ML20096F405
| ML20096F405 | |
| Person / Time | |
|---|---|
| Site: | 05200004 |
| Issue date: | 09/22/1995 |
| From: | Aubert C PAUL SCHERRER INSTITUTE |
| To: | |
| Shared Package | |
| ML20096F375 | List: |
| References | |
| ALPHA-520, NUDOCS 9601230373 | |
| Download: ML20096F405 (28) | |
Text
.
- s PAUL SCHERRER INSTITUT EEfunkE Document No.
ALPHA-520 Document Title PANDA Transient Tests M3 & M4 Integral System Test Procedure PSI internal document Revision Status Approval / Date Rev.
Prepared / Revised by P-PM G-PM G-SOR issue Date Remarks Wl. Q~er 6kW 3.Torbeck 22SEP/995 YS^"
O C. Aubert
'lA is-$$
- 21. Sen 95
/cee-ongf) tt-W 9601230373 960117 PDR ADOCK 05200004 A
1 F
ALPHA-520 Seite 2
Controlled Copy (CC) Distribution List l
Note: Standard distribution (cf. next page) is non-controlled CC Holder CC List Entry Return / Recall No.
Name, Affiliation Date Date 1
Betriebswarte date of issue
Regetnerung TM-42-95-20
..fumC PAUL SCHERRER INSTITUT ALPHA 520-0 PANDA Transient Tests M
Tlel M3 & M4 Integrtal System Test Procedure Autoren/
C. Aubert 12.09.1995 Autorinnen Abstract This report details the procedure for conducting PANDA transient tests M3 and M4 as specified by GE document 25A5764 Rev.1.
All test phases are described in order to allow PANDA operation during preconditioning processes and test phases.
i i
i i
1 Veneiler Abt.
Empfinger/ Ernpfingennnen Expl.
Abt.
Enpiinger/ Empfangennnen Expl.
Expl.
42 G. Yadigaroglu 1
GE at PSI Bibfothek G. Varadi J. Torbeck / G. Wingate 1
C. Aubert 1
A.Arretz 1
Resene 5
T. Bandurski 1
J. Dreier 1
GE San Jose Total 20 J. Healzer 1
1 M. Hoggenberger 1
distribution at GE to J.R.
m 28 S. Lomperski 1
Fitch, T.R. Mc Int >Te, B.S.
fl.J. Strassberger 1
Shiralkar.
Beilagen JE. Torbeck, DRF No. T10-00005)
ALPHA-Dokumentation 2
infomatonsiste Betriebswarte 1
D 1
2 3l 4 5
8 Visum AbtAabodetung-
+'
ALPHA-S20 0 Page 4 PANDA Transient Tests M3 & M4 Integral System Test Procedure 00 Introduction 01 Test Configuration and initial Conditions 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 i
30 Suppression Chambers Setup 31 Water Fi!!ing 1
32 Gas Space Heating 33 Pressurization 40 GDCS Heating 41 Gas Space Heating 42 Water Filling 43 Pressurization 50 PCC1 Poo: Setup i
51 Water Filling 60 PCC2 Pool Setup 61 Water Filling 70 PCC3 Pool Setup 71 Water Transfer from GDCS Tank 72 GDCS Pressurization 80 Drywells Setup 81 Gas Space Heating 82 Pressurization
t k
ALPHA-520-0 Page5 90 RPV Initial Conditions Setup for Test 91 RPV Conditions Adjusting 100 Test Conditions Setup 101 PCC1 PoolConditions Adjusting 102 PCC2 Pool Conditions Adjusting 103 PCC3 Pool Conditions Adjusting 104 SCs Pools Conditions Adjusting 105 SCs Gas Space Conditions Adjusting 106 GDCS Conditions Adjusting 107 DWs Conditions Adjusting 110 Test 111 Data Recording 112 RPV Conditions Adjusting 113 Configuration Setup and Test initiation 120 End of Test 121 End of Data Recording 122 Facility Snut Down 200 Checklist 1
+
s
/
ALPHA-520-0 Page 6 00 Introduction The following procedure describes all test phases for Transient Tests M3 and M4, including preconditioning processes. Assuming that the starting point for the preconditioning is an empty facility at atmospheric conditions, this procedure gives sequences of processes, which do not need to be stricidy followed during the preconditioning process, at the discretion of Test Engineer. Required phases are listed in the Checidist and must be recorded when conducted.
The current procedure gives guidance on how to proceed to bring PANDA to the required initial i
test corxftions for a extreme case (from a cold and empty facility). The order of preconditioning sequences may be modified if needed, and single phases may be adapted to the actual conditions. Heating power indicated in psc0iGMing phases are theoretical and considered as basis for time estimation; the given values correspond to the highest heater performances.
Due to PSI electrical power limitation or modification in preconditioning process, the heating power may be reduced. However, the forseen preconditioning process is to start with the Suppression Chambers conGt;0ning after the facility has been set ready for operation. It continues with the GDCS tank, all PCC condenser pools and the Drywell setup. Just before test initiation, the RPV is setup to satisfy the required initial conditions. The test is then conducted during 20 hours2.314815e-4 days <br />0.00556 hours <br />3.306878e-5 weeks <br />7.61e-6 months <br /> under automatic power control and without any operator action. A time estimation for the preconditioning of an empty and cold facility is grven for each component in the following table.
Applicable specifically to these two tests M3 and M4, thic procedure will be used as basis for the Transient Test M7. A separate procedure will be used for test M7, which is actually an 7
adaptation of the current procetre. Major modifications for M7 concem the Drywell Setup.
Test Plan Specifications are descrbed in the GE document 25A5764 REV.1.
Ngin; - The temperatures are given in Kelvin and also indicated in 'C for the PANDA operation.
j
- Key parameters or key actions are indicated in dark frames to make reading easier during PANDA operation.
