Reactor Coolant System heatup is not in progress, PLACE Letdown To VCT or Holdup Tank Valve 1-LV-ll2A in the VCT position and RAISE level in the VCT by operation of the Reactor Makeup Control System in MANUAL per 13009-1, "CVCS Reactor Makeup Control System". When VCT level reaches approximately 95i,, STOP makeup 4.3.6-to the VCT if applicable and PLACE l-LV-ll2A to the Holdup Tank (HUT) position to lower level, and ESTABLISH a hydrogen supply to the VCT as follows: ) ENSURE that VCT Hydrogen Regulator 1-PCV-8156 is a. set to at least 18 psig, b. OPEN the VCT Hydrogen Manifold Isolation 1-1208-U4-107: independent verification required, CLOSE the VCT Nitrogen Manifold. Isolation c. 1-1208-U4-108: independent verification required, h
- d. -
CLOSE the VCT Waste Gas Decay Shutdown Tanks l Supply To VCT 1-1208-U4-352: independent verification required. ' LOWER the VCT level to 30 - 50% while maintaining a 4.3.7 cover gas pressure of at least 18 psig as indicated on 1-PI-115. j 4.3.8 RAISE the VCT level to 95% as follows: If RCS heatup is in progress, ALLOW the RCS a. expansion to raise level by placing 1-LV-112A to the VCT position, b. If RCS heatup is not in progress, PLACE l-LV-ll2A ( to the VCT position and RAIRE level 13009-1, "CVCS Reactor Makeup Control System"per i 4.3.9 When VCT level reachats 951, STOP Reactor Makeup System if applicable, and PLACE l-LV-112A to the HUT position. J 4.3.10 LOWER VCT level to 30 - 50% while maintaining a cover gas pressure of 18 psig as indicated on 1-PI-il5. i- .4.3.11 REQUEST Chemistry-to sample the VCT gas space.
woocsouns wo. navn:ow 7aas wo. VEGP 13007-1 1 7 of 14 a 4.3.12 REPEAT'Sub-subsections 4.3.8 through 4.3.10 if necessary, until the VCT gas concentration is in specification. 4.3.13 ESTABLISH normal VCT level ands a. PLACE 1-LV-ll2A in AUTO, b. PLACE CVCS Reactor Makeup Control System in AUTO per 13009-1, "CVCS Reactor Makeup control System". 4.3.14 ALIGN the Gaseous Waste Processing System for operation using a Normal Gas Deca 7 ank per 13201-1, " Gaseous T Waste Processing System'. 4.4 TRANSFERRING FROM A HYDROGEN TO A NITROGEN ATMOSPHERE IN THE VCT - NITROGEN SUPPLIED FROM N2 SUPPLY HEADER NOTE This subsection should be used if VCT nitrogen purge gas cannot be supplied from the Shutdown Gas Decay Tank. 4.4.1 ALIGN a Shutdown Gas Decay Tank (S/D GDT) to receive VCT purge as follows: a. 'If a S/D GDT is not in service, ALIGN the system per 13201-1, " Gaseous Waste Processing System", b. If the S/D GDT is in service supplying Unit 2, ALIGN the Unit 2 system to receive Unit i VCT purge p'er 13201-2, " Gaseous Waste Processing 1 i System. j 1 4.4.2 ADJUST VCT Purge Flow Controller 1-HIC-1094 to raise the hydrogen purge flow to the Gaseous Waste Processing System to slightly less than 1.2 scfm. i 4.4.3 ENSURE that VCT Nitrogen Regulator 1-PCV-8155 is set to 18-20 psig. ( 4.4.4 OPEN the VCT Nitrogen Manifold Isolation 1-1208-U4-108. Independent verification required. e i 4.4.5 CLOSE the VCT Hydrogen Manifold Isolation 1-1208-U4-107. Independent verification required. 4.4.6 VERIFY that the VCT pressure is being maintained at f 18 psig or greater as indicated by 1-PI-115. l l 1 l 5
& AGE NO. PRoCsount No. newslON VEGP 13007-1 2 8 of 14 i i* j NorE l Continue the purge flow through the VCT until sample analyses indicate the hydrogen l concentration in the reaccor i coolant has been decreased to less than 5 cc/kg. { l 4.4.7. When the Reactor Coolant System hydrogen concentration is below 5cc/Kg, DISCONTINUE the purge flow through the i VCT as follows: d ADJUST VCT Purge Flow Controller 1-HIC-1094 for i a. zero flow, b. CLOSE the VCT TO GWPS ISO VLV l-PV-115. 4.4.8 If required, ALIGN the Gaseous Waste Processing System for operation using a Normal Gas Decay Tank,_otherwise SHUT DOWN the system per 13201-1, " Gaseous Waste Processing System". 4.5 TRANSFERRING FR W A HYDROGEN TO A NITROGEN ATMOSPHERE IN THE VCT - NITROGEN SUPPLIED FROM THE GWPS NOTE This procedure should be performed in conjunction with unit'cooldowns when the VCT nitrogen purge gas is being supplied from the GWPS. 4.5.1 ALIGN a Shutdown Gas Decay Tank to receive VCT purge as follows: If a S/D GDT is not in service, ALIGN the system a. per 13201-1, " Gaseous Waste Processing", b. If the S/D GDT is is service supplying Unit 2 ALIGN the Unit 2 system to receive Unit i VCT 4 13201-2, " Gaseous Waste Processing gurgeqer ystem 4.5.2 ADJUST l-HIC-1094 to raise the hydrogen purge flow to . the Gaseous Waste Processing System to slightly less than 1.2 scfm. 4.5.3 ' ENSURE that Shutdown Gas Decay Tank to VCT Regulator A-PCV-7891 is-set to 18-20 psig.
