ML20096F431
| ML20096F431 | |
| Person / Time | |
|---|---|
| Site: | 05200004 |
| Issue date: | 11/14/1995 |
| From: | Aubert C PAUL SCHERRER INSTITUTE |
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| Shared Package | |
| ML20096F375 | List: |
| References | |
| ALPHA-521, NUDOCS 9601230386 | |
| Download: ML20096F431 (27) | |
Text
e*
k PAUL SCHERRERINSTITUT Document No.
ALPHA-521 Document Title PANDA Transient Tests M7 Integral System Test Procedure PSI Internal Document Revision Status Approval / Date Rev.
Prepared / Revised by P-PM G-PM G-SOR lssue Date Remarks Q [MV J. Torbeck G-gh (ers gmol 4
O C. Aubert A4->a -6 E 14 Nov 95 iv >, w e om.ll hok kDO!K 052 0004 A
ALPHA-521 Seite 2
Controlled Copy (CC) Distribution List Note: Standard distribution (cf. next page) is non-contro!!ed CC Holder CC Ust Entry Retum / Recall No.
Name, Affiliation Date Date 1
PANDA Betriebswarte date issued
w Jun
~
PAUL SCHERRER INSTITUT 95-21 f
ALPHA 521-0 PANDA Transient Tests M
TW M7 Integral System Test Procedure Autoren/
Autorinnen C. Aubert
- 14. November 1995 Abstract:
This report details the procedure for conducting PANDA Transient Tests M7 specified by GE document 25A5764 Rev.3.
All phases for PANDA operation during the preconditioning processes and the test phases are described.
t i
I l
Vertaler Abt Empl6nger/ C4ip..e Expt Abt.
Empfanger/ E i,iew..e Expt Expl 42 G. Yadigaroglu 1
G. Varadi 1
2 " ' ' " " " ;--
C. Aubert 1
A. Arretz 1
Reserve 5
T. Bandurski 1
J. Dreier 1
GE San Jose Total 20 J. Healzer 1
N 1E. L6e. k 1
M. Huggenberger 1
(for distribution at GE to J.R.
Sehen 32 S. Lomperski 1
Fitch, * " ?* '
. B.S.
HJ. Strassberger 1
Shiralkar, 6~. A. O. 9Me, Beilagen
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ALPHA-Dokumentation 2
T1000005) irtomwonsiste Betribswarte 1
D 1
2 3
4 5
8 9
A p,w h s., he cc.echc/
VsurnAbtAaborleitung:
si FG+2 9C-12 -is
I ALPHA-521-0 ALPHA-521-0 Page 4 Page 4 i
PANDA Transient Tests M7 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 Auxiliary Water System Filling 15 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 Gas Space Heating 42 Water Filling 43 Pressurization 4
50 PCC1 Pool Setup 51 Water Filling 4
60 PCC2 Pool Setup 61 Water Filling 70 PCC3 Pool Setup 71 Water Transfer from GDCS Tank 72 GDCS Pressurization 80 Drywells Setup 81 Drying Vessels 82 Pressurization r
f
oa ALPHA-521-0 ALPHA-521-0 g
Page 5 Page5 90 RPV Initial Conditions Setup for Test 91 RPV Conditions Adjusting 100 Test Conditions Setup 101 Adjusting SC Pools Condmons 102 Adjusting SC Gas Space Conditions 103 AdjustingGDCSCorditions 104 AdjustingDWConditions 105 Adjusting PCC1 Pool Conditions 106 Adjusting PCC2 Poni Conditions 107 Adjusting PCC3 Pool Conditions 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 Shut Down 200 Checklist b
l l
i ALPHA-5210 ~
ALPHA-521-0 '
L Page6' Page 6 s
00 Introduction i
The following procedure describes all ton,t phases for' Transient _ Tests M7, including l
precondiboning processes. Assuming that the starimg point for the preconditoning is an empty F
facility at atmospheric condibons, this procedure gives sequences of processes, which do not.
i j'
nood to be strickly followed during the precondiboning procoes, at the discretion of Test Engineer. Required phases are listed in the Checidist and must be recorded when conducted i
The current procedure gives guidance on how to proceed to bring PANDA to me requred j
initial test condibons for a extreme case (from a cold and empty facility). The order of precondiboning sequences may be modified if needed, and single phases may be adapted to.
the actual conditions. Heating power indicated in preconditioning phases is theoretical and l
+
j-considered as basis for time eshmation; the given values concepond to the highest heater 4
performances. Due to PSI electrical power limitation or modification in preconditioning j
process, the heating power may be reduced In any case, the foressen precondiboning process is to start with the Suppreesson Chambers conditioning after the facility has bee.' set ready for operation. It continues with the GDCS tank, all PCC condenser pools and the Drywells. Just before test initiation, the RPV is set up i.
to satisfy the required initial condsbons. The test is then conducted during 5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> under automatic power control and without any operator action.
i A time estimation for the precondiboning of an empty and cold facility is given for each component in the following table.
j Test Plan Specifications are described in the GE document 25A5764 REV.3.
p i
1
- Since temperatures are given in Kelvin in the Test Plan Specification and in *C in the j
Note:' whole PANDA DAS, they are indicated in both units in that current procedure.
Key pararnstars or key actions are indicated in dark frames to make reading easier during PANDA operation.
j Time Estimation Phase Preconditioning Phases time i
n' 10 initial Alignment not estimated 20 RPV Setup for Vessel Preconditiuning 5,8
[ hour]
l 30 Suppresson Chambers Setup 12,2
[ hour) i 40 GDCS Heating 1,6
[ hour) i 50 PCC1 Pool Setup 1,9
[ hour) 60 PCC2 Pool Setup 1,9
[ hour) 70 PCC3 Pool Setup 1,9
[ hour]
80 Drywels Setup not estimated
[
90 RPV Initial Conditions Setup for Test 0,3
[ hour]
_i l
100 Test Condibons Setup not estimated 110 Test 5,0
[ hour]
4 1
10 to 100 Duration for Proconditioning 25,3
[ hour) 10 to 110 Duration for the whole Test 30,3
[ hour)
M Duration of the phases n' 10,80 and 100 cannot be estimated, it should not exceed a couple of hours.