Time EstimatiQn Phase Proconditioning Phases time n'
10 Initial Alignment not estimated l
20 RPV Setup for Vessel Preconditioning 4.0
[ hour]
30 Suppression Chambers Setup 12.2
[ hour]
40 GDCS Heating 1.7
[ hour) 50 PCC1 Pool Setup 2.3
[ hour) 60 PCC2 Pool Setup 2.3
[ hour) 70 PCC3 Pool Setup 2.3
[ hour]
80 Drywells Setup 0.9
[ hour]
90 RPV initial Conditions Setup for Test not estimated 100 Test Conditions Setup not estimated 110 Test 20.0
[ hour]
10 to 100 Duration for Preconditioning 25.7
[ hour]
10 to 110 Duration for the whole Test 45.7
[ hour]
Note:
Duration of the phases n' 10,90 and 100 cannot be estimated; a certain time will be needed to complete these phases, it should not exceed a couple of hours.
a ALPHA-520-0 Page 7 01 Test Configuration and initial Conditions The configuration for the Transient Tests includes the RPV, Suppression Chambers, Drywells, GDCS, all PCC condensers and their respective pools; the IC condenser and the IC Pool are not part of the test configuration. It is also worth to note that the Equialization Lines connecting both Wetwells to the RPV are closed. A detailed description of the required configuration is given in the above mentioned GE document " Test Plan Specification".
An overview of the test configuration is summarized in the list of Test Initial Conditions given in the following. Defined for all components involved for Transient Tests, these initial Conditions described in the above mentioned GE document are listed below with the respectrve tolerances.
Note: The current procedure is based on the values given in that Test initial Conditions List; evaluaban of parameters used during the process are calculated automatically in order to be updated when Initial Conditions are modified.
Iest initial Conditions List RPV (V.RP)
-Total Pressure MP.RP.1 =
295 [kPa) 4 [kPa)
- Mean Fluid Temperature T nj(RP) =
406 [K) 2 [K)
- Local Fluid Temperature MTF.RP.1 5 = T nf(RP) 2 [K)
12.7 [m]
020 [m]
Drywell 1 and 2 (V.D1 - V.D2)
Air Partial Pressure 13 [kPa) 2 [kPa)
- Mean Gas Temperature T n_o(D1) =
404 [K]
i 2 [K)
T n_o(D2) =
404 [K]
2 [K)
- Local Gas Temperature MTG.D1.1 6 = T% c(D1) 2[K)
MTG.D2.1 6 = T no(D2) 2 [K)
Water Level MLD1 =
0 [m]
0.10 [m]
ML.D2 =
0 [m]
0.10 [m]
Suppression Chamber 1 and 2 (V.S1 - V.S2)
-Total Pressure MP.S1 =
285 [kPa) 4 [kPa)
MP.S2 =
285 [kPa) i 4 [kPa)
Mean Gas Temperature Tm n_o(S1) =
352 [K) i 2[K)
Tm n o(S2) =
352 [K) 2[K)
Local Gas Temperature MTG.S1.1 6 = T no(S1) 2[K)
MTG.S2.1. 6 = T% e(S2) 2[K)
Mean Water Temperature T. n w(S1) =
352 [K) 2[K)
T. n.w(S2) =
352 [K) 2[K)
- Local Water Temperature MTL.S1.1 6 = T n_w(S1) 2[K)
MTL.S2.1 6 = T n_w(S2) 2[K)
- Water Level MLS1 =
3.8 [m]
0.10 [m]
ML.S2 =
3.8 [m]
0.10 [m]
ALPHA-520 0 Page 8
~ Test initial Conditions List (cont'd)
GDCS (V.GD)
-Total Pressure MP.GD =
294 [kPa) 2 4 [kPa)
- Mean Fluid Temperature T,n n_p(GD) =
333 [K) 2 [K)
- Local Fluid Temperature MTF.GD.1.. 7 =
T,n n_F(GD) 2 [K)
- Water Level ML.GD =
0 [m]
0.10 [m]
PCC1,2 and 3 Pools (V.U1 - V.U2 - V.U3)
-Total Pressure
- MP.ENV =
97 [FPa)
- Mean Water Temperature
- T%w(U1) =
372 [K) 2[K]
' T,n ny(U2) =
372 [K) 2 [K)
T, n.w(U3) =
372 [K) 2 [K)
- LocalWater Temperature h
..U1.1.. 7 =
T,n..n_w(U1) 2 [K)
MTL.U2.1.. 7 =
T,n..n_w(U2) 2 [K)
MTL.U3.1. 7 =
T,n..n_w(U3) 2 [K)
Water Level ML.UI =
4.4 [m]
020 [m]
ML.U2=
4.4 [m]
020 [m]
ML.U3 =
4.4 [m]
2 020 [m]
Ngig;
- The pressure and temperature defined for the PCC Pools correspond to saturated conditions of the environment; values given above correspond to common atmospheric conditions.
1
d i
ALPHA-520-0 Page 9 10 initial Alignment Before starting any preconditioning process, the facility is set into a specific state, which establishes operations from the control room. The configuration is set in order to avoid any unintentional hardware manipulation during tasting or preconditioning. Data Acquisition and Control System must be property initiated and brought into operation. Valves are alignod in accordance to STARTUP Status, automatic heat power regulation files are loaded and as the last preparation phase, the auxiliary water system is filled to allow pumps operation.
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.
11 Control System and DAS Setup
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lhTG.AWQNWS.? *.J>W:Yhf5fWf."
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- w :;emy,y wsp3>wpirsved f.,
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.M M.$4 W'M.F.2 ' K,M3fn@l*Wh -MY-g, 'M.Tg%.} ",,',[.)j,N.
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> k., ': 9
.Jl'
'. ".. : - i..ii %,'.
Record on attached checidist 12 Valve Alignment....
, ec.. 9
{ '; 4.]
.f%.Q!>~.l'q W?Md'[k'+M W'T}f?&
- - L:. " '.
.,- -. ; a 2.
- ...... ;.: c Record on attached checklist 4
13 General Facility Configuraton Check W 1 1. N T i, -' '" ? T " S T 7 3 T E '!
- N f ~ ~" A 4
i Record on attached checklist i
14 Prepare Automatic Heat Power Regulation
'~:
b S f - l ' :-Y.
~ W5kf. y..ll Record on attached checklist 15 Auxiliary Water System Filling
- Fill the Auxiliary Water System i
16 instrument / Zero Check EChadt M M Transmitter zero check and DAS reading check according to the actual facility state, recording on DAS-Reading Hard4opy and Trending Plots.
Record on attached checidist
b ALPHA-520
- Page 10 20 RPV Setup for Vessel Preconditioning As the heat source for the whole preconditioning process, the RPV must be capable of producmg steam for vessel heating or provxing 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 venting to the atmosphere. Not all air is purged at this ternperature, but that does not affect the vessels preconditioning. Pure steam condmons are only required for the tests.