enocsouns wo. navision Pen No. VEGP 13007-1 2. 9 of 14 4.5.4 OPEN the GWPS ISO N2 PURGE FROM WASTE DECAY S/D TK TO VCT A-1902-U4-128. Independent verification required. ~ 4.5.5 OPEN the CVCS VCT WGD S/D TANKS SUPPLY TO VCT 1-1208-U4-352. Independent verification required. 4.5.6 CLOSE the VCT Hydrogen Manifold Isolation 1-1208-U4-107. Independent verification required. 4.5.7 VERIFY that the VCT pressure is being maintained at 18 psig as indicated on 1-PI-ll5. i l NOTE Continue the purge flow through the VCT until sample analyses indicate j the hydrogen concentration in the reactor coolant has been lowered to less than 5 cc/kg. 4.5.8 When the Reactor Coolant System hydrogen concentration is below 5 cc/Kg, DISCONTINUE the purge flow through the VCT as follows: a. ADJUST VCT Purge Flow Controller 1-HIC-1094 for zero flow, b. CLOSE the VCT TO GWPS ISO VLV l-PV-Il5. 4.5.9 ALIGN the nitrogen supply regulator to the VCT and discontinue the purge from the Shutdown Gas Decay Tank i as follows: l a. ENSURE that the VCT Nitrogen Regulator 1-PCV-8155 is set to 18-20 psig, l b. OPEN the VCT Nitrogen Manifold Isolation l l-1208-U4-108. Independent verification required, CLOSE the CVCS VCT WGD S/D TANKS SUPPLY TO VCT c. l-1208-U4-352. Independent verification required,< d. If not required for Unit 2 operations, CLOSE the GWPS ISO N2 PURGE FROM WASTE DECAY S/D TK TO VCT Isolation Valve, A-1902-U4-128. Independent Verification required. t s m
pnocsouna No. neymon pass no. VEGP 13007-1 2 10 of 14 4.5.10 VERIFN'thattheVCTpressureisbeingmaintainedat 18-20 psig as indicated on 1-PI-115. 4.5.11 If required, ALIGN the Gaseous Wasta Processing System for operation using a Normal Gas Decay Tank, otherwise shutdown the system per 13201-1, " Gaseous Waste Processing System". 4.6 OXYGEN OR AMMONIA REMOVAL FROM VCT GAS SPACE CAUTION If the Shutdown Gas Decay, Tanks are being used as the purge supply for the Unit 2 VCT, shift purge supply to the nitrogen regulator per 13007-2, VCT Gas Control And RCS Chemical Addition", prior to performing this procedure. 4.6.1 ENSURE the following valves are CLOSED: a. GWPS VCT WCD S/D TANKS SUPPLY TO VCT 1-1208-U4-352, b. GWPS VCT WGD S/D TANKS SUPPLY TO VCT 2-1208-U4-352, l c. GWPS ISO N2 PURGE FROM WASTE DECAY S/D TK TO VCT l Isolation Valve A-1902-U4-128. 4.6.2 ALIGN a Shutdown Gas Decay Tank to receive VCT purge as f follows: a. If a S/D GDT is not is service, ALIGN the system l per 13201-1, " Gaseous Waste Processing System", i b. If the S/D GDT is in service supplying Unit 2, ALIGN the system to receive Unit 1 purge per 1 13201-2, " Gaseous Waste Processing". 1 4.6.3 ENSURE that VCT Nitrogen Regulator 1-PCV-8155 is set to 18-20psig. 4.6.4 ENSURE the VCT Nitrogen Manifold Isolation 1-1208-U4-108 is OPEN. 4.6.5 ENSURE that VCT Purge Flow Controller 1-RIC-1094 is set for zero flow. i
~ maa no. emocsouns mo. newsson VEGP-13007-1 2. 11 of m i CAUTION ~ VCT pressure must be greater than 18 psig to maintain adequate backpressure on Reactor Coolant Pump Seals. i 1 l 4.6.6 MONITOR VCT pressure indicated by 1-PI-115. If VCT pressure ap is, CLOSE the VCT ToGWPSIsolationhroaches^18 a. alve 1-FV-1 b. RAISE the setpoint on VCT Nitrogen Regulator 4 l PCV-8155 prior to re-establishing flow. i 4 f 4.6.7 OPEN the following valves: VCT To GWPS Isolation. Valve,1-PV-Il5, a. i b. VCT Purge Flow Controller 1-HIC-1094 to establish i a purge flow of slightly less than 1.2 scfm. 4.6.8 RAISE VCT level to 90 - 95% as follows: PLACE Letdown to VCT or Holdup Tank Valve, LV-112A a. to the VCT position, b. RAISE level in the VCT by operation.of the Reactor s Makeup Control System in MANUAL per 4 13009-1, "CVCS Reactor Makeup Control System". CAUTION Do not allow VCT level to decrease below 30%. j 4.6.9 When VCT level reaches 90%, PLACE Letdown to VCT or Holdup Tank Valve 1-LV-112A to the HDT position to decrease level, and isolate the purge to the Gaseous Waste Processing System as follows: s I a. CLOSE the VCT 70 GWPS ISO VLY 1-PV-115, 4 b." Continue to divert water to the Recycle Holdup Tank until VCT level is 30 - 50%. 4.6.10 When VCT level reaches approximately 50%, PLACE Letdown t to VCT or Holdup Tank Valve 1-LV-Il2A to AUTO. 4'.6.11 REQUEST Chemistry to semple the VCT gas space.