3 i
i
ALPHA-521-0 ALPHA-521-0
- Page 7 Page 7 01 Test Configuration and initial Conditions The configuration for the Transient Test M7 includes the RPV, Suppression Chambers, Drywells, GDCS, all PCC condensers and their respective pools; the IC condenser and the IC pool is not included to the Test configuration. The Equialization Lines connecting both Wetwells to the RPV are closed. A detailed description of the required configuration is given in the above mrintioned GE document ' Test Plan Specification".
/.n overview of the test configuration is summanzed in the list of Test Initial Condibons given in the following. Defined for all components involved for Transient Tests, these initial Conditions desenbod in the above mentioned GE document are listed below with the respective tolerances.
HQlE The current procedure is based on the values given in the Test initial Conditions List below.
Test initial Conditions List RPV (VElD
-Total Pressure MP.RP.1 =
131 [kPa) 4 [kPa)
- Mean Fluid Temperature Tr, n(RP) = I(MTF.RP.J)/ max 0) with j = 1 to 5 Tr, n(RP) =
380 [K) 2 [K]
-Local Fluid Temperature MTF.RP.1.. 5 =
Tr_,n n(RP) 2 [K)
12,7 [m]
0,20 [m]
Drvwell 1 and 2 (V.D1 - V.D21
- Air Partial Pressure MPG.D1.1 =
131 [kPa]
8 [kPa)
MPG.D2.1 =
131 [kPa) 8 [kPa)
- Mean Gas Temperature To, n(D1) = I(MTG.D1.j)/ max 0) with j = 1 to 6 Taf n(D2) = I(MTG.D2.j)/ max 0) with j = 1 to 6
- Tof n(D1) =
300 [K)
- To, n(D2) =
300 [K) i
- Local Gas Temperature MTG.D1.1.. 6 = Tof n(D1) 2 [K)
MTG.D2.1.. 6 =
To_,n n(D2) 2 [K)
Water Level MLD1 =
0[m]
0,10 [m]
ML.D2 =
0[m]
0,10 [m]
HQLC
- The temperature defined for the Drywells correspond to the room temperature; it might be different than the value indicated.
Suppression Chamber 1 and 2 (V.S1 - V.S2)
-Total Pressure MP.S1 =
131 [kPa]
4 [kPa]
MP.S2 =
131 [kPa) 4 [kPa]
- Mean Gas Temperature Tof n(S1) = I(MTG.S1.j)/ max (j) with j = 1 to 6 Tof n(S2) = I(MTG.S2.j)/ max (j) with j = 1 to 6 To, n(S1) =
352 [K) 2 [K)
To, n(S2) =
352 [K) 2 [K]
-Local Gas Temperature MTG.S1.1.. 6 = To, n(S1) i 2 [K)
MTG.S2.1.. 6 =
To,.,i(S2) 2 [K)
- Mean Water Temperature Tw, n(SI) = I(MTL.Sn.j)/ max (j) with j = 1 to 6 Twf n(S2) = I(MTL.S2.j)/ max (j) with j = 1 to 6 Tw, n(S1) =
352 [K]
2 [K]
Tw, n(S2) =
352 [K) 2 [K)
- Local Water Temperature MTL.S1.1 6 =
Tw, n(S1) i 2 [K)
M TLS2.1.. 6 =
Tw, n(S2) 2 [K]
- Water Level ML.S1 =
3,8 [m]
0,10 [m]
ML.S2 =
3,8 [m]
A 0,10 [m]
i l
[
ALPHA-5210 ALPHA-5210 Page 8 Page 8 s
Test initial Conditions List (cont'd)
GDCS N.GD)
-Total Pressure MP.GD =
131 [kPa) 4 [kPa)
- Mean Fluid Temperature Tr, n(GD) = I(MTF.GD.j)/ max 0) with j = 1 to 7 Tr_,n.=,(GD) =
333 [K) 2 [K]
Local Fluid Temperature MTF.GD.1.. 7 = Tr, n(GD) 2 [K)
-Watet Level MLGD=
0 [m]
i 0,10 [m]
PCC1. 2 and 3 Pools N.U1 - V.U2 - V.U3)
-Total Pressure
- MP.ENV =
97 [kPa)
- Mean Water Temperature Tw_,n n(U1) = I(MTLU1.J)/ max 0) with j = 1 to 7 Tw, n(U2) = I(MTLU2.j)/ max 0) with J = 1 to 7 Tw_,n n(U3) = I(MTLU3.1)/ max (i) with I = 1 to 19
- Tw, n(U1) =
372 [K]
+0/ -4
[K) l
- Tw, n(U2) =
372 [K)
+0/ -4
[K)
- Tw, n(U3) =
372 [K)
+0/ -4
[K)
- Local Water Temperature MTL.U1.1.. 7 =
Tw, n(U1) i 2 [K)
MTLU2.1.. 7 = Twf n(U2) i 2 [K)
MTLU3.1..19 =
- Tw_,
n(U3) 2 [K)
- Water Level ML.U1 =
4,8 [m]
i 0,20 [m]
ML.U2 =
4,8 [m]
0,20 [m]
MLU3 =
4,8 [m]
i 0,20 [m]
311C
- The pressure and temperature defined for the PCC Pools correspond to saturation values at usual atmospheric pressure at the test site.
l l
ALPHA-5210 ALDHA-521-0 Page 9 Page 9 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 property 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 operation.
Four different preparation phases are needed for the Transient Test M7: phase n*11 starting Control and Data Acquisition Systems, phase n*12 for the initialvalve setup, phase n*13 for the configuration checking and phase n*14 for auxiliary water system filling.
11 Control System and DAS Setup NYrNNm cN$$h h p$
& A n h?nNy 2.l$ & f f l
? : wgwgemkwstwwyuis my
@7 > -
~ '
~
N Mkeea%turtme N
.~
m...w4,.py J r& M'V:,P : '"' "[T h (
?'9 h w m W w w e n.-
14 /
a.