Then the RPV is heated to about 440K to supply the auxiliary water system heat exchanger.
The RPV water level set before preconditioning to anbcpate evaporation occuring during heating by steam injection; it should reach the required Tests water level at the end of the preconditoning process. However in any case it must be lower than h main steam lines inlet to avoid water hammer.
21 Water Filling 21.0 Check RPV Parameters Assumption:
- Water Level MLRP.1 =
0.0 [m]
M(RPV-water) =
0.00 [ ton]
21.1 Supply water until water reachs level equal to 12,7 [m]
Vent Air to the Atmosphere
- Open valve CC.RPV Auxiliary water system operation Pump MP. BOD On MV. BOD =.
2.0 [l/s]
M(RPV-water) = 15.00 [ ton]
77 y.y*y : ay
= - -
2
> time
7500 [sec]
Fill preheater heating side with water 3
- Open valve CB.HRH, CB.HFH 212 Check RPV Parameters
- Water Level MLRP.1 =
12.7 [m]
22 Heating / Purging 22.0 Check RPV Parameters Assumptions:
-Total Pressure MP.RP.1 =
101 [kPa) 10 [*C]
-Local Fluid Temperature MTF.RP.1.. 5 =
283 [K)
=
10 [*C]
- Structure temperature MTI.RP.1.. 3 =
283 [K]
=
- Water Level MLRP.1 =
12.7 [m]
22.1 Heat until temperature equals 373
[K)
Heaters On MW.RP.7 = 1500 'kW)
Y l
ALPHA-520 0
'o Page 11 M(RPV-water) = 15.00 [ ton]
> AO
5.67 [GJ)
M(RPV-struct) =
8.00 [ ton]
> AQ
0.19 [GJ)
> AOtot
5.86 [GJ)
> time
3907 [sec) 7 v ~ " c. Q.g,gg hih%hh Note:
- Temperature corresponding to the heat exchanger operation: SC's water filling M(RPV-water) = 15.00 [ ton]
> AQ
428[GJ]
M(RPV-struct) =
8.00 [ ton]
> AQ
027 [GJ)
> AQtot
4.56 [GJ)
> time
3038 [sec)
Heater Off 22.2 Check RPV Parameters
-Total Pressure MP.RP.1 =
746 [kPa) (Psat) 168 [*C]
-Local Fluid Temperature MTF.RP.1.. 5 =
441 [K)
=
168 [*C]
- Structure temperature MTI.RP.1.. 3 =
441 [K)
=
- Water Level MLRP.1 =
14.1 [m]
M(RPV-water) =
15.00 (ton) 30 Suppression Chambers Setup The Test initial Conditions require a collapsed water level in both Suppresson 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 teTicgenscus temperature of 352K for the pool water as well as for the gas space. The total pressure, considering saturated conditions, is at 285kPa, which correspond to an air partial pressure of 240kPa.
The Suppression Chambers Setup starts with water filling and pool conditioning (phase n' 31), continues with gas space heating by steam infecton keeping i bar air partial pressure inside the vessels (phase n* 32). The total pressure is then setup by injecting air with the aux 8iary air system (phase n' 33). Phase n' 33 is performed in parallel with phases n' 31 and 32.
31 Water Filling 31.0 Check SCs Parameters Assumptions:
-Total Pressure MP.S1 =
101 [kPa)
MP.S2 =
101 [kPa) 10 [*C) i
- Local Water Temperature MTLS1.1.. 6 =
283 [K)
=
10 [*C]
MTLS2.1.. 6 =
283 [K)
=
- Water Level ML.S1 =
0 [m]
ML.S2 =
0 [m]
i 31.1 RPV Setup for Heat Exchanger Operation Check RPV Parameters
-Total Pressure MP.RP.1 =
746 [kPa) (Psat) 168 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
441 [K)
=
14.1 [m]
Heaters On MW.RP.7 = 1500 [kW)
ALPHA 520-0 Page 12 31.2 Supply water until water reachs level equal to 3.8
[m]
Auxiliary water system operation Pump PC.HFH On Setup controlvalve CC. BHA g hih. 2 % - M i M 2 G %t W W iffs M S CC.BCA MTL.BCA =
max [K) i
- Open valve CB.S1L Pumo PC. BOD On MV. BOD =
2.1 [l/s]
?';;%%y k 1~P2 ;
M(S1-water) = 42.50 [ ton]
19E A.... n MR 'W M(S2-water) = 42.50 [ ton]
M(TSL-water) =
7.10 [ ton]
=> time = 43857 [sec)
- Close valve CB.S1L Pump PC. BOD Off MV. BOD =
0.0[l/s]
Pump PC.HFH Off Heater Off 31.3 SCs Parameters 79[*C]
-Mean Water Temperature T,n%w(S1) =
352 [K]
=
79[*C]
T,n%w(G2) =
352 [K)
=
-Wate Level MLS1 =
3.8 [m]
MLS2 =
3.8 [m]
32 Gas Space Heating 32.0 Check SCs Parameters Assumptions:
-Total Pressure MP.S1 =
162[kPa]
MP.S2 =
162 [kPa) 10 [*C]
- LocalGas Temperature MTG.St.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.S21.. 9 =
283 [K]
=
32.1 RPV Setup for Steam injection Check RPV Parameters
-Total Pressure MP.RP.1 =
746 [kPa) (Psat) 168 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
441 [K]
=
14.1 [m]
Heaters On MW.RP.7 = 1500 [kW) 322 Steam injecten
- Open valve CB.S1S, CB.S2S
> 4T
69 [K]
M(SCs-struct) =
72.7 [ ton]
> AO
2.52 [GJ)
M(steam) = 1095 [kg)
=> time = 1678.8 [sec)
- Close valve CB.S1S, CB.S2S Heater Off Check RPV Parameters
ALPHA-5204 Page 13
-Total Pressure MP.RP.1 =
746 [kPa) (Psat) 168 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
441 [K)
=
13.1 [m]
32.3 Check SCs Parameters
-Total Pressure MP.S1 =
207 [kPa]
MP.S2 =
207 [kPa) 79 [*C]
- Mean Gas Temperature T%o(S1) =
352 [K]
=
79 ['C]
T%o(S2) =
352 [K)
=
79 [*C]
- Mean Water Temperature T%w(S1) =
352 [K]
=
79 [*C]
T%w(S2) =
352 [K]
=
- Water Level MLS1=
3.8 [m]
MLS2 =
3.8 [m]
33 Pressurization 33.0 Check SCs Parameters
-Total Pressure MP.S1 =
207 [kPa)
MP.S2 =
207 [kPa]
33.1 Air injection until total pressure reachs 285
[kPa]
Auxiliary air supply system operation Setup control valve CC.80G2 MM. BOG = max
- Open valve CB.S1G, CB.S2G, CB.80G M(alr) =
360 [kg]
> time
12800 [sec)
- Close valve CB.S1G, CB.S2G, CB.B0G 332 Check SCs Parameters
-Total Pressure MP.S1 =
285 [kPa)
MP.S2 =
285 [kPa) 79 [*C]
- Mean Gas Temperature T n_o(S1) =
352 [K]
=
79 [*C]
T n_o(S2) =
352 [K)
=
79 [*C]
- Mean Water Temperature T n_w(S1) =
352 [K)
=
79 [*C]
T n_w(S2) =
352 [K]
=
- Water Level ML.S1 =
3.8 [m]
ML.S2 =
3.8 [m]
40 GDCS Heating The Tests Initial Conditions require a collapsed water level in the GDCS tank of 10,7m above the PANDA heater bundle, corresponding to a water level of 0,0m from the bottom of the tank taking into account a full GDCS Retum Line. The required temperature is a homogeneous temperature of 333K for the whole tank, which is achieved by filling with water up to approximately 5m at the required temperature and then draining the tank. The total pressure, considered in saturated conditions, is in equilibrium with the Drywells at 294kPa, which correspond to an air partial pressure of 274kPa.