I i Paoi:soune No. Lavision Pana no. VEGP 13007-1 2. 12 of 14 4 i CAUTION j Do not exceed a Shutuown Gas Decay Tank pressure of 80 psig. i l 4.6.12 REPEAT Sub-subsections 4.6.8 through 4.6.11, if necessary, until the VCT gas concentration is in 1 specification. l 4.6.13 If the Unit 2 VCT purge supply was transferred from j r Shutdown Gas Decay Tank to nitrogen regulator at the l beginning of this subsection, then PERFORM the following: REQUEST Chemistry to sample Shutdown Gas Decay i a. Tank and if acceptable for Unit 2 VCT purge j i
- supply, b.
TRANSFER the Unit 2 VCT purge s pl from nitrogen j regulator to Shutdown Gas Decay per 13007-2, "VCT Gas Control And RCS Chemical Addition". i 4.7 REACTOR COOLANT SYSTEM CHEMICAL ADDITION i NOTE 1 To ensure thorough mix at least one Reactor Coo t Pump should be in operation while chemicals are being l added to the system. i 4.7.1 ISOLATE the Chemical Mixing Tank by verifying the following valves are CLOSED: Chemical Mixing Tank Supply From EMWST a. l-1208-U4-176, a b. Chemical Mixing Tank Outlet Valve, 1-1208-U4-181. 4 CAUTION j When adding chemicals, a face ( shield, gloves and protective l clothing must be worn. Inhalation of, or skin contact with chemicals such as lithium j hydroxide or hydrazine should be avoided. 4.7.2 COORDINATE with Chemistry to add the chemicals to the j . Chemical Mixing Tank per 35110-C, " Chemistry Control of The Reactor Coolant System". d- } n a
PROCsDuns No. ngyeagow pagg wo, VEGP '3007-1 2 13 of 14 4 i ) CAUTION j Tank filling should be J performed slowly to prevent the overflow of chemicals from the tank vent. 1 j 4.7.3 OPEN Chemical Mixing Tank Supply From RMWST 1-1208-U4-176, approximately one eighth turn, to slowly i i fill the tank. 4.7.4 When water starts to flow out of the tank vent, CLOSE i Chemical Mixing Tank Vent 1-1208-U4-179. 4.7.5 Fully OPEN Chemical Mixing Tank Supply From RMWST 1-1208-U4-176. l l i CAUTION ) When adding hydrazine, the 4 Domineralizers should be bypassed and letdown flow i diverted directly to the VCT. q l 4.7.6 If adding hydrazine, PLACE Letdown to Domineralizer/VCT Valve 1-TV-0129 to the VCT position. j i 4.7.8 OPEN Chemical Mixing Tank Outlet Valve 1-1208-U4-181. l 4.7.9 ALLOW flow through the Chemical Mixing Tank for ten minutes, then ISOLATE and DEPRESSURIZE the tank as j follows: CLOSE Chemical Mixing Tank Outlet Valve l a. 1-1208U4-181. Independent verification required, l b. CLOSE Chemical Mixing Tank Inlet Valve i l-1208-U4176. Independent verification required, i Slowly OPEN Chemical Mixing Tank Outlet Drain l c. 1-1205-U4-180 and RELIEVE the tank pressure, then CLOSE the valve. 4 L .4.7.12 After ap1roximately one hour, REQUEST Chemistry to sample tse Reactor Coolant System and REPEAT the chemical addition if necessary. T i w -t--- e- - + +m
NRoCEDURE NO. REVISaoN PAGE NO. 2. 14 cf 14 VEGP 13007-1 r
5.0 REFERENCES
5.1 PROCEDURES 5.1.1 13006-1, "CVCS Startup And Nonnal Operation" 5.1.2 13009-1, "CVCS Reactor Makeup Control System" 5.1.3 13012-1, " Nuclear Sampling System - Liquid" 5.1.4 13013-1, " Nuclear Sampling System - Caseous" 5.1.5 13201-1, " Gaseous Waste Processing System" 5.1.6 13707-C, " Auxiliary Gas System - Nitrogen" 5.1.7 13708-C, " Auxiliary Gas System - Hydrogen" 5.1.8 13733-1, " Reactor Makeup Water System" 5.1.9 35110-C, " Chemistry Control Of The Reactor Coolant System" 5.1.10 13007-2, "VCT Gas Control And RCS Chemical Addition" 5.2 P&ID's 5.2.1
- IX4DB115, Chemical & Volume Control System 5.2.2 1X4DB116-1, Chemical & Volume Control System 5.2.3
- IX4DB128, Waste Processing System-Gas 5.2.4
- IX4DB129, Waste Processing System-Gas 5.2.5
- 1X4DB140, Nuclear Sa.pling System-Liquid 5.2.6
- LX4DB141, Nuclear Sampling System-Gaseous 5.3 Alvin W. Vogtle Units 1 & 2, Precautions Limitations and Setpoints Document for Nuclear Steam Supply Systems.