......A..
Record on attached checidist 12 Valve Alignment m
.~ '
,._s
.h. ;.. m. _ PIUMeerempdpum a#
ut. Am a _ n 2._
f.
- u.
- ~....
i Record on attached checidist 13 General Facility Configuraton Check I
'.TT.'. ~i ' ~E.. C O U. 7 L..
L M X M U i..T C' ""'
~~4 Record on attached checidist 14 Auxiliary Water System Filling
- Fill the Auxiliary Water System 15 Instrument /Zero Check 15.0 i f.' N~ " ? " W '
15.1 M MaAsfiiaanguascaisyWeWPksing@e wee emiiniamppm, emnewgg8M@$$
mademnerimunenessons anschect.ooonsn Record on attached checklist 1
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 venting to the atmosphere. Not a!! 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 heated to about 440K to supply the auxiliary water system heat exchanger.
The RPV water level is set before preconditioning to anticipate evaporation occuring during 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.
i I
l
ALPHA-521-0 ALPHA-521-0 Page 10 Page 10 21 Water Filling 21.0 Monitor RPV Parameters Assumphon.
4
- Water Level MLRP.1 =
0,0 [m]
M(RPV-water) =
0,00 [ ton) 21.1 Supply water until water reaches level equal to 12,2
[m]
Vent Air to the Atmosphere l
- Open valve CC.RPV Auxiliary water system operation Pump MP. BOD On MV. BOD =
2,0 [l/s]
3( 2 3 5..,7 :.x 3 - v
M(RPV-water) =
15,00 [ ton]
> time
7500 [sec)
Pump MP. BOD Off Fill preheater heating side with water
- Open valve CB.HRH, CB.HFH 212 Monitor RPV Parameters
}
- Water Level MLRP.1 =
12,2 [m]
22 Heating / Purging 22.0 Monitor 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]
=
12,2 [m]
j 22.1 Heat untiltemperature equals 373
[K)
800 [kW)
Y;
- h
?
- 1.h M(RPV-water) = 15,00 (ton]
> AQ
5,67 [GJ]
M(RPV-struct) =
8,00 [ ton]
>AO
0,36 [GJ)
> AQtot
6,03 [GJ]
> time
7539(sec]
222 Heat until ternperature equals 441
[K)
.. L 7 pyg f.g
> AT
68 [K]
.. m,yxx. s a a N_g.tg.;
- Temperature corresponding to the heat exchanger operation.
M(RPV water) = 15,00 [ ton]
> AQ
4.28 [GJ)
M(RPV-struct) =
8,00 [ ton]
> AQ
0,27 [GJ)
> AQtot
4,C6 [GJ)
> time
5696 [sec]
Heater Off
.J-
i ALPHA-521-0 ALPHA-521-0
- r Page 11 Page 11
. 22.3 Monitor RPV Parameters
-Total Pressure MP.RP.1 =
746 [kPa) (Psat) j
- Local Fluid Temperature MTF.RP.1.. 5 =
441 [K]
168 [*C]
=
t 168 ['C]
[
- Structure temperature MTI.RP.1.. 3 =
441 [K]
=
- Water Level MLRP.1 =
13,5 [m]
M(RPV-water) =
15,00 [ 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 i
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, is at 131kPa, which e
includes, considering saturated conditons, an air partial pressure of 86kPa. Since the total pressure is quite equivalent to the atmospheric pressure, the pressurization process consists in venting to the atmosphere.
The Suppressen Chambers Setup starts with water filling and pool condiboneg (phase n' 31),
continues with gas space heehng by steam infecnon keeping one bar air partial pressure inside the vessels (phase n' 32). The total pressure is then setup by ven9ng to the atmosphere (phase n' 33). Phase n' 33 is performed after phases n' 31 and 32 have been conducted 31 Water Filling 31.0 Monitor SCs Parameters Assumptons-
-Total Pressure MP.S1 =
101 [kPa]
MP.S2 =
101 [kPa]
10 [*C]
- Local Water Temperature MTLS1.1. 6 =
283 [K]
=
10 [*C]
i MTLS2.1.. 6 =
283 [K)
=
- Water Level ML.S1 =
0 [m]
MLS2 =
0 [m]
31.1 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters
-Total Pressure MP.RP.1 =
746 [kPa] (Psat) 168 ['C]
j
- Local Fluid Temperature MTF.RP.1.. 5 =
441 [K]
=
- Water Level MLRP.1 =
13,5 [m]
1 Heaters On MW.RP.7 = 800 [kW) 31.2 Supply water until water reaches level equal to 3,8
[m]
l Auxiliary water system operation Pump PC.HFH On Set up control valve CC. BHA i7 19 ; 14 i
'F-
~
CC.BCA MTLBCA =
max [K)
- Open valve CB.S1L P
2,1 [l/s]
M(S1-water) = 42,50 [ ton]
M(S2-water) = 42,50 [ ton]
M(TSL-water) =
7,10 [ ton]
- Close valve CB.S1L Pump PC. BOD Off MV. BOD =
0,0 [l/s]
Pump PC.HFH Off Heater Off 9
y.
ALPHA-521-0 ALPHA-521-0 Page 12 Page 12 31.3 Monitor SCs Parameters 79 [*C]
- Mean Water Ternperature Tw m n(S1) =
352 [K]
=
79 [*C]
Twf n(S2) =
352 [K]
=
- Water Level MLS1 =
3,8 [m]
MLS2 =
3,8 [m]
32 Gas Space Heating 32.0 Monitor SCs Parameters Assumphons.
-Total Pressure MP.S1 =
162 [kPa]
MP.S2 =
162[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]
=
32.1 RPV Setup for Steam injection Monitor RPV Parameters
-Total Pressure MP.RP.1 =
746 [kPa] (Psat) 168 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
441 [K]
=
- Water Level MLRP.1 =
13,5 [m]
32.2 Steam injection
- Open valve CB.S1S, CB.S2S
> AT
69[K) t.a5... ~ :. :? D.,... J T',
.n.