The GDCS Setup starts with structure heating by steam injection (phase n' 41),
continues with water filling and pool conditioning, while keeping the vessel isolated, the
t ALPHA-520-0 Page 14 air is not vented to the atmosphere as long as the total pressure is lower than 10 bars (phase n* 42). The total pressure is then adjusted by injecting air through the auxiliary air system or by venting air to the atrnosphere (phase n' 43). That last phase is performed after water has been drained and transferred to the PCC pools.
41 Gas Space Heating 41.0 Check GDCS Parameters Assumptions:
-Total Pressure MP.GD =
101 [kPa]
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[m]
41.1 RPV Setup for Steam injection Check RPV Pararneters Total Pressure MP.RP.1 =
746 [kPa) (Psat) 168 ['C]
Local Fluid Temperature MTF.RP.1.. 5 =
441 [K]
=
- Water Level MLRP.1 =
13.1 [m]
Heaters On MW.RP.7 = 1500 [kW)
Note: The RPV temperature must be reduced for the GDCS water filling operation (T=> 436K see 41.2 & 42.1) 412 Steam injection
- Open valve.
CB. GDS
> AT
50 [K]
f ' if.p/..
j,jg;j m
M(GD-struct) =
5.00 [ ton]
> AO
0.13 [GJ)
M(steam) = 54.6 [kg)
> time
84 [sec]
- Close valve CB. GDS Heater Off Check RPV Parameters
-Total Pressure MP.RP.1 =
669 [kPa) (Psat) 163 ['C]
- Local Fluid Temperature MTF.RP.1.. 5 =
436 [K]
=
- Water Level MLRP.1 =
12.9 [m]
41.3 Check GDCS Parameters
-Total Pressure MP.GD =
121 [kPa) 60 [*C]
-Local Fluid Temperature MTF.GD.1.. 7 =
333 [K]
=
60 ['C]
- Structure temperature MTI.GD.1.. 6 =
333 [K)
=
Water Level MLGD=
0 [m]
Note: In order to get homogeneous temperature in GDCS, it is filled with water.
42 Water Filling 42.0 Check GDCS Parameters
-Total Pressure MP.GD =
121 [kPa]
60 [*C]
-Local Fluid Temperature MTF.GD.1.. 7 =
333 [K]
=
60 [*C]
- Structure temperature MTI.GD.1.. 6 =
333 [K)
=
- Water Level ML.GD =
0 [m]
J ALPHA 520-0
'a Page 15 42.1 RPV Setup for Heat Exchanger Operation Check RPV Parameters
-Total Pressure MP.RP.1 =
669 [kPa) (Psat) 163 [*C]
-Local Fluid Temperature MTF.RP 1.. 5 =
436 [K]
=
- Water Level MLRP.1=
12.9 [m]
)
Heaters On MW.RP.7 = 1500 [kW) 42.2 Supply water until water reachs level equal to 5.0
[m]
Auxiliary water system operation Pump PC.HFH On 60 [*C]
Setup control valve CC. BHA MTLBHA=
333 [K)
=
CC.BCA MTL.BCA =
max [K)
2.9 [l/s]
i
- Open valve CB.GDL A&Q.A tA FtC M M(GD-water) =
14.8 [ ton]
> time
5086 [sec]
- Close valve CB.GDL Pump PC. BOD Off Pump PC.HFH Off Heater Off 42.3 Check GDCS Parameters
-Total Pressure MP.GD =
626 [kPa) 60 [*C)
- Mean Fluid Temperature Tw(GD) =
333 [K)
=
60 [*C)
- Structure temperature MTI.GD.1.. 6 =
333 [K)
=
- Water Level ML.GD =
5.00 [m]
43 Pressurization 43.0 See phase n*72 Since the GDCS is full with water, it cannot be pressurized during the phase n' 43.
The GDCS pressurization is performed during phase n*72.
50 PCC1 Pool Setup The Tests initial Conditions for all PCC Pools are the same; water level from the top of the PANDA heater bundle is defined at 23,2m, which corresponds to a water level of 4,4m in the pools, in order to anticipate the effect of evaporation during preconditioning, water is filled up to 4,6 m. The end point temperature is near the saturation temperature for atmosphene pressure.
The pools Setup is performed as follows: water is filled at the highest possible temperature (phase n*51,61 & 71) and the temperature conditions are adjusted then by circulation through the auxiliary heat exchanger (phase n*101,102, & 103).
Note: Similar phases can be performed in parallel; pools can be connected and filled on the same time and water circulation can be also performed with conected pools.
1 s
ALPHA.520-0 Page 16 51 Water Filling 51.0 Check PCC1 Pool Parameters 10 ['C]
- Local Water Temperature MTL.U1.1.. 7 =
283 [K)
=
Water Level ML.U1 =
0 [m]
51.1 RPV Setup for Heat Exchanger Operation Check RPV Parameters
-Total Pressure MP.RP.1 =
669 [kPa) (Psat) 163 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
436 [K)
=
12.9 [m]
Heaters On MW.RP.7 = 1500 [kW)
- rp4 g;.:7 l.
