ML20096F470
| ML20096F470 | |
| Person / Time | |
|---|---|
| Site: | 05200004 |
| Issue date: | 12/18/1995 |
| From: | Aubert C PAUL SCHERRER INSTITUTE |
| To: | |
| Shared Package | |
| ML20096F375 | List: |
| References | |
| ALPHA-528, NUDOCS 9601230404 | |
| Download: ML20096F470 (27) | |
Text
-
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PAUL SCHERRER ltiST1TITT E2f_
~
m Document No.
ALPHA-528 l
l Document Title j
PANDA Transient Tests M9 Integral System Test Procedure PSI internal Document 1
Revision Status Approval / Date
_ -PM G-PM G-SOR issue Date Remarks Rev.
Prepared / Revised by P
3 Mdb dTorbeck dM 8 7 '/f***'
Id I@I O
C. Aubert A9-tu-SE 15 Dec 95 st-2.h alt Aem-o.u e l
1 9601230404 960117
~
PDR ADOCK 05200004 A
Controlled Copy (CC) Dist.ribution List Note: Standard distribution (cf. next page) is non-controlled CC Holder CC List Entry Retum / Recall No.
Name, Affiliation Date Date 1
PANDA Betriebswarte date issued
Registnerung E!55
~
'" G PAUL SCHERRER INSTITUT 95-29 ALPHA-528-0 PANDA Transient Tests Erw2t Trel M9 Integral System Test Procedure Autxen/
Adahs CW
- 15. Dezember 1995 Abstract:
This report details the procedure for conducting PANDA Transient Tests M9 specified by GE document 25A5824 Rev.0.
All phases for PANDA operation during the preconditioning processes and the test are described.
t Verteiler Abt.
Empfinger/ Empf&ngerinnen Expl.
Abt.
Empfinger / En vii,p..-i Expl.
Expl.
42 G. Yadagaroglu 1
GE at PSI Bbliotnek G. Varadi 1
A. Arretz 1
C. Aubert 1
Reserve 5
T. Bandurski I
GE San Jose J. Dreier 1
J. Torbeck Total 20 O. Fischer 1
(for distribution at GE to 1
J. Healzer 1
J.R. Fitch, G.A. Wingate, Seiten 27 M. Huggenberger 1
B.S. Shiralkar, S. Lornperski 1
DRF No.T1000005)
Bedagen H.J. Strassberger 1
informatonsitste ALPHA-Dokumentation 2
0 1
2 3
4 5
8 9
A Betriebswane 1
Visum AbtAaboriettung:
ALPHA-528-0 ALPHA-528-0 Page 4 Page 4 PANDA Transient Tests i
M9 Integral System Test Procedure 00 introduction 01 Test Configuration and initial Cond:tions 10 Initial Alignment 11 Control System and DAS Setup 12 Valve Alignment 13 General Facility Configuraton Check 14 Prepare Automatic Heat Power Regulation 15 Auxiliary Water System Filling 16 Instrument / Zero Check 20 RPV Setup for Vessel Preconditioning 21 Water Filling 22 Heating / Purging 30 Suppression Chambers Setup 31 Water Filling 32 Gas Space Heating 33 Pressurization 40 GDCS Heating 41 Water Filling 42 Pressurization 50 PCC1 Pool Setup 51 Water Filling 60 PCC2 Pool Setup 61 Water Filling 70 PCC3 Pool Setup 71 Water Transfer from GDCS Tank 72 Water Filling 73 GDCS Pressurization 80 Drywells Setup 81 Gas Space Heating
ALPHA-528-0 ALPHA-528-0
-Page5 Page5 90 RPV Initial Conditions Setup for Test 91 Adjusting RPV Conditions 100 Test Conditions Setup 101 Adjusting SC Pools Conditions 102 Adjusting SC Gas Space Conditions 103 Adjusting GDCS Conditions 104 Adjusting DWs Conditions 105 Adjusting PCC1 Pool Conditions 106 Adjusting PCC2 Pool Conditions 107 Adjusting PCC3 Pool Conditions 110 Test 111 Data Recording 112 Adjusting RPV Conditions 113 Configuration Setup and Test initiation 120 End of Test 121 End of Data Recording 122 Facility Shut Down 200 Checklist l
l l
l 4
l l
l
ALPHA-528-0 ALPHA-528-0 Pige 6 Page 6 00 Introduction This procedure for Transient Test M9 describes all test phases including preconditioning processes. Assuming that the starting point for the preconditioning is an empty facihty at atmospheric conditions, this proceduro gives sequences of processes, which do not need to be strickly followed during the preconditioning process, at the discretion of Test Engineer. Required phases are listed in the Checklist and must be recorded when conducted.
The current procedure gives guidance on how to proceed to bring PANDA to the required initial test conditions for a extreme case (from a cold and empty facility). The order of preconditioning sequences rnay be modified if needed, and single phases may be adapted to the actual conditions. Heating power indicated in preconditioning phases is theoretical and considered as basis for time estimation. Due to PSI electrical power limitation or modification in preconditioning process, the heating power may be reduced, in any case, the foreseen preconditioning process is to start with the Suppression Chambers conditioning after the facility has been set ready for operation. It continues with the GDCS tank, all PCC pools and the Drywells. Just before test initiation, the RPV is set up to satisfy the required initial conditions. The test is then conducted under automatic power control and with specific operator actions at the beginning of the test in order to satisfy the test objectives. The test duration is 3 hours3.472222e-5 days <br />8.333333e-4 hours <br />4.960317e-6 weeks <br />1.1415e-6 months <br />.
A time estimation for the preconditioning of an empty and cold facility is given for each component in the following table.
Test Plan Specifications are described in the GE document 25A5824 REV.O.
Note; Since temperatures are given in Kelvin in the Test Plan Specification and in 'C in the PANDA DAS, they are indicated in both units in the current procedure.
- Idem for pressures which appear in kPa in the Test Plan Specification and in bar in the PANDA DAS; they are also indicated in two units in the current procedure.
- Key parameters or key actions are indicated in dark frames to make reading easier during PANDA operation.
Time Estimation time Phase Proconditioning Phases n'
10 Initial Alignment not estimated 20 RPV Setup for Vessel Preconditioning 1,6
[ hour]
30 Suppression Chambers Setup 12,8
[ hour]
40 GDCS Heating 2,4
[ hour) 50 PCC1 Pool Setup 2,0
[ hour]
60 PCC2 Pool Setup 2,0
[ hour]
70 PCC3 Pool Setup 2,1
[ hour) 80 Drywells Setup 1,3
[hourj 90 RPV Initial Conditions Setup for Test not estimated 100 Test Conditions Setup not estimated 110 Test 3,0
[ hour) 10 to 100 Duration for Preconditioning 24,2
[ hour]
10 to 120 Duration for the whole Test 27,2
[ hour]
NQ1g; Duration of phases n'10,90 & 100 cannot be estimated; it should not exceed a couple of hours.