f
- h. '
M(SCs-struct) =
72,7 [ ton]
> AO
2,52 [GJ]
M(steam) = 1095 [kg]
> time
3148 [sec]
- Close valve CB.S1S, CB.S2S Heater Off Monitor RPV Parameters
-Total Pressure MP.RP.1 =
746 [kPa) (Psat) 168 [*C]
- Local Fluid Temperature MTF.RP.1.. 5 =
441 [K]
=
- Water Level MLRP.1 =
12,6 [m]
32.3 Monitor SCs Parameters
-Total Pressure MP.S1 =
207 [kPa]
MP.S2 =
207 [kPa) 79 [*C]
- Mean Gas Temperature Te., n(S1) =
352 [K]
=
79 [*C]
To, n(S2) =
352 [K)
=
79 [*C]
- Mean Water Temperature Tw, n(S1) =
352 [K]
=
79 [*C]
Tw3 n(S2) =
352 [K]
=
- Water Level MLS1 =
3,8 [m]
f MLS2 =
3,8 [m]
~
ALPHA-521-0 ALPHA-521-0 j,
Page 13 Page 13 33 Pressurization 33.0 Monitor SCs Paramelers Assumptions:
-TotalPressure MP.S1 =
207 [kPa) l MP.S2 =
207 [kPa) 33.1 Vent untilpressure reachs 131 Set up control valve CC.S1V i
- Close valve CC.S1V i
1 33.2 Monitor SCs Parameters j
-Total Pressure MP.S1 =
131 [kPa]
MP.S2 =
131 [kPa]
l 79 [*C]
l
- Mean Gas Te nperature Tc,,,,,,(S1) =
352 [K)
=
Tq,,,,,,(S2) =
352 [K]
- 79 [*C]
i
=
4
-Mean Water Ternperature Tw.,,,,,,(SI) =
352 [K) 79 [*CJ
=
Tw.,,,,,,(S2) =
352 [K) 79 [*C]
=
- Water Level ML.S1 =
3,8 [m]
i ML.S2 =
3,8 [m]
l 40 GDCS Heating The Test initial Condibons require a 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 2
account a full GDCS Retum Line. The required temperature is a homogeneous temperature l
of 333K for the whole tank, which is achieved by filling with water up to approximately Sm at the required temperature and then draining the tank. The total pressure in saturated conditions and in equilibrium with the Drywell pressure is at 131kPa, which includes an air partial j
pressure of 101kPa. The pressurization process is performed after to GDCS has been drained, because water filling and water draining are performed by keeping the GDCS vent valve open.
i The GDCS Setup starts with structure heating by steam injechon (phase n' 41), continues with water filling and pool conditioning, while keeping the vent valve open, the air is vented to the i
4 atmosphere (phase n' 42). A pressure corresponding to the atmosphenc pressure is i
automatically set up during water is drained to the PCC3 Pool (phase n' 43) and air is injected in order to establish the required test initial conditon. These processes &=.i,0ied to phases i
n' 71 and 72.
l
)
41 Gas Space Heating 4
41.0 Monitor GDCS Parameters Assurnptions:
Total Pressure MP.GD =
101 [kPa]
i
- Local Fluid Temperature MTF.GD.1.. 7 =
283 [K]
10 [*C]
=
-Structure temperature MTI.GD.1.. 6 =
283 [K) 10 [*C]
=
- Water Level ML.GD =
0 [m]
}
l 41.1 RPV Setup for Steam injechon Monitor RPV Parameters
-Total Pressure MP.RP.1 =
746 [kPa) (Psat) 1
- Local Fluid Temperature MTF.RP.1.. 5 =
441 [K]
168 [*C]
=
12,6 [m]
800 [kW) i Nela; The RPV ternperature must be reduced to 436K for the GDCS water filling operation (see 41.2 & 42.1) f 1
i
.v.~,
,y e.
ALPHA-5214 ALPH.45210 Page 14 Page 14 6
41.2 Steam injechon e. n valve CB. GDS
=> AT = ~
50 [K]
- 4. ;d.
)?. 9; b. d M. $
- y-M(GD-struct) =
5,00 [ ton)
> AO
0,13 [GJ)
M(steam) =
54,6 [kg]
> time
157 [sec)
-Close valve CB. GDS Heater Off Monitor RPV Parameters l
Total Pressure MP.RP.1 =
669 [kPa] (Psat) 163 [*C]
l
-Local Fluid Temperature MTF.RP.1.. 5 =
436 [K)
=
-Water Level MLRP.1 =
12,4 [m]
41.3 Monitor GCCS Parameters Total Prescure 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]
No.it; in order to get homogeneous temperature in GDCS, it is heated with water.
42 Water Filling 42.0 Monitor 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]
42.1 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters l
-Total Pressure MP.RP.1 =
669 [kPa) (Psat) 163 [*C)
-Local Fluid Temperature MTF.RP.1.. 5 =
436 [K)
=
- Water Level MLRP.1=
12,4 [m]
Heaters On MW.RP.7 = 800 [kW) 42.2 Supply water until water reaches level equal to 5,5
[m]
Vent Gas to the Atmosphere Open valve CC.BUV, CB.GDV Auxiliary water system operation Pump PC.HFH On 60 [*C]
Set up controlvalve CC. BHA MTL. BHA =
333 [K]
=
CC.BCA MTL.BCA =
max [K)
2,9 [l/s]
- Open valve CB.GDL N=6 M(GD-water) =
16,2 [ ton]
> time
5595 [sec]
- Close valve CB.GDL Pump PC. BOD Off Pump PC.HFH Off Heater Off
- Close valve CC.BUV, CB.GDV
i ALPHA-521-0 ALPHA-521-0 Page 15 Page 15 42.3 Monitor GDCS Parameters
-Tota! Pressure MP.GD =
1232 [kPa) 60 ['C]
- Mean Fluid Temperature T,_,n n(GD) =
333 [K]
=
-Structure temperature MTI.GD.1.. 6 =
333 [K]
60 [*C]
=
- Water Level MLGD=
5,50 [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 Test initial Conditions for all PCC Pools are the same; water level from the top of the i
PANDA heater bundle is defined at the highest 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 atmospheric pressure.