J-
> AT
11.0 [K) Hojr;
- Temperature corresponding to the heat exchanger operation: PCC1 Pool water filling MP.RP.1 =
870 [kPa) ML.RP.1 = 132 [m] M(RPV-water) = 15.00 [ ton)
>AQ
0.08 [GJ) M(RPV-struct) = 8.00 [ ton)
> AO
0.04 [GJ)
> AQtot
0.09 [GJ]
> time
59 [sec) 51.2 Supply water until water reachs level equal to 4.6 [m] Auxiliary water system operation Pump PC.HFH On 102 [*C] Setup control valve CC. BHA MTLBHA = 375.5 [K) = CC.BCA MTLBCA = max [K) l Pump PC. BOD On MV. BOD = 1.6[l/s) l - Open valve CB.U1L l 3 . l e; 7,, 7 7,- li-M(U1-water) = 13.35 [ ton)
> time
8345 [sec] - Close valve CB.U1L l Pump PC. BOD Off Pump PC.HFH Off Heater Off 51.3 Check PCC1 Pool Parameters 99 ['C] - Mean WaterTemperature T.np(U1) = 372 [K) = - Water Level MLU1= 4.60 [m] 1 1 +
i ~ ALPHA-520 0 Page 17 60 PCC2 Pool Setup t For PCC2 Pool Setup refer to description of pools conditioning in phase n*50. 61 Water Filling 61.0 Check PCC2 Pool Parameters 10 [*C] Local Water Temperature MTLU2.1.. 7 = 283 [K) = - Water Level MLU2 = 0 [m] 61.1 RPV Setup for Heat Exchanger Operation Check RPV Parameters -Total Pressure MP.RP.1 = 870 [kPa] (Psat) 174 [*C] - Local Fluid Temperature MTF.RP.1.. 5 = 447 [K) = - Water Level MLRP.1 = 132 [m] Heaters On MW.RP.7 = 1500 [kW) 4 E 612 Supply water until water reacns level equal to 4.6 [m] Auxiliary water system operation Pump PC.HFH On 102 [*C] Setup control valve CC. BHA MTLBHA = 375.5 [K) = CC.BCA MTLBCA = max [K] ] Pump PC. BOD On MV. BOD = 1.6 [l/s] - Open valve CB.U2L k-. ;c.. Mx e n G l 7 (E M(U2 water) = 13.35 [ ton]
> time
8345[sec) - Close valve CB.U2L Pump PC. BOD Off Pump PC.HFH Off Heater Off 61.3 Check PCC2 Pool Parameters 99 [*C] - Mean Water Temperature T..n_w(U2) = 372 [K] = - Water Level MLU2 = 4.6 [m] 70 PCC3 Pool Setup For PCC3 Pool Setup refer to desenption of pools conditioning in phase n*50. This phase is actually for the water transfer from GDCS to PCC3 pool; the water used to heat the GDCS tank. After water has been drained, the GDCS is pressurized by air injection (phase n'72). 4
s ALPHA-520-0 Page 18 71 Water Transfer from GDCS Tank 71.0 Check PCC3 Pool Parameters 10 [*C] Local Water Temperature MTLU3.1.. 7 = 283 [K) = Water Level ML.U3 = 0 [m] Check GDCS Parameters Total Pressure MP.GD = 626 [kPa) 60 [*C] - Mean Fluid Temperature T,n ny(GD) = 333 [K) = 60 [*C] Structure temperature MT1.GD.1.. 6 = 333 [K] = Water Level MLGD= 5.00 [m] 71.1 RPV Setup for Heat Exchanger Operation Check RPV Parameters -Total Pressure MP.RP.1 = 870 [kPa] (Psat) 174[*C] -Local Fluid Temperature MTF.RP.1.. 5 = 447 [K] = Water Level ML.RP.1 = 13.2 [m] Heaters On MW.RP.7 = 1500 [kW)
- MTF.RP.1.. 5 =
444 [K]
> AT
-3.0 [K) 171 [*C] = Note:
- Temperature corresponding to the heat exchanger operation: water heating from GDCS up to 373K 71.2 Supply water until water reachs level equal to 4.6
[m] Auxiliary water system operation Pump PC.HFH On 102 [*C] Setup controlvalve MTL. BHA = 375.5 [K] = MTL.BCA = max [K] Pump PC. BOD On MV. BOD = 1.60 [l/s] - Open valve CB.U3U, CB.GDL 4,i. 2 L.. W, T N M(U3-water) = 13.35 [ ton]
> time
8345 [sec] Close valve CB.U3U, CB.GDL Pump PC. BOD Off Pump PC.HFH Off Heater Off 71.3 Check PCC3 Pool Parameters 99 [*C] -Mean Water Temperature T,n w(U3) = 372 [K] = Water Level MLU3 = 4.60 [m] Check GDCS Parameters -Total Pressure MP.GD = 122 [kPa) 60 [*C] - Mean Fluid Temperature T,n nj(GD) = 333 [K] = 60[*C] - Structure temperature MTI.GD 1.. 6 = 333 [K] = - Water Level MLGD= 0.10 [m] Check RPV Parameters -Total Pressure MP.RP.1 = 814 [kPa) 171 [*C] Local Fluid Temperature MTF.RP.1.. 5 = 444 [K) = - Water Level MLRP.1 = 13.1 [m]
ALPHA-52CH) Page 19 72 GDCS Pressurization 72.0 Check GDCS Parameters -Total Pressure MP.GD = 122 [kPa) 72.1 Air injection until total pressure reachs 294 [kPa) Auxiliary air supply system operation Setup controlvalve CC. BOG.2 MM. BOG = max - Open valve CB.GDG, CB.B0G B b.'W 39BBE Niid M(alr) = 28 [kg)
> time