ALPHA-528-0 ALPHA-528-0 Page 7 Page 7 01 Test Configuration and initial Conditions The configuration for the Transient Test M9 includes the RPV, Suppression Chambers, Drywells, GDCS, all PCC condensers and their respective pools; all pools will be isolated from each other. Since the IC is not lined up for M9, the IC pool will be isolated from the system.
The Equalization Lines connecting both Wetinells to the RPV are not part of the system and kept closed.
A detailed description of the required configuration is given in the Test Plan.
The initial conditions described in the above mentioned GE document are listed below with the respective tolerances.
M The current procedure is based on the values given in the following List.
Test initial Conditions List RPV (V.RP)
-Total Pressure MP.RP.1 =
319 [kPa) 4 [kPa]
- Mean Fluid Temperature Tp, n(RP) = I(MTF.RP.i)/ max (l) with i=1 to 5 Tp, n(RP) =
409 [K) 2 [K)
- Local Fluid Temperature MTF.RP.1.. 5 =
Tp_
n(RP) 2 [K]
3,50 [m]
0,20 [m]
Drvwell 1 and 2 (V.D1 - V.D2)
- Air Partial Pressure MPG.D1.1 =
0 [kPa]
2[kPa]
MPG.D2.1 =
0 [kPa]
2 [kPa]
- Mean Gas Temperature To, n(D1) = I(MTG.D1.1)/ max (i) with i=1 to 6 To, n(D2) = I(MTG.D2.1)/ max (i) with i=1 to 6 To, n(D1) =
409[K]
2 2 [K]
Tc_ n(D2) =
409 [K]
2 [K]
- Local Gas Temperature MTG.D1.1. 6 =
Top n(D1) 2 [K]
MTG.D2.1. 6 =
Tof n(D2) 2 [K]
- Water Level ML.D1 =
0,00 [m]
0,10 [m]
ML.D2 =
0,00 [m]
0,10 [m]
Sunnression Chamber 1 and 2 (V.S1 - V.S2) j
- Total Pressure MP.S1 =
301 [kPa]
4 [kPa)
MP.S2 =
301 [kPa]
4 [kPa]
- Mean Gas Temperature To, n(SI) = I(MTG.S1.1)/ max (i) with i=1 to 6 To_ n(S2) = I(MTG.S2.1)/ max (i) with i=1 to 6 Top..n(S1) =
352 [K) 2 [K]
Tof..n(S2) =
352 [K]
1 2 [K]
- Local Gas Temperature MTG.S1.1. 6 =
Tof..n(S1) 2 [K]
MTG.S2.1. 6 =
To_,n..n(S2) 2 [K) 7
- Mean Water Temperature Tw,..n(S1) = I(MTL.S1.i)/ max (i) with i=1 to 6 Tw,..n(S2) = I(MTL.S2.I)/ max (i) with i=1 to 6 Tw,..n(S1) =
352 [K) 2 [K]
Tw
,(S2) =
352 [K]
2 [K)
- Local Water Temperature MTL.S1.1.. 6 =
Twf..n(S1) 2 [K]
MTL.S2.1.. 6 =
Twf n(S2) 2 [K]
- Water Level ML.S1 =
3,80 [m]
0,10 [m]
ML.S2 =
3,80 [m]
0,10 [m]
ALPHA-528-0 ALPHA-528-0 Test initial Conditions List (cont'd) t GDCS (V.GD)
-Total Pressure MP.GD =
318 [kPa) 4 [kPa)
- Mean Fluid Temperature Tppon(GD) = I(MTF.GD.i)/ max (i) with i=1 to 7 Tpfon(GD) =
329 [K) 4 [K)
Local Fluid Temperature MTF.GD.1.. 7 = Tpfan(GD)-
4 [K)
- Water Level MLGD=
3,50 [m]
0,10 [m]
PCC1. PCC2 and PCC3 Pools (V.U1 - V.U2 - V.U3)
- Total Pressure
- MP.ENV =
97 [kPa)
Mean Water Temperature Twfon(U1) = I(MTL.U1.1)/ max (i) with i=1 to 7 Tw, n(U2)= I(MTLU2.i)/ max (i) with i=1 to 7 Twfon(U3) = I(MTLU3.1)/ max (i) with i=1 to 19
- Twfon(U1) =
372 [K)
+ 0/ -4
[K)
- Tw,on(U2) =
372 [K]
+0/ -4
[K)
- Twfon(U3) =
372 [K]
+0/ -4
[K)
- Local Water Temperature MTL.U1.1.. 7 = Tw,.n(U1) 2 [K)
MTLU2.1.. 7 = Tw,.n(U2) 2 [K)
MTL.U3.1.19 = Twfun(U3) 2 [K)
- Water Level ML.U1 =
4,80 [m]
i 0,20 [m]
MLU2 =
4,80 [m]
0,20 [m]
MLU3 =
4,80 [m]
0,20 [m]
Note:
- The pressure and temperature defined for the PCC Pools correspond to saturation values at usual atmospheric pressure at the test site.
10 initial Alignment Before starting any preconditioning process, the facility is set into the specific state which establishes operations from the control room. The configuration is set in order to avoid any unintentional hardware manipulation during testing or preconditioning. The Data Acquisition and Control System must be properly initiated and brought into operation. Valves are aligned in accordance to STARTUP Status, automatic heat power regulation files are loaded and the auxiliary water system is filled to allow pump operatien.
Five different preparation phases are needed for the Transient Tests: phase n*11 starting Control and Data Acquisition Systems, phase n*12 for the initial valve setup, phase n*13 for the configuration checking, phase n*14 to prepare the automatic heat power regulation and phase n*15 for auxiliary water system filling.
r 11 Control System and DAS Setup
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l ALPHA-528 ALPHA-528-0 Page 9 Page 9 13 General Facility Configuraton Check Meli @EfailNily,MoonsgigitTs t[EsppigsMog!AsisaNnE Record on attached checidist 14 Prepare Automatic Heat Power Regulation
((DiIliff7 N ~N N Rf maenmnamassencensesst cale= ec)62{M Record on attached checidist l
15 Auxiliary Water System Filling Fill the Auxiliary Water System i
4 i
16 instrument / Zero Check 16.0E'TEMMf56bDqip7Gasandh~ Heaters ^ d
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Record on attached checidist i
4 20 RPV Setup for Vessel Preconditioning As the heat source for the whole preconditioning process, the RPV must be capable of producing steam for vessel heating or providing hot water to the auxiliary system. In order to establish conditions to generate steam, the RPV is first heated to 373K, while most of the air is purged by l
venting to the atmosphere. Not all air is purged at this temperature, but that does not affect vessel preconditioning; pure steam conditions are only required for the tests. Then the RPV is F
heated to about 415K to supply the auxiliary water system heat exchanger.