( END OF PROCEDURE TEXT 218
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...r~., ss CN-Ta-88-71 1., 1 leMen 2., Attachment to FR88/Cwas-460 d Boren Dilution Event Analysis acs Active volumes 3 eggsgs. The volumetrie units are cubic feet (ft ). RSA/IER (1) asm/xra car cas s&P SCP TBX TCX Segnant CEE ESDI TWP/TEP CCE CDs, =- _=- 4 4 4 4 4
====.=_===- 46750l4603.5 I A 3 1 3 4 4646.1 4678.0 4721 3 j B 3733.7 3733 7 3643.5-4678.0 (3)C 547.0 547.0 694.0 831 9 531 9 1019,9 019 9 831.9 421.9 i D 79.5 106.5 83.3 91.1 91 1 4 1 38L' 71.3 79.5 79.5 E 935.0 1080.3 973.6 1036 0 936.0 973 8 973.4 1936.0 935.0 F 133.8 138.9 135.5 137 7 137.7 .r130 5-130.5 139.3 139 3 8 78.6 78.6 86.0 78 6, 78.6 v86 0* 86.0 78.6 78 6 I 89.3 119.7 89.9 98.6 98.6 .r80.ga 80.8 53.8 82.8 313.3 313.3 313 3 313 3 313 3 313.3 313.3 313 3 313.3
_=-
.=_ :=
=
Total 4816.3 3013.9 4631.1 5611 4 5511.4 (239.1 8381.7 5555.5 5535.5 V2. L (1) Segment key # Res leeps a l A-g3417 l B = Reactor Vossal volume c - Upper head and guide tube volumes a g gje g / D = Not Img piping volume - i E - 5/G (Primary sideb volume .g p9g/g )jZ* F - Cressover Img pip W volume op 8-O = Reactor Coolant pump volume E - Cold Zag ing volume .p-x - C
=
,.1 The volume The total voluna is the sum of segments 3 and D through 2. (3) of segment C is subtracted. 9 a j o v ~M V A p
/ GeorgaPower A Inter:ffloo C:rrespond:nse DATE: April 18, 1988 .RE: Plant Vogtle - Units 1 & 2 Refueling O wage Meeting Minutes (April 14, 1988) FROM: J. F. D'Amico 10: J. B. Beasley 14, 1988 The biweekly Refueling Outage Meeting was held on Ttursday, April The following is a simum7 of topics discussed. at 11:00 AM. His handout Ron Bush, Engineering, discussed the Spent Fuel Rack Project. of project milestones, a list of involved schedzie (attached) incluces a Also sproved sche &zle for fuel rack installation. personnel and the currentincluded is the ps-:::d sM1e idtich was develop delay in delivery of racks number 7 and tamber 8. 18, 1988, contingency planning still allows for fuel receipt Wnning on July with at least four racks in the fuel pool. Indira Kochery, Health Physics, explained time requirement that all ..f~.cs of prior contractors arriving on-site nust provide acceptable, s yn at Vogtle Otherwise, occupational radiation exposure history. will be lind.ted to 1 Ram per quarter. l Elijah Dixon, Building and Grounds, presented his re~===1dations for Outage F1==4ne will take the lead Turbine Building Washdown (see ace =W). on determining feasibility and sMie restraints for this tInsk. l l Joe D'Amico stated that Chad. cal Clean-Up will take place at mid-loop and l will take 2 1/2 to 3 days. The first is Two lists of Surveillances were distributed to the attandees. l a list of those Surveillance Tasks which are currently planned for the first Itw second is a list of all the Surveillance Tasks which have The refueling outage. a late date prior to Jtzia 2,1990, (prior to the sected refueling outage). attendees'were asked to ccupare the two lists and identify miy items which should Please address consents to Iori Potts at be added to the first refueling outage. extension 4288 or Mercy Haase at extension 3164. Joe D'Amico presented a list of new activitias added to the outage schedule He stated that he intends to distribute a during the past week (attached). subsequent outage meetings for all activities a similar list atHe will add the estimated nonpower for each activity to this list last meeting. if it is deemed necessary. i Janes Sutphin, IEC, briefly described the IEC plan to identify PM's required i He plans to look at the PM's de due within l for the' first refueling outage. 21,1988. He i the next 12 nonths and expects to begin pr*ing results by April L anticipates ccupletion of this project by May 15, 1988. l ? J