945 [sec) - Close valve CB.GDG, CB. BOG 72.2 Check GDCS Parameters -Total Pressure MP.GD = 294 [kPa) - Mean Fluid Temperature T,n nj(GD) = 333 [K] Water Level ML.GD = 0.1 [m] 80 Drywells Setup The nominal Drywell condition is no water; the atmosphere is a mixture of steam with a small amount of air. The total pressure considered at saturated condition is defined at 294kPa, which corresponds to an air partial pressure of 13kPa. The required temperature being homogeneous in the whole gas space, is defined at 404K. The Drywells Setup consists of steam injection to heat the gas space (phase n' 81) and of a depressurization by venting to atmosphere (phase n' 82). In order to get homogeneous temperature in the whole vessel, air is purged during phase n*81 and an amount of about 20kg of air is injected to the Drywells in order to satisfy the required air partial pesst.re of 13kPa. During the heating process, the RPV, used as steam source, is cooled down in order to draw near to the required test initial conditions - heater power is controlled in order to decrease the RPV temperature. 81 Gas Space Heating 81.0 Check Drywells Parameters Assumptions: Total Pressure MP.D1 101 [kPa) MP.D2 101[kPa) 10 [*C] - Local Gas Temperature MTG.D1.1 6 = 283 [K) = 10 [*C] MTG.D2.1.. 6 = 283 [K] = 10 [*C] - Structure temperature MT1.D1.1.. 9 = 283 [K] = 10 [*C] MTI.D2.1 9 = 283 [K] = - Water Level ML.D1 = 0.0 [m] ML.D2= 0.0 [m] 81.1 Connect Drywells to all PCC Condensers Open valve CB.P1 F, CB.P2F, CB.P3F 81.2 RPV Setup for Steam injection Check RPV Parameters Total Pressure MP.RP.1 = 814 [kPa) 171 [*C] Local Fluid Temperature MTF.RP.1 5 = 444 [K] = Water Level ML.RP.1 = 13.1 [m]
i ALPHA-520-0 Page 20 Heaters On MW.RP.7 = 1500 [kW) 81.3 Steam injection Vent Valve Opening for Air Purging - Open valve CC.BUV, CB.D1V, CB.D2V - Open valve CB.D1S, CB.D2S y, J $jlpf _G/' jrjy
> AT
90 [K] Q';.,_ f,;;. A: 44f(9,y g, l ..{ y.{ ;. -I @l M(DWs-struct) = 48.9 [ ton]
> AO
221 [GJ) M(DWs-steam) = 98[kg)
> AO
0.26 [GJ]
> AQtot
2.47 [GJ) M(steam) = 961 [kg)
> time
1645 [sec) Vent valves are closed when temperature has reached 373K and seems steady 2:_ ; ;.: N ;- p n 3.y.gg; qqp 81.4 Continue steam injection kh Y WE%p.g,ye. $ M
> AT
31 [K] a;p.:;. +2 g1 M(DWs-struct) = 48.9 [ ton]
> AO
0.76 [GJ] M(DWs-steam) = 182 [kg)
> AO
0.43 [GJ)
> AQtot
1.20 [GJ) M(steam) = 331 [kg)
> time
797 [sec) Close valve CB.D1S, CB.D2S Heater Off Note: The RPV cooling down energy corresponds to 2,55 GJ, the duration of that steam injection process might be overestimated. 81.5 Check RPV Parameters -Total Pressure MP.RP.1 = 295 [kPa] 133[*C] - Mean Fluid Temperature T, r(RP) = 406 [K] = - Water Level ML.RP.1 = 12.6 [m] Check Drywells Parameters -Total Pressure MP.D1 281[kPa] MP.D2 281 [kPa) 131 [*C] - Local Gas Temperature MTG.D1.1.. 6 = 404 [K) = 131 ['C] MTG.D2.1.. 6 = 404[K] = 131 ['C] - Structure temperature MTI.D1.1.. 9 = 404[K) = 131 [*C] MTI.D2.1.. 9 = 404 [K) = Check PCCs Parameters -Total Pressure MP.P1F = 281 [kPa) MP.P2F = 281 [kPa] MP.P3F = 281 [kPa] - Local Gas Temperature MTG.P1.1.. 9 = 372 [K) 99 [*C] = 99 [*C] MTG.P2.1.. 9 = 372 [K] = 99 ['C] MTG.P3.1.. 9 = 372 [K] =
i ALPHA-520-0 P:ge 21 82 Pressurization Both Drywells have been now purged to the atmosphere or to the PCC condensers; a certain amount of air have been vented to the PCCs, in order to satisfy the temperature equilibrium in the pools and the pressure equilibrium between Drywells and PCCs. The Drywell atmosphere is considered as pure steam and saturated, while the PCCs contain some air. Drywells and PCCs are pressurized by air injechon (phase n*82). 82.0 Check Drywells Parameters -Total Pressure MP.D1 281 [kPa] MP.D2 281 [kPa] 131 ['C] - Local Gas Temperature MTG.D i.1.. 6 = 404 [K] = 131 [*C] MTG.D2.1 6 = 404 [K) = 131 [*C] - Structure temperature MTI.D1.1.. 9 = 404 [K) = 131 [*C] MTI.D2.1.. 9 = 404 [K] = 82.1 Air injection until air partial pressure reaches 13 [kPa] 2 [kPa] a 1 Auxiliary air supply system operation Setup control valve CC. BOG.2 MM. BOG = max - Open valve CB.D1G, CB.D2G. CB. BOG - 5..;[%.&&? f>.j(h[h&' ?k F. + L w r u x ;%% M(air) = 20 [kg)
> time
741 [s6c] - Close valve CB. DIG, CB.D2G, CB. BOG 82.3 Check Drywells Parameters - Air Partial Pressure 13 [kPa] 2 [kPa) 131 ['C] - Local Gas Temperature MTG.D1.1.. 6 = 404[K) = 131 [*C] MTG.D2.1.. 6 = 404 [K) = 131 [*C] - Structure temperature MTI.D1.1 9 = 404[K) = 131 [*C] MTI.02.1.. 9 = 404 [K) = Check PCCs Parameters -Total Pressure MP.P1 F = 294 [kPa) I MP.P2F = 294 [kPa) MP.P3F = 294 [kPa] 99 [*C] - Local Gas Temperature MTG.P1.1.. 9 = 372 [K] = 99 [*C] MTG.P2.1.. 9 = 372 [K] = 99 ['C] MTG.P3.1.. 9 = 372 [K) = 90 RPV Initial Conditions Setup for Test After having used the RPV as heat source for the vessel preconditioning, it might be at conditions, which might differ from these required for test initiation; water level, pressure and temperature may need to be adjusted in order to satisfy the test initial conditions. However the whole preconditioning anticipates the final state; start conditions are defined in order to get RPV conditions after other vessel preconditioning close to the required test initial conditions for the RPV. Phase n' 91 is a parameter check, which will give basis for the adjusting of RPV conditions.