The RPV water level is set before preconditioning to anticipate evaporation occuring during i
heating by steam injection; it should reach the required test water level at the end of the preconditioning process. However in any case it must be lower than the main steam line inlets to avoid water hammer.
21 Water Filling 21.0 Monitor RPV Parameters Assumption:
- Water Level MLRP.1 =
0,0 [m]
M(RPV-water) =
0,00 (ton) 21.1 Supply water until level reaches 3,5 (m)
Vent Air to the Atmosphere
- Open valve CC.RPV Auxiliary water system opeiation I
2 [l/s]
FAAl.!.RPJuMSEl{vn]Mj M(RPV-water) =
4,29 [ ton)
> time
2146 [sec)
Pump MP. BOD Off Fill preheater heating side with water
- Open valve CB.HRH, CB.HFH 21.2 Monitor RPV Parameters
3,50 [m]
d
ALPHA-528-0 ALPHA 526-0 PageSO Page 10 22 Heating / Purging 22.0 Monitor RPV Parameters 0,97 [bar]
-Total Pressure Assumptions:
MP.RP.1 =
97 [kPa]
=
10 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
283 [K]
=
10 [*C]
- Structure temperature MTI.RP.1.. 3 =
283 [K]
=
3,50 [m]
22.1. Heat until temperature equals 373
[K]
800 [
IIllTIT@3 47
> AT
90 [K]
hi M M % M st f M 19C3 d M(RPV-water) =
4,29 [ ton]
> AO
1,62 [GJ)
M(RPV-struct) =
8,00 (ton]
> AO
0,36 [GJ]
> AQtot
1,98 [GJ]
> time
2480 (sec]
EMWpjleWld 22.2 Heat until temperature equals 415 [K]
> AT
42 [K]
HQ11n
- Temperature corresponding to the heat exchanger operation:
SC's water filling M(RPV-water) =
4,29 [ ton]
> AO
0,76 [GJ)
M(RPV-struct) =
8,00 [ ton]
> AQ
0,17 [GJ]
> AQtot
0,93 [GJ)
> time
1157 (sec)
Heaters Off 22.3 Monitor RPV Parameters 3,88 [bar]
-Total Pressure MP.RP.1 =
388 [kPa]
=
142 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
415 [K)
=
142[*C]
- Structure temperature MTI.RP.1.. 3 =
415 [K]
=
3,8 [m]
M(RPV-water) =
4,29 [ ton]
30 Suppression Chambers Setup The Test initial Conditions require a collapsed water level in both Suppression Chambers of 3,8m above the PANDA heater bundle, that corresponds to a water column of 3,8m from the bottom of the Suppression Chamber. The required temperature is a homogeneous temperature of 352K for the pool water as well as for the gas space. The total pressure, considering saturated conditions,is at 301kPa, which includes an air partial pressure of 256kPa.
The Suppression Chambers Setup starts with water filling and pool conditioning (phase n*31),
continues with gas space heating by steam injection keeping 1 bar air partial pressure inside the vessels (phase n*32). The total pressure is then set up by injecting air with the auxiliary air system (phase n*33). Phase n*33 is performed during phases n*31 and 32.
31 Water Filling 31.0 Monitor SCs Parameters Assumptions:
0,97 [bar]
- Total Pressure MP.S1 =
97 [kPa]
=
0,97 [bar]
MP.S2 =
97 [kPa]
=
10 [*C]
- Local Water Temperature MTL.S1.1.. 6 =
283 [K]
=
10 [*C]
MTL.S2.1.. 6 =
283 [K]
=
- Water Level ML.S1 =
0,00 [m]
ML.S2 =
0,00 [m]
ALPHA-528-0 ALPHA-528-0 V
- Page 11 -
Page 11 31.1 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters 3,88 [bar)
Total Pressure MP.RP.1 =
388 [kPa]
=
142 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
415 [K)
=
- Water Level MLRP.1 =
3,78 [m]
21.2 Supply water until level reaches 3,8 [m]
Auxiliary water system operation Pump PC.HFH On Setup control valve CC. BHA MBTCBHf=*E3(4TgSTneMGMTD]YK]
CC.BCA MTL.BCA =
max [K)
- Open valve CB.S1L, CB.S2L Pump PC. BOD On MV.B00 =
2 [l/s)
MiM;fM1M3ff[ny)[h
- Mg g
M(S1-water) =
42,50 [ ton]
1 Q= 3AJm]
M(S2-water) =
42.50 [ ton)
M(TSL-water) =
7,10 [ ton)
> time
46050 [sec)
- Close valve CB.S1L, CB.S2L Pump PC. BOD Off MV. BOD =
0 [l/s]
Pump PC.HFH Off Heaters Off 31.3 SCs Parameters 79 [*C]
- Mean Water Temperature Tw.,n..n(S1) =
352 [K)
=
79[*C]
Tw.n(S2) =
352 [K)
=
- Water Level ML.S1 =
3,80 [m]
ML.S2 =
3,80 [m]
32 Gas Space Heating 32.0 Monitor SCs Parameters Assumptions:
1,56 [bar)
- Total Pressure MP.S1 =
156 [kPa)
=
1,56 [bar)
MP.S2 =
156 [kPa)
=
10 [*C]
- LocalGas Temperature MTG.S1.1.. 6 =
283 [K]
=
10 [*C]
MTG.S2.1.. 6 =
283 [K)
=
10 [*C]
- Structure temperature MTI.S1.1._9 =
283 [K]
=
10 [*C)
MTI.S2.1.. 9 =
283 [K)
=
j 32.1 RPV Setup for Steam injection Monitor RPV Parameters 3,88 [bar]
-Total Pressure MP.RP.1 =
388 [kPa)
=
142 [*C)
- Local Fluid Temperature MTF.RP.1.. 5 =
415 [K]
=
3,78 [m]
800 [kW) 322 Steam injection
- Open valve CB.B1S, CB.S1S, CB.S2S WATfI.B=$7&iGNi"%
> AT
69 [K)
[h3/84M@3Ey@79.{*C]Mg l
MT1.S2.12.9iBdi2 g!W$TMQygg(K]jjicQ l
M(SCs-struct) =
72,7 [ ton]
> AO
2,52 [GJ)
AM(steam) = 1095 [kg)
> time
3148[sec)
Close valve CB.B1S, CB.S1S, CB.S2S Heaters Off i
ALPHA-520-0 ALPHA-528-0 Page 12 Page 12 Monitor RPV Parameters 3,88 [bar)
-Total Pressure MP.RP.1 =
388 [kPa)
=
142 [*C]