{. j. i j0 .I J. B. Beasisy Refueling Outage Meeting Mimtes (April 14, 1988) April 18, 1988 ) 1 l Work Planning and Outage Planning will get together to develop a method to l prioritize the p=9=:4ng effort for FM and Corrective Work Orders. i Seven itens on the Resolution Item Tracking Lir.c (attached) were discussed i I as follows: Live load Packing Program - Ric Liaine said the DCP is currently Ikmber 7 at PfED.. The scope includes.yy dmately 10 BOP valves, many of which are in the condenser area. Questions will be resolved a and the package will be out of PPTO by April 28, 1988. ) Control Rod Wear Inspection - Don Williams said the package is N eber 26 currently held up by the Reactor h 4 % Supervisor. said he is Contairunant Spray Miniflow Concerns - Ric Blaine i N eber 40 aumiting a response tram PFIO on the RIGl. The resolution will imposing an adninistrative control on the duration of =*= 41 Formal resolutfrm expected by run during ESTAS testing. pump /88. l 5/15 Neber 67 Additional TGV Guidelines - Art M411 stated response is dae e back from PfE0 by 4/16/88. REll For Domin Valve 1418-U8-005 - Mark Biron said the REll Naber f-Number 70 would be available the afternoon of 4/14/88. {' Number 78 Turbine Building Bei Crane - Ric Blaine stated that two REA's with response anticipated within three have been sent to weeks. One REA is to upgrade the limit of the Unit I crane, the h the allowable period of time during which l: other is to dot both cranes may be on one side of the building. Determine Regulatory Committments - Terry Wendt said ce==nts e Humber 6 are &as back 4/22/88 on the letter to all departments reme-ting input. Items brought 19 & ring the open discussion portion of the meeting were: 4 If the AMSAC/ Core Drill can be performed within a six day window, the - question of control room pressurization will be satisfiad. Any Schedule information received in bid packages d=1d be inn =44mtaly forwarded to Marty Haase/ Wren Stevenson. An sr.cl.u-ing device will be required dring removal of the generator This will be added to the Resolutions Item Tr*+15 List. rotor. Bill Lankin/ John Qualizza need to know requirements for hydown areas L in containment as well as polar crane usage. l
_y l. I J. B. Beasley i Refueling Outage Meeting Minutes (April 14, 1988) 1 April-18, 1988 'ihe Breathing Air question has been resolved. 'Ihe skid unit (under a l-Top Mod) will be the primary source and service air (with filters) ~ will be the secondary source. Supervisors need to let their le know that up-to-date rufueling and ~ pre e ?=ga schedules are avai e ' for their use and <== wits. 'Ihe schehles are issued for the purmee of ating feed-back and information. Please let Outage ?lanning if you would like additional information, or the sane information in a different format. '1he next Refuel Outage Meeting is w+=A'1ed for April 28, 1988, at 11:00 A.M. in the Outage War i IAP/cjb 3 l Attachments xc: Attendees Refueling Outage Status Contacts 9 l i
AT11NDEE LISI j NAtE DEPARIMENT PIDE EKr. i 1. Wren Stevenson OEP 4470 2. Dinos Nicolaou OEP 3236 3. Don Deisley OEP 3205 4. Phillip L. Cupp OET 4212 5. Allen Cure HP 4474 6. Mark Biron HP 4362 7. Robert GLam Sec. 4111 8. Tony Prestifilippo Eng. 3869 9. Doug Akin Admin. 34 %
- 10. Daryl T. Glover Work Planning 4422
- 11. -Jerry Martin Work Planning 3577
- 12. ' Jerry Greenwood West (SSM) 4176
- 13. Michael Cortese OEP 4139
.14. T. B. Lunsford Materials 3950 15. Indira Fid sj h? 3229 -16. S. P. Green M*=wwe 3487
- 17. Tim Austin Training 3315
- 18. Art Caudill Eng. Suppt.
4124
- 19. Steve A. Phillips Maint.
3469
- 20. Dusty Rhodes OEP 3269
- 21. Jemifer Bates
.NPFSG 3595 22. S. Swanson OEP 3812 23. A. A. Sinuson Q.C. 3293
- 24. Darrell Barnett Maintenance 3190 25.
E. L. Kellun Maintenance 3481
- 26. Hank '!hampson Maintenance 3899
- 27. Terry Wendt NSAC 3178
- 28. Mike lackey WPG 4175
- 29. Tom MLmdy WPG 3860
- 30. John Qualizza OEP 3173
- 31. Ron Bush GPC 8-526-7159 32.
D. O. Williams Reactor Eng. 4144
- 33. Rick Barlow Operations 3497
- 34. David Seckinger Mr 3474
- 35. Jim Montgomery G.E. Co.
3513
- 36. Ric Blaine Eng. Support 3162
- 37. Joe Fehrenbach Unit 2 Sched.
1517
- 38. David McCary 0EPACSG 4142 3
- 39. Fred Warren OEPACSG 3919 l
- 40. Cronuell Stone OEPACSG 3450 41.
W. A. Iankin OEPACSG 4114 42. J. B. Beasley OEP 4209 43. M. R. Haase .OEP 3164 44. J. F. D'AmLco OEP 3139
- 45. Iori Potts OEP 4288 46.: S..Sammes Eng.