I \\ ALPHA-520 0 Page 22 91 RPV Conditions Adjusting 91.0 Check RPV Parameters Assumtions: -Total Pressure MP.RP.1 = 295 [kPa) 133[*C] - Mean Fluid Temperature T s,(RP) = 406 [K] = - Water Level MLRP.1= 12.6 [m] j 91.1 Adjust Test initial Conditions in RPV j Assuming saturated conditions and a negligeable air partial pressure, the pressure is set i by adjusting the temperature. Cooling is achieved by supplying cold water and/or by venting steam to the atmosphere. Heating is performed by using RPV heaters. Any required action is allowed to setup the RPV test initial conditions to match the required tolerances (ref. GE document " Test Plan Specification'). 100 Test Conditions Setup PANDA preconditioning has been now performed and its state is close to those required for the initiation; conditions out of tolerance must be adjusted to the defined values. Temperatures, pressures or water levels are set in order to anticipate the natural evolution; 4 values do not exceed the corresponding tolerances. The test condition setup starts with PCC Pools condition adjustments (phase n' 101, 102 & 103), which can be performed in parallel, continues with both Suppression Chambers (SCs) pools (phase n' 104), whose conditions are also adjusted in parallel, and with conditions ac' justing for the SCs gas space (phase n'105). The GDCS tank is then adjusted to its defined test initial condmions (phase n*106), before adjusting conditions in both Drywells (phase n' 107). All these phases are not defined in detail, allowing any required action to get the test initial conditions established. l 101 PCC1 Pool Conditions Adjusting 101.0 Adjust Test initial Conditions in PCC1 Pool Assuming saturated conditions at atmospheric pressure, the water temperature might be adjusted by water circulation through auxiliary heat exchanger; and due to evaporation, the water level might adjusted by supplying water. Any required action is allowed to setup the PCC pools test initial conditions according to the defined tolerances (ref. GE document ' Test Plan Specification"). All PCC pools conditions must be adjusted, that may be perfomed simultaneously by connecting the 3 pools together. 101.1 Check PCC1 Pool Parameters - Mean Water Temperature L ~. ~ r 1e -cwee e r er "'m I .. 1 '. 5 ; cN WfN^ + E ' O ?% 4 M 'T. ? = 9 - _ ~U l - Local Water Temperature j,,( [ ] N ' g g g f % J. g j [ g p p g ] - Water Level l Record on attached checklist i
ALPHA 520-0 Page 23 102 PCC2 Pool Conditions Adjusting 102.0 AdjustTestInitialConditionsin PCC2 Pool For PCC2 pool conditions adjusting refer to description of pool conditions adjusting in phase n*101. 102.1 Check PCC2 Pool Pararneters ? @b; 'c. y wf.5 ; ;.-' A P "? '. '.33 W :VWC ?. $.? - Mean Water Ternperature .a 6 %, ~..- T . Local Water Temperature "~ iM'7" .7 M.;...i ~ .i
- : ;,py;w
. y..p,y.- n.:, y. _ ..m ....n u,. . Water Level 2. Record on attached checklist 103 PCC3 Pool Conditions Ad,iusting } 103.0 Adjust Test initial Conditions in PCC3 Pool For PCC3 pool conditions adjusting refer to description of pool conditions adjusting in phase n*101. i 103.1 Check PCC3 Pool Parameters M ~ " 7 ,,ww.c y: x y d et % M W ?' M .Mean Water Temperature . ' -~
- . c <
~2 l 3* ' y;< fi ).. 4.; ;y; ;. ~ ,, '*QQL '. ':.f',. 'pj;,, % fy*: , : 'u' w. W - o e - Local Water Temperatur9 o-'- . M N U D $ ' C Y N_ U N NkMk - Water Level i Record on attached checidist t 104 SCs Pools Conditions Adjusting 104.0 Adjust Test Initial Conditions in Suppression Chamber Pools After the check of the water temperature and water level, reouired action to adjust the i conesponding parameters are supplying or draining water to satisfy the defined water level, I and water circulation through one or the other of the two auxiliary heat exchangers as required to adjust the desired temperature. Any action is allowed to setup the SCs pools test initial conditions according to the defined tolerances (ref. GE document " Test Plan Specification"). 1' 104.1 Check SCs Parameters ~ - Mean Water Temperature ..4< N;L kkdk Nd, & : ~Q-jf % fi.(}!) hit) - <*a *y.. v.- m : -le.ld. '_m. ; e.,W.M, g a;.~ ". . ~4./ J:. s.. - - Local Water Temperature - n.Gi:te>J &.... r.- h 'a J. - mu- .;.3 - Water Level - ?'.I'Ib NN DD D.. <;.r f.qqst:: O rc 9m ' y. e- ..r ; c. i. w.. E 3,.w._ :.3 s K. m
- x..,,
.y Record on attached checklist
ALPHA-520-0 Page 24 105 SCs Gas Space Conditions Adjusting I 105.0 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 (ref. GE document " Test i Plan Specification *). i 105.1 Check SCs Parameters L ~ 3%.. . x.. wg y ::D. n'y.'.w; w'- -TotalPressure %%. ' w y".Q[ : ..:4 7 1. a. j A.,..J:j > ' ?
- 4
-x e - Mean GasTemperature z. ; ;, p,s:7..:.~4., y:J ~ gg i; ......9 .u.,. yQ;L ': lc ' x.c . ;.[p e Q
- c..p y Q C.. M : % '. Q w?? %
.l....). M u; n-~;.*$ Ti g y.ru4.; W W y y ~ g :)v M 4 , o., 6-ga. - LocalGas Temperature 2 u ? J., . 2w. Record on attached checklist 4 106 GDCS Conditions Adjusting 106.0 AdjustTestinitialConditionsin 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 (ref. GE document " Test Plan Specification"). 106.1 Check GDCS Parameters p. 'l g.f 4./ * " ' ;
- r-
- m.,. e.*. i%- }* -Total Pressure
- j..g..-
q - Mean Fluid Temperature w ., a: ;wgwm 4.w. y n m (f .,. _ > p y, gy.. j y .p,.... ; z.