- Local Fluid Temperature MTF.RP.1,. 5 =
415 [K)
=
2,82 [m]
32.3 Monitor SCs Parameters 2,01 [bar]
- Total Pressure MP.S1 =
201 [kPa)
=
2,01 [bar)
MP.S2 =
201 [kPa)
=
79[*C)
-Mean Gas Temperature To,..n(S1) =
352 [K)
=
79 [*C]
Ta,..n(S2) =
352 [K)
=
79[*C)
Mean Water Temperature Tw,..n(S1) =
352 [K)
=
79 [*C)
Tw,..n(S2) =
352 [K)
=
- Water Level MLS1 =
3.80 [m]
MLS2 =
3,80 [m]
33 Pressurization 33.0 Monitor SCs Parameters 2,01 [bar)
- Total Pressure MP.S1 =
201 [kPa)
=
2,01 [bar)
MP.S2 =
201 [kPa)
=
33.1 Air injection until total pressure reaches 301
[kPa]
Auxiliary air supply system operation Setup controlvalve CC.80G.2 MM. BOG = max
- Open valve CB.StG, CB.S2G, CB. BOG ISIETW K=7 M M E @ W @
AM(air) =
62 [kg)
> time
2073 [sec)
- Close valve CB.S1G, CB.S2G, CB.B0G 332 Monitor SCs Parameters 3,01 [bar]
- Total Pressure MP.S1 =
301 [kPa)
=
3,01 [bar]
MP.S2 =
301 [kPa)
=
79 [*C]
Mean Gas Temperature To, n(S1) =
352 [K]
=
79 [*C]
To, n(S2) =
352 [K]
=
79 [*C]
Mean Water Temperature Tw,..n(S1) =
352 [K)
=
79 [*C)
Tw,..n(S2) =
352 [K)
=
- Water Level ML.S1 =
3,80 [m]
MLS2 =
3,80 [m]
40 GDCS Heating The Test Initial Conditions require a water level in the GDCS tank of 14,8m above the PANDA heater bundle, corresponding to a water level of 4,10m from the bottom of the tank, taking into account a full GDCS Retum Line. The required temperature is a homogeneous temperature of 329K for the whole tank, which is achieved by filling with water up to approximately 5,5m at the required temperature and then draining the tank until the required level is reached. The total pressure in GDCS, under srtrated conditions and in equilibrium with the Drywell pressure is at 318kPa, which include a air partial pressure of 16kPa.
The GDCS Setup consits of heating by water filling (phase n' 41) and pressurization by air injection (phase n' 42). Filling and draining processes are performed with the GDCS vent valve open. The total pressure is then adjusted by injecting air by mean of the auxiliary air system or by venting air to the atmosphere (phase n' 42). That last phase is performed after water has been drained and transferred to the PCC pools.
ALPHA-528-0 ALPHA-528-0 Page 13 Page 13 41 Water Filling 41.0 Monitor GDCS Parameters Assumptions:
0,97 [bar]
- Total Pressure MP.GD =
97 [kPa]
i
=
10 ['C]
- Local Fluid Temperature MTF.GD.1.. 7 =
283 [K]
=
10 [*C]
- Structure temperature MTI.GD.1 6 =
' 283 [K)
=
- Water Level ML.GD =
0,00 [m] '
41.1 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters 3,88 [bar)
-Total Pressure MP.RP.1 =
388 [kPa]
=
142 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
415 [K]
=
Water Level MLRP.1 =
2,82 [m]
800 [kW]
41.2 Supply water until level reaches 5,5 [m]
Setup controlvalve CC.BUV
- Open valve CB.GDV Auxiliary water system operation Pump PC.HFH On 58 [*C]
Setup control valve CC. BHA MTL. BHA =
331 [K)
=
CC.BCA MTL.BCA =
max [K)
2 [l/s]
- Open valve CB.GDL E"EEI M M M i M(GD-water) =
16,4 [ ton]
> time
8195 [sec]
- Close valve CB.GDL Pump PC. BOD Off Pump PC.HFH Off Heaters Off 41.3 Monitor GDCS Parameters 0,97 [bar]
- Total Pressure MP.GD =
97 [kPa]
=
- Mean Fluid Temperature Trf (GD) =
329 [K]
56 [*C]
=
56 [*C]
- Structure temperature MTI.GD.1.. 6 =
329 [K)
=
- Water Level MLGD=
5,50 [m]
42 Pressurization 42.0 See phase n*73 Since the GDCS is full with water, it cannot be pressurized during the phase n*42.
The GDCS pressurization is performed at phase n*73.
ALPHA-528-0 ALPHA-528-0 Page 14 Page 14 50 PCC1 Pool Setup The Test Initial Conditions for all PCC Pools are the same; water level from the top of the PANDA heater bundle is defined at the maximum possible level (23,6m), which corresponds to a water level of 4,8m in the pools. The end point temperature is near the saturation temperature for actual atmospheric pressure.
The Pools Setup is performed as follows: water is filled at the highest possible temperature (phase n*51, 61, 71 & 72) and the temperature conditions are adjusted then by water circulation through the auxiliary heat exchanger (phase n*105,106 & 107).
Ngig Pools can be connected together and filled simultaneously; water circulation might also be performed simultaneously with interconnected pools.
51 Water Filling 65.0 Monitor PCC1 Pool Parameters 10 ['C]
- LocalWater Temperature MTL.U1.1.. 7 =
283 [K)
=
- Water Level ML.U1 =
0,00 [m]
65.1 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters 3,88 [bar)
> Total Pressure MP.RP.1 =
388 [kPa]
=
142 ["C]
Local Fluid Temperature MTF.RP.1. 5 =
415 [K)
=
2,82 [m]
800 [kW]
HQ1g The RPV temperature indicated here is a basis for the water filling operation; it might be lower than indicated.