The Pools Setup is performed as follows: water is filled at the highest possible ta Tiperature (phase n' 51, 61 & 71) and the temperature conditions are adjusted then by circulation through the auxiliary heat exchanger (phase n* 101,102 & 103).
j H21E Similar phases can be performed simultaneously; pools can be connected and filled at the same time and water circulation can be also performed with connected pools.
51 Water Filling
)
51'.0 Monitor PCC1 Pool Parameters 10 ['C]
- Local Water Temperature MTL.U1.1.. 7 =
283 [K]
=
- Water Level MLU1=
0 [m]
51.1 RPV Setup for Heat Exchanger Operation Monitor RPV Parameters Total Pressure MP.RP.1 =
669 [kPa] (Psat) 163 [*C]
-Local Fluid Temperature MTF.RP.1.. 5 =
436 [K]
=
12,4 [m]
800 [kW)
- ygg r 4ppy y p
> AT
0 [K]
"L ::.m...
=A_,;,
U21g
- Temperature corresponding to the heat exchanger operation.
PCC1 Poolwater filling 51.2 Supply water until water reacnes level equal to 4,8
[m]
Auxiliary water system operation Pump PC.HFH On Set up controlvalve CC. BHA MTLBHA =
375,3 [K]
102
[*C]
=
CC.BCA MTLBCA =
' min [K]
2,0 [l/s]
Open valve CB.U1L MM M(U1-water) =
13,93 [ ton]
> time
6966 [sec)
]
ALPHA-521-0 ALPHA-521-0 Page 16 Page 16 i
- Close valve CB.U1L Pump PC. BOD Off Pump PC.HFH Off Heater Off M
- The temperature on the RPV side might be too high; a low flow in that side should help to reduce the temperature in the heatexchanger. If that flow reduchon is not enough, the temperature in RPV must be reduced.
51.3 Monitor PCC1 Pool Parameters 99 ['C]
- Mean Water Temperature Tw_,n n(U1) =
372 [K)
=-
- Water Level ML.U1 =
4,80 [m]
60 PCC2 Pool Setup For PCC2 Pool Setup refer to description of pools conditioning in phase n'50.
61 Water Filling 61.0 Monitor PCC2 Pool Parameters 10 ['C]
- Local Water Temperature MR..U2.1.. 7 =
283 [K)
=
- Water Level MLU2 =
0 [m]
61.1 RPV Setup for Heat Exchanger Operation Monitor 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 [m]
Heaters On MW.RP.7 = 800 [kW) 61.2 Supply water until water reaches level equal to 4,8
[m]
Auxiliary water system operation Pump PC.HFH On Set up control valve CC. BHA MTL. BHA = 375,3 [K) 102 [*C)
=
CC.BCA MTL.BCA =
- min (K)
2,0 [l/s)
- Open valve CB.U2L ET"liilECf2W4)~d$
M(U2-water) =
13,93 [ ton]
> time
6966 [sec)
Note:
- The temperature on the RPV side might be too high; a low flow in that side should help to reduce the ternperature in the heatexchanger. If that flow reduction is not enough, the temperature in RPV must be reduced and water recirculated through the heatexchanger.
- Close valve CB.U2L Pump PC. BOD Off Pump PC.HFH Off Heater Off 61.3 Monitor PCC2 Pool Parameters
- Mean Water Temperature Tw_,n..n(U2) =
372 [K) 99 [*C]
=
- Water Level MLU2 =
4,8 [m]
ALPHA-521-0 ALPHA-521-0 Page 17 Page 17 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 water transfer from GDCS to PCC3 pool.
The water is heated by passing through the auxiliary heatexchanger, which process helps to cool down the RPV in order to appraoch the required test initial conditions for the RPV.
Since the required total pressure in GDCS higher than the atmospheric pressure, the GDCS vent valve is kept open during water is drained; the total pressure in the GDCS tank will be adjusted by air injection in phase n*72 (phase n' 71 & n' 72).
P 71 Water Transfer from GDCS Tank 71.0 Monitor PCC3 Pool Parameters 10 [*C]
-Local Water Temperature MTLU3.1.19 =
283 [K]
=
- Water Level MLU3 =
0 [m]
Monitor GDCS Parameters
-Total Pressure MP.GD =
101 [kPa]
60 [*C]
- Mean Fluid Temperature Tr_m n(GD) =
333 [K)
=
2 60 [*C]
- Structure temperature MTI.GD.1.. 6 =
333 [K]
=
- Water Level ML.GD =
5,50 [m]
Monitor 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 s.
12,4 [m]
712 Supply water until water reaches level equal to 4,8 [m]
GDCS Pressurization
- Open valve CC.BUV, CB.GDV S W Z 3 M '4 D M Ef1 Auxiliary water system operation
0
[kW)
Pump PC.HFH On 102 [*C]
Set up controlvalve MTL. BHA =
375 [K)
=
MTL.BCA =
max [K)
Pump PC. BOA On MV. BOA =
2,0 [l/s]
- Open valve CB.U3U, CB.GDL ben MC.U3 = Ei4,80 Hm]sg M(U3-water) =
13,93 [ ton]
> time
6966 (sec)
- Close valve CB.U3U, CB.GDL Pump PC. BOD Off Pump PC.HFH Off Heater Off
- Close valve CC.BUV, CB.GDV NQ1E
- During that phase, the RPV, used as heat source for auxiliary water heatexchanger, is cooled down in order to appraoch the required test initial conditions - heater power is controlled (even not used) in order to decrease the RPV temperature.