4346 . 47. E. Dimon BEC 3727
- 48. ~ James 93*ahin
.I&C 3181 4 ,w a
RERELING OUTAGE STARIS Q2fTACTS DEPARTMENT DEPAIUMENT CONTACT DCT. BEEPER i OtfrAGE PUdWING Tim Adams 3198 823-7564 1 Wren Stevenson 4470 1 Dusty Rhodes (BOP) 3269 828-9405 ) John Qualizza (NSSS) 3173 PSEWC Jerry Martin 3577 WSG Fred Page 4172 MAINIENANCE Steve Phillips 3469 I&C Mike Hobbs 3174 OPERATIONS Bill Burmeister 3286 HP Ken Petrosky 4018 alt. Allen cure 3871 CHEMISTRY Rich Tupper 4135 ENGINEERING Ric Blaine 3162 REACIOR ENG. Don Willima 4144 NPSFt; Jennifer Bates 3595 QC Rick Haitz 3293 NSAC Terry Wendt 3178 IRAINING Mike Kurtzman 3354 alt Russell Brown 3353 SECURITY Sid Walker 3514 AININ Doug Akin 34% - PROCURIMNT Terry Imsford 3950 233
-FUEL RACE PROJECT MILESTONES AUGUST 1987 -CONTRACT SIONED FOR 20 RACES FOR WEST POOL (CSI SERVICESs NOVEMBER 1987 -157 LICENSING SUBMITTAL (SEISMIC AND CRITICALLITY) JANUARY 1988 -2ND LICENSING SUBMITTAL (SN M LICENSE) APRIL 1988 -3RD LICENSTNG SUBMITTAL (FUEL POOL COOLING) JUNE 19888 -DELIVERY OF RACES 1 TRRU 8 JUNE 1988 -INSTALLATION OF RACES 1 TERU 8 NOV 1988 -DELIVERY OF RACES 9 TERU 20 1989 -INSTALLATION OF RACES 9 TERU 20
- CBI HAS SCHEDULED DELIVERY OF RACES 9 TERU 12 TEIS YEAR ALTIOUG CONTRACT ALLONS FOR INCREMENTAL SEIPMENT DATES OF SEPT 1988, APRIL 1989 AND NOV 1989.
4 m +
TUEL RACE PROJECT PRIMARY CONTACTS PROJECT MGR. RON BCSE GPC 8-526-7159 DESIGN ENGINEER ARTUR0 CORRAL BECHTEL 7757 i SYSTEM ENGINEER SPENCER SEMMES GPC 4346 EXPEDITER OMAR SMITH SCS 7666 i INSTALLER MIEE CAGLE PULLMAN 7430
- i LICENSING PEIL GRISSOM SCS 7774 CBI PROJ MGR.
DICE C0KWAY CBI 815-933-2200 ADDITIONAL CONTACTS NUCLIAR SAFETY EARRY MAJORS SCS 6495 NUCLEAR FUELS RON C0CEERELL SCS 7330 LICENSING J0EN BARTEA GPC 7113' TUEL BANDLING DON WILLIAMS WESTINGEOUSE 4144 MATERIALS ING . DAVE CARLSON BBCETEL 7170 FIELD INGINEER ED WILCOE SECETEL 7356 NUCLEAR ENG TJERI SURJANT0 SCS 7244 CIVIL ENG JOB EASSAS SICETEL 7247 CIVIL ING RAMESE BUA SCS 5839 INGINEERING MGR. BILL RAMSEY SCS 7916 LICENSING MGR. JIM SAILEY SCS 7912
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. -.. ~ i.* I TURBINE BUILDING WASHDOWN i i
Purpose:
To rid Turbine Building of accumulated dirt, debris and dust that can't be reached by any other methods. Method: Service Water - Starting at Level 5 and washing down to each lower floor. Time: 24 hours to wrap and waterproof electrical equipment and motors. 24 hours for actual washdown. 4 Work Plant Coordinate with Operations, Test Shop and Maintenance Shop as j to what equipment, supplies, etc., need to be waterproofed. l (wrapped with plastic and taped) l Work Force: 3 Electrical Personnel - 3 Test Shop Personnel. B&O will supply additional personnel to work wl.th these groups. i Safety Concerns: All non-essential electrical equipment to be de-energized. Notice posted for actual date of washdown, advising personnel of falling debris and water. A requirement of eye protection to be posted. 4 k I 4
..~.-.... .~. - -.. -.. -. - -. - -. - ~ l ,d/SP CONVEOSATIONAL MONITOR 5YSTED PAGE' l . FILE: MMI-APRIL A1 f NEW ACTIVIIIES ADDED DURING WK OF 4/G-4/12 I-I 724511101
- MAIN TUR8 SACR-UP OVERSPEED TEST & CHANNEL CAL 24 l
7245131U1 *THN A SAFETY FEATURES SEQUENCER U3001 CHAN CAL
- '24 I