51.2 Supply water untillevel reaches 4,9. [m]
Auxiliary water system operation
^
Pump PC.HFH On 102 [*C]
Setup controlvalve CC. BHA MTL. BHA =
375 [K)
=
CC.BCA MTL.BCA =
max [K]
2[l/s]
- Open valve CB.U1L h
2MCD[=34)MnD M(U1-water) =
14,22 [ ton]
> time
7111 [sec)
Close valve CB.U1L Pump PC.B0D Off Pump PC.HFH Off Heaters Off 51.3 Monitor PCC1 Pool Parameters 99 [*C]
- Mean Water Temperature Tw,..,(U1) =
372 [K]
=
- Water Level ML.U1 =
4,90 [m]
60 PCC2 Pool Setup For PCC2 Pool Setup refer to description of pools condrtioning in phase n*50.
61 Water Filling 61.0 Monitor PCC2 Pool Parameters
- Local Water Temperature MTLU2.1.. 7 =
283 [K]
10 ['C]
=
- Water Level ML.U2 =
0,00 [m]
ALPHA-528 ALPHA-528-0 i
Page 15 Pag 15 i.
RPV Setup for Heat Exchanger Operation Monitor RPV Parameters 3,88 [bar)
-Total Pressure MP.RP.1 =
388 [kPa]
=
142 [*C]
Local Fluid Temperature MTF.RP.1.. 5 =
415 [K)
=
- Water Level MLRP.1=
2,82 [m]
MQtg The RPV temperature indicated here is a basis for the water filling operation; it might be lower than indicated.
61.2 Supply water until level reaches 4,9 [m]
Auxiliary water system operation Pump PC.HFH On 102 [*C]
Setup controlvalve CC. BHA MTLBHA =
375 [K]
=
CC.BCA MTL.BCA =
max [K)
2 [l/s)
- Open valve CB.U2L PGTIQ.R si?d.4(jm))jf M(U2-water) =
14,22 [ ton]
> time
7111 [sec)
- Close valve CB.U2L
_p Pump PC. BOD Off Pump PC.HFH Off Heaters Off 61.3 Monitor PCC2 Pool Parameters 99 [*C]
- Mean Water Temperature Tw_m..n(U2) =
372 [K)
=
- Water Level ML.U2 =
4,90 [m]
70 PCC3 Pool Setup For PCC3 Pool Setup refer to description of pools conditioning in phase n*50. In that case, the water comes from the GDCS; this phase defines the transfer (of the water used to heat the GDCS tank) from GDCS to PCC3 pool.
After water has been drained, the GDCS is pressurized by air injection (phase n*73).
71 Water Transfer from GDCS Tank 71.0 Monitor PCC3 Pool Parameters 10 ['C]
- Local Water Temperature MTL.U3.1.19 =
283 [K]
=
- Water Level ML.U3 =
0,00 [m]
Monitor GDCS Parameters 0,97 [bar)
- Total Pressure MP.GD =
97 [kPa)
=
56 ['C]
- Mean Fluid Temperature Tp_m n(GD) =
329 [K)
=
56 [*C]
- Structure temperature MTI.GD.1.. 6 =
329 [K)
=
- Water Level ML.GD =
5,50 [m]
71.1 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters 3,88 [bar)
-Total Pressure MP.RP.1 =
388 [kPa)
=
142 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
415 [K)
=
2,82 [m]
)
ALPHA-528-0 ALPHA-528-0 Page 16 Page 16 Heaters On MW.RP.7 =
800 [kW)
Note: The RPV temperature indcated here is a basis for the water filling operation; it might be lower than indicated.
712 Supply water untillevel reaches 3,5 [m] in the GDCS tank Auxiliary water system operation Pump PC.HFH On 110[*C]
Setup controlvalve MTLBHA=
383,0 [K)
=
MTL.BCA =
max [K)
Pump PC. BOA On MV. BOA =
2 [l/s)
- Open valve CB.BOL, CB.LXA, CB.AXU CB.U3U, CB.GDL QTOMYWVin[d ljMMAU3,,sijd5j,[m]
M(U3-water) =
4,21 [ ton]
> time
2104 [sec)
- Close valve CB.U3U, CB.GDL CB.BOL, CB.LXA, CB.AXU Heaters Off Pump PC. BOA Off Pump PC.HFH Off isolate GDCS from atmosphere
- Close valve CC.BUV, CB. GOV 71.3 Monitor PCC3 Pool Parameters 99[*C]
- Mean Water Temperature Tw_m..n(U3) =
372 [K]
=
- Water Level ML.U3 =
1,45 (m]
Monitor GDCS Parameters 0,97 [bar)
- Total Pressure MP.GD =
97[kPa]
=
56('C]
- Mean Fluid Temperature TF.,me.n(GD) =
329 [K]
=
56['C]
- Structure temperature MTI.GD.1.. 6 =
329 [K]
=
Water Level ML.GD=
3,50 [m]
Monitor RPV Parameters 3,88 [bar)
Total Pressure M P.n P.1 =
388[kPa)
=
142[*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
415 [K)
=
2,82 [m]
72 Water Filling Since the available water in GDCS does not fill entirely the PCC3 pool, cold water is supplied from the demineralized water tank.
72.0 Monitor PCC3 Pool Parameters 99['C]
- Mean Water Temperature Tw m..n(U3) =
372 [K)
=
- Water Level ML.U3 =
1,45 [m]
72.1 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters 3.88 [bar)
-Total Pressure MP.RP.1 =
388 [kPa)
=
142 [*C]
Local Fluid Temperature MTF.RP.1.. 5 =
415 [K)
=
2,82 (m)
~
ALPHA-528-0 ALPHA-528-0 v
Page 17 Page 17 MW.RP.7 = 800 [kW)
HQ1E The RPV temperature indicated here is a basis for the water filling operation; it might be lower than indicated.