- ,. y
- Local Fluid Temperature ~ TD k.' ~ L V 3.D % M :I 3 D O ^ ' UfNiM'h -NDisAA.i - Water Level Record on attached checklist 4 107 DWs Conditions Adjusting 107.0 AdjustTestinitialConditionsin Drywells Assuming saturated steam / air mixture, the temperature and the pressure are separately d adjusted by steam and air injection. Any required action is allowed to setup the Dryweils test initial cor4Gv6s according to the defined tolerances (ref. GE document " Test Plan Specification").
ALPHA-5200 f, - Pzgo 25 f - 107.1 Check Drywells Parameters - Air Partial Pressure ~f W 4',U J ~ 'i E '~ i - Mean GasTemperature i. f - Local Gas Temperature l - Structure temperature - Water Level j Record on attached checidist i l l L. 110 Test The facility satisfies now the required test initial conditions and must be configured accordmg to the test configuration described in GE document ' Test Plan Specification". i Due to the relatively quick test initiation, data recordmg is started (phase n*111) before settmg the desired RPV conditions (phase n*112) and before settng the test g configuration (phase n*113). That last phase should not affect the PANDA conditions, but in order to assure test initial conditions satisfyng the defined tolerances, the duration of i-all these phases between the test configuration setup (phase n*113.1 to n' 133.9) and j the test initiation (phase n*113.10) should not exceed a few minutes (-5 min). After test initiation, the test initial conditions must be within the tolerances given in phases n*110 i and 112, in order to satisfy the acceptance criteria defined in the above mentioned GE j document. If test initial conditions do not satisfy the above menboned acceptance cntena, test is interrupted, the heat power is shut down (phase n* 122.0), vessel are j isolated (phase n' 122.1) and the procedure starts again with the Test Conditions Setup (phase n* 100). j Due to the excessive pressure differences between vessels during the preconditioning, ( the pressure difference transmitters lineup (valve in) must be performed after the facility has test initial conditions established; it is performed during test conhguration setup i (phase n*113.7). i 111 Data Recording j-S 111.0 Start Data Recording ( At least 20 hours after test initiation) y.Ly[.i h tid-f.'. d i j i Record on attached checidist I 111.1 1..i i' . r.. c. Record on attached checidist i 1 4 an.-. + -..,.. .-,-a-> ..n.. .e--
I i l ALPHA-52N) l Page 26 l l 112 RPV Conditions Adjusting 112.0 AdjustTestinitialConditionsin RPV Assuming saturated conditions and a negligeable air partial pressure, the required pressure is set by adjusting the temperature. Any required action is allowed to setup the RPV test initial conditions according to the defined tolerances (ref. GE document " Test Plan Specification"). 4 112.1 Check RPV Parameters pf j ; Qcg.[:? -Total Pressure % - J.:. #$. gl.3$k,y 'g,.;g ' .;_y 7 4 'c
- m Q MV ?. PJg;;g.t f:,Gf.,'W.; y
-Mean Fluid Temperature
- .d c'
.; qq:q . iv.. y t y%qy.L..;9::[ pnp u;,~ w,,'q' ;:+;.' &.p., N. ', q.
- M q.M
-Local Fluid Temperature ',( glc3 4. s - },..c;;.,..- ~ 1.E y -1... ' b yy. 3. ; 72 2.... g.,@p; cc -.., %"; -..*- - Water Level .. A...." s.- A. ; - ., - ww. -. Record on attached checklist 113 Configuration Setup and Test initiation 113.0 Setup Automatic Heat Power Regulation 4 p.; m. e; '.u,:...v t.gr y, .cng
- t. i.. y..
.-=. S a e m e==L, u; r 7- - - " s F' Record on attached checidist 113.1 Connect all Pools Together .. ~,y,, .,,g.. 3.g g ' u gia m m. i. a..:v,.y.. / a ~.: Record on attached checklist ..e 1132 Open GDCS Pressure Equialization lines .;.;...,cc. ....7. Record on attached checklist 113.3 Open Main Vent Lines v1 '. .) z u,: Record on attached checklist i 113.4 Open GDCS Return Line 2 O illi : d Record on attached checklist 113.5 Open PCC Vent Lines !"f. T.7. 3 & X J { M E T 5 ?j Record on attached checklist 113.6 Open PCC Condensate Lines Record on attached checklist 113.7 Instrument / Zero Check and Pressure Difference Transmitters Valve in ,, ;.. ~,_ s. .c.._... 7.,... .m... } dk} Record on attached checklist 113.8 Open Main Steam Lines .. wi f 9 . tom.a. ... :.s.. W 2:u%1 Record on attached checklist
ALPHA-5204 . Page 27 113.9 Print Valve Status Report two hours dur' the Test duration ~ Record on attached checidist 113.10 Test initiation ' t,i,1 ' j ("t g.g,j .( 's... ;i Record on attached checidist 113.11 Check Test initial Conddions - Acceptance Criteria Record on attached checidist 113.12 Test interruption if the Acceptance Criteria are not satisfied follow goto phase n' : 122.0 & 122.1 => phase n' 122.0 => phase n' 122.1 - Restart procedure with phase n' 100 (Test Conditions Setup) 120 End of Test At the end of 20 hours' data recording will be terminated and the test performances completed Phases n' 121 and 122 describe the end of test and the facuity shut down. 121 End of Data Recording 121.0 Stop Data Recording (cf DAS User's Guide) After 20 hours test data recording is terminated. t Record on attached checidist 121.1 ' ' ~ i 121.2 i Record on attached checidist l j 122 Facility Shut Down 122.0 Stop Heat Power Heater Off 122.1 Isolating Vessels - Close valve CB.MS1, CB.M2S 3' C8.P10, CB.P2C, CB.P3C CB.P1V, CB.P2V, CB.P3V CB.G RT.2, CB.GRT.1 CB.MV1, CB.MV2 CB.U1L, CB.U2L, CB.U3L 1222 Valve Alignment Set valve positions according to the valve SHUT DOWN status Printout valve status report - Compare to valve status for facility shut down 1 1
ALPHA-520-0 Page 28 200 Checklist Checklist Transient Test Number Completion of Procedure Date / Time Signatures j Phase n' Performer / Reviewer ) 11 12 13 14 ^ 16 101 j 102 103 104 105 106 107 111.0 111.1 112 113.0 113.1 113 2 113.3 113.4 113.5 11.1.6 113.? - 113.8 113.9 113.10 1 113.11 121}}