724614101 *1RN B SAFE 1Y FEATURES SEQUENCER U3002 CHAM CAL 24 + 724616101 *TURS IMPULSE CHAMSER PRESSURE PROTEC1 1505 CAL 8 724618102 *TURS IMPULSE CHAMBER PRESSURE PROTECT P505 ACOT 4 r 724617101 *1DRS IMPULSE CHAMBER PRES 5URE PROTECT P504 CAL e ? 724617102 *TURS IMPULSE CHAMEER PRESSURE PROTECT P504 ACOT 8 724701101 *RCP 81 OVERCURRENT RELAYS 250/251M CHANNEL CAL 12 'I 724702101 'RCP 82 OVERCURRENT RELAYS 250/251M CHANNEL CAL 12 724703101'*RCP #3 OVERCURRENT RELAYS 250/251M CHANNEL CAL 12 724704101 *RCP #4 OVERCURRENT RELAYS 250/251M CHANNEL CAL 12 724706101 *RCP #1 GROUND PROYECTION RELAYS 250/251GM CAL 10 724707101 *RCP 82 GROUND PROTECTION RELAYS 250/251GM CAL 10 I 7247D8101 *RCP #3 GROUND PROTECTION RELAYS 250/251GM CAL 10 724709101 *RCP e4 GROUNO PROTECTION RELAYS 250/251GM CAL 10 724701101 *RCP #1 OVERCURRENT RELAYS 250/251M CHANNEL CAL 12 l 724702101 *RCP 82 OVERCURRENT RELAYS 250/251M CHANNEL CAL 12 -{ 724703101 *RCP a3 OVERCURRENT-RELAVE 250/251M CHANNEL CAL 12 l i 724704101 *RCP a4 OVERCURRENT RELAYS 250/251M CHANNEL CAL 12 724706101 *RCP,s1 GROUND PROTECTION RELAVS 250/251GM CAL 10 724707101 *RCP #2 GROUND PROTECTION RELAYS 250/251GM CAL' 10 l 724708101 *RCP a3 CMOUND PROTECTION RELAYS 250/251GM CAL 10 724709101 *RCP e4 GROUNO PROTECTION RELAYS 250/251GM CAL 10 755010101
- CONTAINMENT SPRAY SYSTEM LEAKAGE ASSESSMENT 4-i 4-755011101 *CVCS LEAKAGE ASSESSMENT l
4-755012101 *RHR SYSTEM LEAKAGE ASSESSMENT 755018101 *SI SYSTEM LEARAGE ASSESSMENT 4-724910181
- DELTA T/T AVG LOOP 1. CHAN I. T-411 CHANNEL CAL 34 -
i 724811101
- DELTA T/T AVG LOOP 2 CHAN II. T-421 CHANNEL CAL
- 34 -
i 724812301
- DELTA T/T AVG LOOP 3. CHAM III.kT-431 CHANNEL CAL
- 38 -
724813101
- DELTA T/T AVG LOOP 4. CHAN IV. T-441 CHANNEL CAL
- 35 -
724901101 *TRN A SAFETY FEATURES SEOUENCER U3001 RST 18 - 724902101 *TRN 8 SAFETY FEATURES SEOUENCER U3002 RST 18 - 72467S101
- REACTOR VESSEL LEVEL TRANSMITTER CALIBRATION 30 -
l 724538103 *RM COOLANT PRESSURE (MR) P-403 ACOT 4 724519103 *RM COOLANT PRESSURE (MR) P-405 ACOT 4-f 724831101 *RM TRIP & ESF LOGIC (PROCESS & PROTECTION) RST S-t 4-724839101 *RCP UNDERVOLTAGE RELAYS SENSOR RST 724520101 *RCS SUSCOOLING MARGIN MONITOR CALIBRATION 8-724539101
- PRES $uMIZER PRESSURE CONTROL P-455 CHANNEL CAL 8-754812101
- 2 CHANNEL RM TRIP SYS RESPONSE TIME SUISIATION 8-724910101
- PASS GASEOUS LEARAGE ASSESSMENT 12 -
728835101 *TRM A H2 RECOMBINER VISUAL INSPECT AND ELEC TEST
- 8-728835102 *TRM S H2 RECOMBINER VISUAL INSPECT AND ELEC TEST
- 8-l 728907102 RCP-2 13.SKV BMR OVERCURRENT PROTECTION TEST 4 -
4SOV BMR TYPE 42 GRP 2 DVERCURRENT PROTECT TEST 4 - 728909113 2-714700101 MANUAL REACTOR TRIP TEST 2-714910101 RCS LEAKAGE INSPECTION ..m
- GE:
1 RE50LGil09 ITE9 iPAC*ING DATE: 94't!'a! l -e OfE4
- itnS l
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- atit 1:'ll'97 04 31 i9
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- ETE*MINE SCOPE OF 90 VATS TESilNG FOR SCHEDULE !MPACT.
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- a!Nt 1:rgligt 35!01/00 /
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- Itt g
- 31 !? 05l31'00 DETERM!NE UN MRNATER INSPECTION REQUIREME4TS. ISSUE MATL. REG
- al'.'.!P S ENG; NEE *
- 31 17 94/15/00
! CONTROL R00 NEAR INSPECTION. 93400C TO PRI AFTER FUEL INT. PROC. di'.LI AnS
- 2t!8!aLS 12/01/87 05/01100 / / MATEPIAL DESERVATION. STASING. LOCATION
.JWSSFORO ESTABLISH INTERIR ACCESS PROSAM. AuAITING PROCDURE SIGN-OF
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- 5*
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- !!:..****.*!::'*!=?-
04 ICENT!FIED DUE RE50LvG sa: 1.*i!* 115:s!!: )C' ifATUS 10f4!!FfCTP!:0.J CEANE TO $98PGFT e0Pt Atilvli:li 05 EW.5*!NT '5-45:1S.