72.2. Supply water until level reaches 4,90 [m]
Auxiliary water system operation Pump PC.HFH On 102 ['C]
Setup controf valve CC. BHA MTL. BHA =
375 [K]
=
CB.BOL CC.BCA MTL.BCA =
max [K)
2 [l/s]
- Open valve CB.U3L
{}djlch164Wi[i63 M(U3-water) =
10,01 [ ton]
> time
5007[sec]
Close valve CB.U3L Pump PC. BOD Off Pump PC.HFH Off Heaters Off 72.3 Monitor PCC3 Pool Parameters 99 ['C]
- Mean Water Temperature Tw_m..n(U3) =
372 [K]
=
- Water Level ML.U3 =
4,90 [m]
73 GDCS Pressurization 73.0 Monitor GDCS Parameters 0,97 [bar]
- Total Pressure MP.GD =
97 [kPa]
=
73.1 Air injection until total pressure reaches 318 [kPa]
Auxiliary air supply system operation Setup controlvalve CC.B0G.2 MM. BOG = max
- Open valve CB.GDG, CB. BOG NElfR.GDWM314WG fEP 2TiiTibe:FU AM(air) =
14,0 [kg]
> time
465 [sec)
- Close valve CB.GDG, CB.80G 732 Monitor GDCS Parameters 3,18 [bar)
- Total Pressure MP.GD =
318 [kPa]
=
- Mean Fluid Temperature T, m..n(GD) =
329 [K)
Water Level ML.GD =
3,50 [m]
80 Drywells Setup The nominal Drywell condition is no water, pure steam condition and homogeneous temperature of 409K.
The Drywells Setup consists of steam injection to heat up the gas space and the structure; the air is purged during the first part of the heating process in order to get pure steam conditions J
(phase n'81).
During the heating process, the RPV, used as steam source, is cooled down in order to j
approach the required test initial conditions - heater power is controlled in order to decrease the RPV temperature.
1
1 ALPHA-528-0 ALPHA 528-0 Page 18 -
Page 18 g.
81 Gas Space Heating 81.0 Monitor Drywell Parameters
_ Assumptions:
0,97 [bar]
Total Pressure MP.D1=
97 [kPa]
=
0,97 [bar]
MP.D2 =
97 [kPa]
=
10 ['C]
Local Gas Temperature MTG.01.1.. 6 =
283 [K)
=
10 ['C]
MTG.D2.1.. 6 =
283 [K)
=
10 [*C]
- Structure temperature MTI.D1.1.. 9 =
283 [K]
=
10 [*C]
MTl.D2.1.. 9 =
283 [K]
=
- Water Level ML.D1 =
0,00 [m]
ML.02=
0,00 [m]
81.1 Connect Drywells to all PCC Condensers
- Open valve CB.P1F, CB.P2F, CB.P3F 81.2 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters 3,88 [bar]
Total Pressure MP.RP.1 =
388 [kPa]
=
142[*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
415 [K)
=
- Water Level MLRP.1=
2,82 [m]
800 [kW) 81.3 Steaminjection (withairpurging)
Vent valve opening for air purging Open valve CC.BUV, CB.D1V, CB.D2V Open valve CB.B1S, CB.D1S, CB.02S T4ffCDCW 6 $ PJ W' L'Il
> AT
90 [K)
- ~
1 yggy
" ~
- ?
> AT
90[K)
DN e
N!NNO5 -
M(DWs-struct) =
48,9 [ ton]
> AO
2,21 [GJ)
M(DWs-steam) =
98 [kg)
> AQ
0,26 [GJJ
> AQtot
2,47 [GJ)
AM(steam) = 1073 [kg]
> time
3084 [sec)
Vent PCC Feed lines are closed when temperature has reached 373K and is steady h
C8.PiF CB ps%WjiQF(without air purging) 81.4 Continue Steam injection
> AT
36 [K]
$WsMd 414fD.tE1d@e;==pp;138; MilW
> AT
36 [K)
48,9 [ ton]
> AQ
0,88 [GJ)
M(DWs-steam) =
182 [kg]
>30
0,44 [GJ]
> A0 tot
1,32 [GJ]
AM(steam) =
575
[kg)
> time
1652 (sec)
- Close valve CB.B1 S, CB.D1 S, CB.D2S Heaters Off Note:
- During that phase, the RPV, used as heat source for steam injection to the Drywell, is cooled down in order to approach the required test initial conditions - heat power is controlled (eventually not used) in order to decrease the RPV temperature.
l ALPHA-528-0 ALPHA-528-0 i
Page 19 Page 19 81.5 Monitor RPV Parameters j
3,19 [bar]
-Total Pressure MP.RP.1 =
319 [kPa]
=
136 ['C]
- Mean Fluid Temperature Tr_ n(RP) =
409 [K]
=
- Water Level MLRP.1 =
1,50 [m]
Monitor Drywell Parameters 3,19 [bar]
- Total Pressure MP.D1 =
319 [KPa]
=
3,19 [bar)
MP.D2 =
319 [kPa)
=
136 [*C]
- Local Gas Temperature MTG.D).1.. 6 =
409 [K]
=
136 [*C]
MTG.D2.1 6 =
409 [K]
=
136 [*C]
- Structure temperature MTI.D1.1.. 9 =
409 [K]
=
136 ['C]
MTI.D2.1 9 =
409 [K]
=
90 RPV Initial Conditions Setup for Test After having used the RPV as heat source for vessel preconditioning, it might be under conditions differing from these required for test initiation; water level, pressure and temperature may need to be adjusted in order to satisfy the test initial conditions.
Phase n' 91 starts with a parameter monitoring, which will give the basis for RPV condition adjustement.
91 Adjusting RPV Conditions 91.0 Monitor RPV Parameters Assumtions:
3,19 [bar]
-Total Pressure MP.RP.1 =
319 [kPa]
=
136 [*C]
- Mean Fluid Temperature Tr_ n(RP) =
409 [K]
=
3,50 [m]
91.1 Adjust Test initial Conditions in RPV Assuming saturated conditions and a negligible air partial pressure, the pressure is set by adjusting the temperature. Cooling is achieved by venting steam to the atmosphere. Heating is performed by using RPV heaters. Any required action is allowed to set up the RPV test initial conditions with the required tolerances (see phase 01).
100 Test Conditions Setup PANDA preconditioning has now been performed and the state of the facility is close to that required for test initiation; conditions out of tolerance must be adjusted to the defined values.
The test condrtion setup starts with the adjustment of both Suppression Chamber (SC) Pools (phase n' 101) and continues with the SCs gas space setup (phase n*102). The GDCS tank is then adjusted to its defined test initial conditions (phase n*103), before adjusting conditions of both Drywells (phase n' 104). The test condition setup continues with the PCC Pools condition adjustment (phase n* 105,106 & 107), which can be performed simultaneously. All these phases are not defined in detail, allowing any required action to get the test initial conditions established.
)
ALPHA-5284 ALPHA-528-0 Page 20 q-Page 20 101 Adjusting SC Pools Conditions l
101.0 Adjust Test Initial Conditions in Suppression Chamber Pools After the check of the water temperature and water level, required action to adjust the corresponding parameters are supplying or draining water to satish N defined water level, and water circulation through one or the other of the two auxiliary c.,at exchangers as required to adjust the desired temperature. Any action is allowed to setup the SCs pools test initial conditons according to the defined tolerances (see phase 01).