71.3 Monitor PCC3 Pool Parameters
- Mean Water Temperature Tw_m n(U3) =
372 [K]
99 [*C]
=
- Water Level ML.U3 =
4,80 [m]
ALPHA-521-0 ALPHA-521-0 Page 18 Page 18 s
Monitor GDCS Parameters
-Total Pressure MP.GD =
101 [kPa]
60 [*C]
-Mean Fluid Temperature Tp_
,(GD) =
333 [K]
=
60 ['C]
- Structure temperature MTI.GD.1.. 6 =
333 [K]
=
- Water Level MLGD=
0,10 [m]
Monitor RPV Parameters
-Total Pressure MP.RP.1 =
262 [kPa] '
126 [*C]
Local Fluid Temperature MTF.RP 1.. 5 =
399 [K]
=
Water Level MLRP.1=
12,3 [m]
72 GDCS Pressurization 72.0 Monitor GDCS Parameters
-Total Pressure MP.GD =
101 [kPa]
- Mean Fluid Temperature
- Tr_,
n(GD) =
333[K]
- Water Level MLGD=
0,1 [m]
72.1 Air injection until total pressure reachs 131 [kPa]
Auxiliary air supply system operation Set up controlvalve CC.B0G.2 MM. BOG = max Pump PC.HFH CB.S1G, CB.S2G, CB. BOG
. ? y ',
-.c T:o
- Close valve CB.S1G, CB.S2G, CB. BOG 80 DryWells Setup The nominal Drywell condition is no water and a dry atmosphere at room temperature.
Tliat means that Drywells do not need specific action to reach the required state; it is only needed to make sure that both vessels are dry (without any residual pool water) and at atmosphenc temperature.
j in dry conditions, the air partial pressure is defined equals at about 131kPa. The desired temperature has been defined at 300K, but it might be different if the room temperature is different.
The Drywells Setup consists actually of making sure that both Drywells are completely dry (phase n' 81) and of pressurizing the vessels up to 131kPa.
81 Drying Vessels 81.0 Monitor Drywell Parameters Assunptions:
-Total Pressure MP.D1 =
101 [kPa]
MP.D2 =
101 [kPa]
27 ['C]
- LocalGas Temperature MTG.D1.1.. 6 =
300 [K]
=
MTG.D2.1 6 =
300 [K) 27 ['C]
=
- Structure temperature MTI.D1.1 9 =
300 [K]
27 ['C]
=
MTI.D2.1 9 =
300 [K]
27 [*C]
=
- Water Level ML.D1 =
0,0 [m]
ML.D2 =
0,0 [m]
81.1 Make sure both Drywells are completely dry - No pool of water !
- Open both vessels
- Dry recidual water pool!
- Close both vessels
r ALPHA-5210 ALPHA-521-0 m.
Pa9e 19 Page 19 81.2 Connect Drywells to all PCC Condensers
- Open valve CB.P1 F, CB.P2F, CB.P3F 81.3 Monitor Drywell Parameters
-Total Pressure MP.D1=
101 [kPa)
MP.D2 =
101 [kPa)
- LocalGas Temperature MTG.D1.1.. 6 =
300 [K) 27 [*C]
=
27 [*C]
MTG.D2.1.. 6 =
300 [K)
=
- Structure temperature MTI.D1.1.. 9 =
300 [K) 27 [*C]
=
MTI.D2.1.. 9 =
300 [K]
27 [*C]
=
Note: Temperatures in Drywells correspond to room temperature, might be different than indicated !
Check PCCs Parameters Total Pressure MP.P1F =
101 [kPa)
MP.P2P =
101 [kPa)
MP.P3F =
101 [kPa)
- LocalGas Ternperature MTG.P1.1.. 9 =
372 [K) 99 [*C)
=
MTG.P2.1.. 9 =
372 [K) 99[*C]
=
MTG.P3.1.. 9 =
372 [K) 99 [*C]
=
82 Pressurization Both Drywells are now dry and at room ternperature; the air partial pressure is equals to the atmospheric pressure. The vessels must be pressurized up to the required pressure (131kPa).
Just before the pressurization process by air injection (phase n*82), Drywells are isolated from the PCCs in order to let stabilize the pressure.
92.0 Isolate Drywells from PCCs
- Close valve CB.P1F, CB.P2F, CB.P3F 92.1 Monitor Drywell Parameters
-Total Pressure MP.D1 =
101 [kPa)
MP.D2 =
101 [kPa}
)
- Local Gas Temperature MTG.D1.1.. 6 =
300 [K) 27 ['C]
=
MTG.D2.1.. 6 =
300 [K) 27 ['C]
=
27 [*C]
- Structure temperature MTI.D1.1.. 9 =
300 [K)
=
MTI.D2.1.. 9 =
300[K) 27 [*C]
=
92.3 Air injection until Drywell total pressure reaches 131 [kPa]
8 [kPa)
Auxiliary air supply system operation Set up control valve CC. BOG 2 MM. BOG = max
- Open valve C,B D_1G, CB.D2G, CB.B0G y
g> y.: x n w m *^. v ; '.~
f
..____;u
.,s M(air) =
30 [kg)
> time
1071 [sec)
- Close valve CB.D1G, CB.D2G, CB. BOG 92.4 Monitor Drywell Parameters
- Air Partial Pressure MPG.D1.1 =
131 [kPa) 8 [kPa)
- Local Gas Temperature MTG.D1.1.. 6 =
300 [K) 27 [*C]
=
MTG.D2.1.. 6 =
300 [K) 27 [*C]
=
- Structure temperature MTI.D1.1.. 9 =
300[K) 27 [*C]
=
MTI.D2.1.. 9 =
300 [K) 27 ['C)
=
Note: Temperature,s in Drywells correspond to room temperature, might be different than indicated !
1 I
ALPHA-521-0 ALPHA-521-0 Pa0s 20 -
Page 20 i
90 RPV Initial Conditions Setup for Test After having used the RPV as heat source for vessel precondsboning, it might be at condibons
)
different from these requaed 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 precond 00ning close to the required test initial conditions for the RPV.
Phase n' 91 is a parameter check, which wil give the basis for adjusting of RPV condibons.
91 RPV Conditions Adjusting 91.0 Monitor RPV Parameters Assumbons:
-Total Pressure MP.RP.1 =
262 [kPa) 126 [*C]
-Local Fluid Temperature MTF.RP.1.. 5 =
399 [K]
=
- Water Level MLRP.1 =
12,3 [m]
91.1 AdjustTestinitialConditionsin RPV Assuming saturated conditiens and a negligible air partial pressure, the pressure is set by adjusting the temperature. Cooling is achieved by supplying cold water arxFor 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 to match the required tolerances (ref. GE document " Test Plan Specircahon").