- G f: :: it ?! 11 89
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- 5 35 a
31/01 99 4! 81 90 . wi !N PE50LVE Cini SPRAf nlN! FLON CONCERNS NITH RO UCED FLON. UNIT 2 48 INi!v!!n 81/ :i98 94'!5/99 ' s K516N CHANGE TO REPAIR EllSilNG VALVES NITH LONER CV
- ,,rtiw #
0!4flFY *CEDUATE PONER SUP*LT FOR BREATH!NG AIR CORPPESSOR de
- tt 82/91399 M191/98 EM6tNEE8!NG TO EVALUATE UTILl!!N6 MCC AS PONER SOUPCE.
- . a:N '.!
3L 31'98 85 81/96 CONTINGENCf FRAGNET PREPMAT10N - EVALUATE IPPACT ON SCHGUL COMPLETE OPS 'REPMAil0N FOR OUTAGE USING SinULATOR TO SHMP
- P
- 5!*u:0=1 1 3 l:8 99 #S 81/90 / /
PLMT EVOLui10NS UNIOUE TO QUTA6E tilP0 REconMENDAi!DN) " -543 i 8 !:6'!9 95/81/88 1 / DETERMINE OUTAGE $NIFT SCHGULE I.E. M 'S. 2-10'S. 2-12'S. O MIC3 TH15 ACTIVli) REGUIRED TO RANLDAD ANI RESOURCE CONSTRAIN OUTAG 24 w5 82/26/80 5/01/II / / INVElflGATE POS$1BLlif 0F INCREASING RNP SIGN-lu LINES FOR : GE SPECIFIC RNP S AND PROBLER AREA RNP's TO REDUCE C8MEESTION a *wE8'
- ?
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- AUt!LL YES. ADDITIONAL ANALYS!$ NILL M E OUIRD. If NAS M EN KTERnl LANTMD TRANSOUCERS N!LL NOT M USD. SullELINES FROM R.K!E
PAGE: 3 RESOLUT10N ITEM i8ACrING Daft:84:!3;te OPE 4 liEM5 .nou.oooon ou n===.--.-oo no-on.onomu uu========= ===== u unn== =.na n um j !F1. CE!'CN!!6LE #515 MTE MTE BATE LEECP18T!0N 8!!3.f:C4 -!8 4fatsf' DR IMNTIFIED DUE RESOL's!L arc l 9.c.f E 5 !%!4!E8 10P iia dS f ' EAi= Su S!C5 'O SPOVICE E61*EE !% *.#EU : t.g 04,,EAS in!!L".!%. ti i M :* 19 ?! n* 18 d Eit EMI qtpl% To m ovlE Ev;LLafice, iPEC!FIC EVALLAf!0N u!LL eEGu!RE PP FE 'Es.ND T!*8 %[ *C E %!4Ei21Q. th!Tl ATE RER THAT NOULD PROV!DE FOR TECH i EC Cn4aH f4* acud 4 : 4 g up g 83 I?;!9 84'l'?98 Mu!N VALVE 1411 M NEN M ING 9 M I'd E N O ' IIRCN i i
- AINTENANCE to DEVELOP A DETAILED PLAN ON $NUBBER TESi!NG. IRIAT TY
?! P4 INT
- 3/17t99 95/01/99 s t
- HILI!PS iEN00P SUPPORT !! RES 0 7 NHAT TYPE OF TEST EQUIPMENT REB *D ? LOCA OPEFai!0NS MAS RESPONS!tLITY TO APPOINT A RETURN to SERV!CE C00Reis OPS 13/1T/88 85,01/98 i /
t!!CENS ClP ' 34'81,08 #5/01/98 / DR6AullE AND Aen!NISTER SONE FAMILIARl!Afl0N TRAINING ON Pi2 FDR $l$19 0 APICO SORS AhD FOREMEN. TRAIN THER 04 HON TO READ P/2 SCEDULES AN l !%! NEE # 4 $8/08/98 84/::198 i / MTERMINE TURIINE tu!LDINE MIDGE CRANE RESTRiti10NS. '.!!E I NNTIFY SPECIFit PENETRATION SEALING & CORE DRILL REeulREMENT o
- W!NEER 38!8813g
/ / / / ulTH AMSAC AND THE COMESPONDING INTERFACE dlTH CONTROL ROO I m@
4 t' i REPTELING OLTIAGE EETING AGENE FOR APRIL 28 1988 OUIAGE WAR Rom 1 i i 1. OPENING RENARKS 4 2. SNUBBER REDUCTION - 704 ARIDTIO 4 a 4 l 3. BREATHING AIR - MARK BIIG/m ADITENCAMPE \\ 4. IZAD SHIELDING UPDAIE - M AUITENCAMPE 5. GJrAGE WORKING HOURS .KE D'AMICO 6. TIRBINE BUILDING WASHD0544 FMIDW-UP - DUSTY RH00ES i 7. O NIAIN1ENI COATINGS - m N E 8. PIPING CLEANLINESS - M QUALIZZA/RIC EUG2E I 9. RES M IW IITM LIST i
- 10. OPEN DISCUSSIW l
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