101.1 Monitor SCs Parameters
}Ei$g f } @ M. { W : @ g%y $g g 4 K$Qi fifMQpQ
}d
- Mean Water Temperature M
E D
$p@g d m w {jksg$jgyht ' 'Q[B $$$
p(t me f MFQEMj 3 [Mt4NE LocalWater Temperature h? S!
Mh M
E
$M Q$dl.;S8 MgAQ114{n$
pe%cdW6th
- Water Level WRmwW41SM11d
- d Record on attached checklist 102 Adjusting SC Gas Space Conditions 102.0 Adjust Test initial Conditions in Suppression Chamber Gas Space Assuming saturated steam / air mixture, the temperature and the pressure are separately adjusted by steam and air injection. Any required action is allowed to setup the SCs gas space test initial conditions according to the defined tolerances (see phase 01).
102.1 Monitor SCs Parameters
'-r" sfW
- Total Pressure q'J4NcR W +
- k k b
),
i g% -
lg:y
- Mean Gas Temperature i<
e 3jl $$
1 9
b.
Y W
R 9
~
4M WiSMsl$
h?jp j
, %i 9
h j
Ed I g
inq
% fNMMgfk j
-LocalGas Temperature i
$11 RIG.St.1$hQ"[ "
Record on attached checklist 103 Adjusting GDCS Conditions 103.0 AdjustTestinitialConditions in GDCS Assuming saturated steam / air mixture, the temperature and the pressure are separately adjusted by steam and air injection. Any required action is allowed to setup the GDCS test initial conditions according to the defined tolerances (see phase 01).
103.1 Monitor GDCS Parameters O,04 pier]/P{f5 li($m dig 1D=)323,1s$asfjP??
-Total Pressure
$@dhg(MGD)Mi%229SQf!h y@Sq@
Ii
}bM
- Mean Fluid Temperature rM%l%j@i$2fCig%g$gy@gy@j y yggW AD.11 Q s Q D)j h
- Local Fluid Temperature h
- Water Leve!
9k J)JLGD=WS.WimJfMW r/0,101aGMM Record on attached checklist m
w-
- w
ALPHA-528-0 ALPHA-528-0 i
Page 21 Page 21 104 Adjusting DWs Conditions -
104.0 AdjustTestinitialConditionsin Drywells Assuming saturated conditions and an air partial pressure satisfying the required value, the temperature is adjusted by steam injection. Any required action is allowed to setup the Drywells test initial conditions according to the definea tolerances (see phase 01).
104.1 Monitor Drywell Parameters
M SIgMPG Mfy gpPsQ
$qpbd4fG.02.!d=@gggliiPs}Qigg$$Faj
- Air Partial Pressure pOAjflelW $g i
E h M M k h h 45(IM h E M f' M M h
- Mean Gas Temperature k,
kkhNYNh?$ h
'S fkW h?h? ~\\
4#
p:{pm nr,w,mm" J y
3 4
A pn Mr;g f
- Local Gas Temperature hi!
)
h NY k
slg((@h$8 in g;
pg
- Structure temperature Oh
&i $
m:
&pM5lW[FtLDit=mmom*sG(Mide$$ek{ D y h 1DglM y.
dSD
. Water Level
,10Ju 5
Record on attached checklist 105 Adjusting PCC1 Pool Conditions 4
105.0 AdjustTestinitialConditionsin PCC1 Pool For all pools, water temperature adjustment is performed by water circulation through the auxiliary heat exchanger and level adjustment by supplying water from the demineralized water tank. Any required action is allowed to setup the PCC pools test initial conditions according to the defined tolerances (see phase 01).
Since all PCC pool initial conditions are the same, they may be adjusted simultaneously by connecting the four pools together, 105.1 Set PCC1 Pool Parameters
- Mean Water Temperature
$ %F"*HHay Q
ie4@j%!r, gpgg
- Local Water Temperature j hg j
g I!M W#@fi AL.U1k;SN,W W/0,2Disig Mi Water Level Record on attached checklist 106 Adjusting PCC2 Pool Conditions 106.0 AdjustTestinitialConditionsin PCC2 Pool For PCC2 Pool conditions adjustment refer to description of phase n*105.
106.1 Monitor PCC2 Pool Parameters 1 % (N i M M i % f5 j p % 5 5 ]IQ @ p +0 F 4L{
qwgu2)k
- Mean Water Temperature hh j
QvJp4Altu2.1M MNMhntELU2d=$7,7 dMMj$?:2?@$1K]yfgp2Q
- Local Water Temperature MOsism1FR443]O,201saj UC 2 i
- Water Level Record on attached checklist
ALPHA-528-0
' ALPHA-528.
Page 22 Page 22 107 Adjusting PCC3 Pool Conditions 107.0 Adjust Test initial Conditions in PCC3 Pool For PCC3 Pool conditions adjustment refer to description of phase n*105.
107.1 Monitor PCC3 Pool Parameters -
- Mean Water Temperature
- W;- 3 T " N p % 272 % @gg
$ W $w 4W 6 g#p a
~
4' wsac h, Nb 3
- LocalWater Temperature a
$$$ f
_ $$2MAEM Ei $
- Water Level Record on attached checklist 110 Test The facility satisfies now the required test initial conditions and must be configured according to i
the test configuration desenbed in GE Test Plan. Due to the relatively quick test initiation, data recording is started (phase n*111) before setting the desired RPV conditions (phase n*112) and before setting the test configuration (phase n*113). That last phase should not affect the PANDA conditions, but in order to assure test initial conditions satisfying the defined tolerances, the '
duration of all these phases between the test configuration setup (phase n*113.1 to 113.9) and the test initiation (phases n*113.10 to 113.12) should not exceed a few minutes (-Smin). Before test initiation, just before phase n' 113.10, the test initial conditions must be within the tolerances given in all n*100 and n*112 phases, in order to satisfy the acceptance criteria defined in phase
- 01. If test initial conditions do not satisfy the above mentioned acceptance criteria, the test is interrupted, the heat power is shut down (phase n* 122.0), the vessels are isolated (phase n' 122.4) and the procedure starts again with the Test Conditions Setup (phase n' 100).
Due to the excessive pressure differences between vessels during the preconditioning, the pressure difference transmitters valve-in must be performed after the test initial conditions have been established; it is performed during test configuration setup (phase n*113.8).