91.2 Vent Gas to the Atmosphere Open valve CC.RPV
- '. +
91.3 Supply water unbl water reaches level equal to 12,7 [m]
Auxiliary water system operation MV. BOD =
2,0 [l/s]
Pump MP. BOD Off 91.4 Set RPV Parameters i
-Total Pressure MP.RP.1 =
131 [kPa]
l
- Mean Fluid Temperature MTF RP.1.. 5 =
380 [K) 107 [*C]
=
- Water Level MLRP.1 =
12,7 [m]
100 Test Conditions Setup PANDA preconditioning has been now 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, l
j The test condition 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 l
- 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 then with the PCC Pools condition adjustment (phase n* 105,106 & 107), which can be performed simultaneously. All i
these phases are not defined in detail, allowing any required action to get the test initial l
conditions estabbshed.
l.
ALPHA-521-0 ALPHA-521-0 Page 21 Page 21 4
101 Adjusting SC Pools Conditions 101.0 AdjustTestinitialConditionsin SuppressionChamber Pools After the check of the water temperature and water level, actions to adjust the corresponding parameters are supplying or draining water in order to satisfy the defined water level, and water circulation through one or the other of the two auxiliary heat exchangers as required to establish 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 SpNification").
101.1 Monitor SCs Parameters
- Mean Water Temperature gp M Tw M 1) g seauijpgmg'g:
j
$1?QQQ%lh '
hi% l 4 ny 9
y h TOmmISE U l I
MW[nM fM N $ $4 9l" l
I
- LocalWater Temperature
l
$psk_ _
, at I
g, o
g h
~gd sto 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 action is allowed to setup the SCs gas space test initial conditions according to the defined tolerances (ref. GE document " Test Plan Specification').
102.1 Monitor SCs Parameters N MTMP3GM',
~
"f
-Total Pressure Ree B i s $m % AMP.S2W 2 il c-t y
W:n@ nil.qw(>SJ)
Wy w
wu a. g jdg Qe f,,
ig 1.
,8
~-
- n. MTd, $. 2.((0W,p;f fjai2M, h. w
- v.,y,
- h. v, b.
- Mean Gas Temperature
- g.. n.
a
-,W sWB9 f.*Qk 8_6.N -.
,4 ae S2,)'=n m]K~}W,?a $.
.. ?
m i gm - yp &w,pq ms pq. p1K]P.rm:a?d ssi3S2.:,+pw m#
p yn
, Nf a
- 7; pg y
2 4 m n,.. L yg &gg g M LMTGSi r sE W ~ m_m agay+g g p,,y
~p
..m :, w
.:4t, w
- LocalGas Temperature iMag b
MNkkN ENhb i_M Record on attached checklist 103 Adjusting GDCS Conditions 103.0 AdjustTestInitialConditionsin GDCS Assuming saturated steam / air mixture, the temperature and the pressure are separately adjusted by steam and air injection. Any required action is allowed to setup the GDCS test
!nitial conditions according to the defined tolerances (ref. GE document " Test Plan Specification").
}
ALPHA-6210
' ALPHA-5210 Page 22 Page 22 6
103.1 Set GDCS Parameters
- -Total Pressure 1.. ;
. Z..
Mean Fluid Temperature.
l- {,
- 7. C..
. Water Level 4-
~ ~
.~
Record on attached chocidist 104 Adjusting DW Conditions
= 104.0 Adjust Test Initial Conditons in Drywells Considering pure air conditen at atmosphic pressure and at room temperature, the Drywell do not need any temperature adjustment, in order to establish the required air partial pressure, it might be needed to adpust the pressure by injecting air to the Drywells. Test initial conditions and corresponding tolerances are defined in the GE document " Test Plan Speedicaton'.
104.1 Set Drywells Parameters
- Air Partial Pressure
- , 3.
L.,
j, }$v '
- Mean Gas Temperature
~ T-8.
'e i
~
~
- Local Gas Temperature
- Structure temperature
,,, ;,..[ ]
. Water Level
~
f# "l:r-
.. ':.g
~ J^i.h.
. n..:
y l
Record on attached checidst l
105 Adjusting PCC1 Pool Conditions 105.0 Acqust Test initial Conditons in PCC1 Pool Assuming saturated conditions at atmospheric pressure, the water temperature might be adjusted by water circulation through auxiliary heat exchanger; due to evaporation, the water level might need adjustment by supplying water. Any 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 conditons must be adjusted; that may be perfomed simultaneously by 105.1 Set PCC1 Pool Parameters
~. " 4 W '?* % ~'if
- :< p.$ l%$$;s / (l..'.
J:.-
- Mean Water Temperature r '
3
.. :,:1.,.i : yj k%jk&;.s x -
.i
- :%i
",' p'. :s. '"l4:f 8
Local Water Temperature F,.m.,f-.+
m,
": C
.r'
~
j Z
w.c p.n &.
- Water Level
- w r-
.. :.. p 4 x..
"4?
Record on attraned checklist
ALPHA-521-0 ALPHA-521-0 Page 23 Page 23 106 Adjusting PCC2 Pool Conditions 106.0 AdjustTestInitialConditionsin PCC2 Pool For PCC2 pool conditions adjustment refer to description of pool conditions adjustmerri in phase n*101.
106.1 Set PCC2 Pool Parameters
~ ' T N IV sYiR
- Mean Water Temperature
. s. A n?H. i fffh.b. ((i. ~ M
' $Y
- LocalWater Temperature
'^j (.ggg.g'. %
- Water Level
.3 a e, _ s
. hm.. Aa Record on t.ttached checklist 107 Adjusting PCC3 Pool Conditions 107.0 Adjust Test Initial Conditiens in PCC3 Pool For PCC3 pool conditions adjustment refer to description of pool conditions adjustment iri phase n*101.
107.1 Set PCC3 Pool Parameters
-Mean Water Temperature
,)
t' M Di*
- Local Water Temperature
. A.'..
- C e "$f7MYM e.