111 Data Recording 111.0 Start Data Recording MMWe
' Record on attached checidist i
111.1
- mutuumMat,elgjgglethyndj2mW$
Record on attached checidist 112 Adjusting RPV Conditions 112.0 AdjustTestInitialConditionsin RPV Assuming saturated conditions and a negligible air parijal pressure, the required pressure is set by adjusting the temperature. Any required action is allowed to setup the RPV test initial conditionc, according to the defined tolerances (see phase 01).
112.1 Monitor RPV Parameters gp3f9%pNg5 " '
. bas 1}g ji
(
-Total Pressure.
J9W A*, _
W 40thi ggs d
- Mean Fluid Temperature 1N
- k. ETJIP)
%gN wph se; W notes [ @{' -
pH apr
- LocalFluid Temperature l y.
[. _ _,
WPSAS
- Water Level
- PDM e
Record on attached checklist i
t
?.
ALPHA-528-0 ALPHA-528-0 e
Page 23 Page 23 113 Configuration Setup and Test initiation Before test initiation the PANDA facility is partly configured; all valves which must be lined up are open, except both main steam line valves and the GDCS drain line valve.
These last lineup processen are included in the test initiation phase; they are perfomed at phases n*113.11 1
k 113.0 Setup Automatic Heat Power Regulation M6DPElllAWi@llWElW p2mM $N Record on attached checklist 33 L
- EFDLNSENT ST_Af}TMAFJiSCRAM*
113.1 Isolate Pools Pools might be already isolated, in that case verify that the following valves are closed C9a(
{ll3sepgele?!pClggdWraFgg))gy, $$hdN Record on attached checklist
$DS$5M$i.;1CSM1td5.iELifCSA130 1132 Open GDCS Pressure Equialization lines MMMME Record on attached checklist 113.3 Open Main Vent Lines
@ ipaspp F E C IB M M if f2 M
. Record on attache <1 checklist i
113.4 Open PCC Vent Lines EsbangehipMMFtII[CEf.Pi@7CSYSVI~~!
Record on attached checklist 113.5 Open PCC Condensate Lines Eonsiwesusace m.wica m.d Record on attached checklist 113.6 Open all PCC Feed Lines Ehsabth42BfiPitn/MCM Record on attached checklist 113.7 Instrument / Zero Check and Pressure Difference Transmitters Piping Valve in i
WW
~ % inj @ g gJQ bCMig etammamamies $sgge(inJ$less ef*16 MN$W 'dh Record on attached checklist i
113.8 VB-Opening Setup allt,0sgelc_
W Record on attached checklist 113.9 Heat Power Setup ECsiiiiit SiisitisilDiiiiTEIM$isikWeseTrist aiiiiiil%
~
~
s $degMCTLRena tdshtTED FOmfEftC? POWWERDN"Mid Esmeetwmm.NemieniuriuscAmidNS STAillCEE Record on attached checklist 113.10 Open Main Steam Lines EOpenivahe R Dib W rWEih 3P Record on attached checklist 113.11 Open GDCS Drain Line EOpenvadveFCisIGRTKCIEGRD]
Record on attached checklist 113.12 Print Valve Status Report every hour during the Test duration FwSw N MMEM iAAntil Velve Sakse nspons to the_ Checklist 3 Record on attached checklist
l ALPHA-528-0 ALPHA-528-0 Page 24 Page 24 g
113.13 Check Os Probes c.n edi a mo n w% m$ cggen b M [sust K ff @ w m id[
9@M WSj[
an.tamesa= =walemines Record on attached checklist 113.14 Check Test initial Conditions - Gee if Acceptance Criteria were reached before Test Initiation R@ M ~es @ E6hesesf elm,lS T Record on attached checklist 113.15 TestInterruption if the Acceptance Cdteria were not satisfed before test start, conduct phases n*122.1 & 122.4
=> phase n' 122.1
=> phase n' 122.4
- Restart procedure with phase n' 100 (Test Conditions Setup) 120 End of Test At the end of 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> data recording may be terminated (phase n*121), and the test performance declared complete.
The facility shutdown is described at phase n'122.
121 End of Data Recording 121.0jGlMip,_M ( poe@s'_ C M Record on attached checklist At 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> after test start, the test is terminated and data recording stopped.
j 121.1 bisue cstaMAAS times's Oulde) W6 Record on attached checklist 1212 Missgespipes af eleiiiton Om aniM3stNJ11 Record on attached checklist 122 Facility Shut Down 122.0 VB-Opening Setup
- Disable automatic VB-Opening Control (Procesr, Control System) 122.1 Stop Heat Power Heaters Off 122.2 Oxygen Probes Shut Off 122.3 Pressure Transmitters Piping Valve Off 122.4 Isolating Vessels Check that the following valves are closed :
CB.MS1, CB.MS2 CB.P1F, CB.P2F, CB.P3F CB.P1C, CB.P2C, CB.P3C CB.P1V, CB.P2V, CB.P3V CB.GRT.2.CB.GRT.1 CB.MV1, CB.MV2 CB.GP1, CB.GP2
,. - _~.-.
o; l
ALPHA-528-0 ALPHA-528-0 l
., / '
Page 25 Page 25 122.5 Valve Alignment i
- Set valve positions accordirig to the valve STARTUP status
- Print out valve status report
- Compare the printed out valve status report to valve STARTUP status i
4 122.6 ' - Set " Data recording ra# on HP-1000 / Low Scan Rate: 2*10 Hz 2
b i
s Y
5 i
i a
i I
a 4
f i.
1 5
L i
s i
I i
e I
5 1
n s
?
ALPHA-528-0 ALPHA-528-0 Page 26 Page 26 i
200 Checklist Checklist Transient Test Number:
Date:........
Completion of Procedure Date / Time Signatures Phase n' Performer / Reviewer 11 12 13 14 16 101.1 102.1 103.1 104.1 105.1 106.1 107.1 l
111.0 111.1 Building Temperatures at Om:
and 22m:
112.1 113.0 113.1 113.2 113.3 113.4 113.5 113.6 113.7 113.8 113.9 113.10 Time of Test Start 3
t 4
ALPHA-528-0 ALPHA-528-0
/
Page 27 Page 27 Checklist (cont'd)
Transient Test Number:
Date:........
Completion of Procedure Date / Time Signatures Phase n' Performer / Reviewer 113.11
[
113.12 113.13 113.14 121.0 121.1 j-121.2 Building Temperatures at Om:
and 22m:
i t
i I
l n
- m..
_