Y I.
"N 2
- Water Level J
Record on attached checidist i
110 Test The facility satisfies now the required test initial conditions and must be configured according to the test configuration described in GE document " Test Plan Specification *.
4 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 that the facility stays inside the defined tolerances, the duration of all these phases between the test configuration setup (phase n*113.1 to n' 133.9) and 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 and 112, in order to satisfy the acceptance criteria defined in the " Test Plan Specification". 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* 122.1) and the procedure starts again with the Test Conditions Setup (phase n* 100).
Due to tha 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 configuration setup (phase n*113.7).
ALPHA-521-0 ALPHA-521-0 Page 24 Page 24 o
111 Data Recording 111.0 Start Data Recording ( Atleast 5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> after testinitiation) o.y...
5, y x
- g.,w qw.,,. g
'.f'
' I' ' ~ '
- }
'f
', #"'Q {
p{' I,]'
Record on attacned enecidist 111.1
"..~7 Record on attached checidist 112 RPV Conditions Adjusting l
112.0 AdjustTestInitialConditionsin RPV I
1 i
Assuming saturated conditions and a negligible air partial pressure, the required panssure is set i
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").
j i
112.1 Set RPV Parameters
- g,. g ?j-( y. g(
- . c.
l
-Total Pressure
.,.w.M.x. M,: f.a..
u wt
^-
N
- Mean Fluid Temperature 2
.r.
- a,
- h. 4 kg l,t i::1... ~: i 4.:. #:s....~'...: 1.: ' '
.f:
^ r
- l
- M.g it ~,, S '; 3 77
- Local Fluid Temperature x, ' c m.y.;.
.,. e v y
x
... ;I e ~.a :
~
-e
.- ' p.x
..~:
- Water Level v
Record on attached checidst l
113 Configuration Setup and Test initiation 113.0 Setup Constant Heat Power. Leave it OFF v
... ~.,.
~....e.4,;-O a.
.......t,..
4 '.
.,~.
x a
J-.
Record on attached checklist 113.1 Make sure all PCC Pool r are isolated
.e Record on attached checidist 1132 Open GDCS Pressure Equialization lines MTM6 Record on attached checklist 113.3 Open Main Vent Lines T. y ' N i-P 7Jlri:.P : M Record on attached checklist 113.4 Open GCCS Retum Line
.-Z P Wi 7 3 Record on attached checkrst 4. --- -
113.5 Open PCC Vent Lines E.'.T.L'~T i f W i O a.Z E E M IE Record on attached checklist 1
113.6 Open PCC Condensate Lines 4
Record on attached checklist 113.7 Open PCC Feed Lines TT2EC_3W i T d.ANKGii.liipiel Record on attached checkrst 113.8 Instrument / Zero Check and Pressure Difference Transmitters Piping Valve in
o.
ALPHA-521-0 ALPHA-521-0 Page 25 Page 25 N.YY
....N[m,,b ecord on attached checidist
.7"7[$
h R
?
113.9 Open Main Steam Lines Record on attached checidist 113.10 Print Valve Status Report every two hours during the Test duration
.'y {'W -.R.a%Qisiq $1%,~C':.'.~%..'u "'If[ _..: '
r Record on attached checidist 113.11 Check Oxygen for O Probes
,2
'4kI....... (..
. 41 ~,,4,. r.' ' ;.......L 1..
......a._7 d
Record on attached checkhst 113.12 Test initiation
- 7.,....,... -..
,I s
h.L..
,.b.,+
Aho,*.? j ~,.....-,..,..*
A
' h, '
v..
Record on attached checidist 113.13 Check Test initial Conditions - Acceptance Criteria M'.E E. 7 72...?f?E.~E C.?.'if9 tri Record on attached checidist 113.14 Testinterruption If the Acceptance Criteria are not satisfied go to phase n' : 122.0 & 122.1
==> phase n* 122.0
=> phase n* 122.1 l
- Restart procedure with phase n* 100 (Test Conditions Setup) l l
113.15 VB, Opening Setup i
,f~...
-- yg y
..y m...
...... w -
he*paels:=tc=M..a.,# @)]
L w.
.a,,,... _.. _... w w._. _. -
Record on attached checklist 120 End of Test At the end of 5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> data recording the test will be terrninated. Phases n* 121 and 122 describe the end of test and the facility shut down.
i i
i i
121 End of Data Recording i
121.0 Stop Data Recording (cf DAS Useri Guide)
After 5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> data recording teh test is wr.eated.
121.1.O 'M i Ai.1:.. i. '.E e 1.l> 1L* l." : Y Record on attached checklist
.n
..._.1s,,a.,,~......,._,.-..;~,.
.... b,ny,..
3 g 3.2.c. c.
.L_
..r.
_ +.
Record on attached checklist 122 Facility Silut Down 122.0 Stop RPV Heat Power Heater Off 122.1 Oxygen Probes Shut Off 4
122.2 Difference Pressure Transmitters Piping Valve Out
ALPHA-521Q ALPHA-521-0 Page 26 Page 26
+
122.3 leolating Vessels
- Close valve CB.MS1, CB.M2S CB.P1C, CB.P20, CB.P3C CB.P1V, CB.P2V, CB.P3V CB.GRT.P. CB.GRT.1 CB.MV1, CB.MV2 CB.P1F, CB.P2F, CB.P3F CB GP1, C8.GP2 122.4 Valve Alignment
- Set valve positions according to the valve STARTUP status Printout valve status report
- Compare to velve status for fac4ty shut down e
4 5
)
--- ----..---------------------------------------m
ALPHA-5210 ALPHA-521-0 Page 27 Page 27 200 Checklist Checklist Transient Test Number Completion of Procedure Date / Time Signatures Phase n' Performer / Reviewer 11 12 13 15 101 4
102 103 104 105 106 107 111.0 111.1 Building Temperature at Om:
and 22m:
112 113.0 113.1 1132 113.3 113.4 113.5 113.6 113.7 113.8 113.9 113.10 113.12 Start Time:
113.13 113.15 121.1 1212 Building Temperature at Om:
and 22m:
e