ML20108D632

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Panda Transient Tests M3A Integral Sys Test Apparent Test Results
ML20108D632
Person / Time
Site: 05200004
Issue date: 03/29/1996
From: Aubert C
PAUL SCHERRER INSTITUTE
To:
Shared Package
ML20108D621 List:
References
ALPHA-604, ALPHA-604-R, ALPHA-604-R00, NUDOCS 9605080206
Download: ML20108D632 (22)
v • d • e


Text

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PAUL SCHERRER INSTITtJT 5?M Document No.

ALPHA-604 Document Title PANDA Transient Tests M3A Integral System Test Apparent Test Results Revision Status Approval / Date Rev.

Prepared / Revised by P-PM G-PM G-SQR lssue Date Remarks 3 mat J. Torbeck G. Wingate O

C. Aubert 29 March 96 por v !s on le N-[-)h 28 March 96 28 March 96 (P.EAM 36 p.2) 9605000206 960506 PDR ADOCK 05200004 A

PDR

ALPHA-604 Seite 2

Controlled Copy (CC) Distribution List Note: Standard distribution (cf. next page) is non-controlled CC Holder CC List Entry Return / Recall No.

Name, Affiliation Date Date i

i sugistnemr,g m246-06 AZ PAUL SCHERRER INSTITUT i

ALPHA-604-0 Erse PANDA Transient Tests Titel M3A Integral System Test Apparent Test Results Erstem Autoren/

C. Aubert, J. Dreier, O. Fischer, M. Huggenberger, S.Lomperski, H.J. Strassberger Autorinnen 26.03.96 Summary:

This Apparent Test Results (ATR) report is compiled in accordance with the requirements j

specified in the Test Plan (TP) 25A5764R2 (GE document) section 10. The report covers the results for the PANDA Transient Test M3A. The ATR summarizes the apparent results and includes: test number, test objective, test date and time, data recording period, data analysis period, name of data file and ORACLE data tables, list of failed or unavailable instruments considered to be required for the test, list of required instruments with zero or reference check points not in tolerance or in over-range or under-range during test, deviations from test proce-dure and problems which occured during test. Statements are made whether or not the test objective has been reached and the data were recorded correctly. A table of actualinitial con-ditions based on average and standard deviation over one minute time periodjust before the test start for all parameters with a specified acceptance criteria in section 9.2 of TP is provided as well as time history plots over test duration for all top priority measurements.

Verteder Abt.

Ernpfinger/Empfingemnen E pt Abt.

Ernpfinger/Ertpfangennnen Egl.

Expl.

1 GE San Jose CA Bbletbek G. Yadigaroglu 42 I

O.' fube J.E. Torbeck h

6 T. Bandurski I

(for distribution at GE to Total 19 l

J. Dreier i

I O. Fischer 1

J.R. Fitch, G.A. Wingate, se m 22 1

J.Healzer 1

B.S. Shiralkar, l

M. Huggenberger 1

S. Lomperski 1

DRF No. T10-00005)

B& gen l

H.J. Strassberger 1

interrnaronse.

PANDA Documentation 2

D l1 l2 l3 l4 ls ls l9 l A Visum Abtllaborterfung-

ALPHA-604-0 4

page PANDA INTEGRAL SYSTEM TEST APPARENT TEST RESULTS TEST M3A Contents:

.Page

1. Test Objectives 5
2. Reference Documents 5
3. Test Date/ Time 5
4. Data Recording Period 5
5. File Names 5
6. ORACLE Data Tables 5
7. RPV Power Curve 6
8. Test Instrumentaion 6
9. Deviations from Test Procedure 6
10. List of Deviations from Reugested Initial Conditions 7

7

11. Test Processing
12. Water Temperature for PCC Pool Refilling 7

7

13. Regnested Initial Conditions Data Analysis Period for Initial Conditions 7

Environment Parameters 8-RPV Parameters 8

DRYWELL Parameters 8

SUPPRESSION CHAMBER Parameters 9

GDCS Parameters '

10 PCCI Pool Parameters 1I PCC2 Pool Parameters 11 PCC3 Pool Parameters 12

14. Graphs M3A Test - Vacuum Breaker Opening 13 M3 A Test - RPV, Drywell and Wetwell Pressures 14 M3A Test - Drywell and Wetwell Air Partial Pressures 15 M3A Test - RPV Heater Power 16 M3A Test - RPV and Drywell Temperatures 17 18 M3A Test - Wetwell Temperatures M3A Test - PCC Lower Drum and GDCS Return Line Water Temperatures 19 M3A Test - PCC Vent Line Gas Temperatures 20 M3A Test - PCC Main Steam Line & PCC Feed Line Flows 21 22 M3A Test - PCC Pool Refilling

l

~

ALPH A-60 *-O page 5

PANDA INTEGRAL SYSTEM TEST APPARENT TEST RESULTS TEST M3A

1. TEST OBJECTIVES:

The objectives of the PANDA integral system tests are to provide additional data to: a) confirm the capability of TRACG to predict SBWR containement system performance, including potential systems interaction effects (Integral System Tests) and b) demonstrate startup and long-term op-eration of a passive containement cooling system (Concept Demonstration).

The specific objective of test M3A which was conducted with nominal post-LOCA conditions after a Main Steam Line Break is to establish the base case and demonstrate transient system response and repeatability.

l

2. REFERENCE DOCUSENTS:

l Test Plan:

GE document 25A5764R2 l

Test Procedure:

ALPHA-520-2

3. TEST DATEfrIME:

Test Start:

25-OCT-95 / 22:46:42 Test Stop:

26-OCT-95 /18:54:57 Test Duration:

20:08:15 Test Period:

0 to 72495 sec l

4. DATA RECORDING PERIOD:

t Start:

25-OCT-95 / 22:35:50 Stop:

26-OCT-95 /18:54:57 Data Recording Period:

-652 to 72495 see 1

5. FILE NAMES:

i Raw Data:

panda _M3A.dat DAS-Configuration / Channel List:

kbt99999999,ol2 l

6. ORACLE DATA TABLES:

PANDA _M3A_MT_LINE PANDA _M3A_MT_ POOL l

PANDA _M3A_MT_REF PANDA _M3A_MT_ VESSEL PANDA _M3A_M_OTHER PANDA _M3A_M_TIhE PANDA _M3A_KBT INFO _ TESTS t

l l

~.

ALPHA-604-0 page 6

PANDA INTEGRAL SYSTEM TEST APPARENT TEST RESULTS TEST M3A

7. RPV POWER CURVE:

Power analys' period:

20 to 72495 sec Maximum negative deviation:

{

Maximum positive deviation:

j Standard deviation:

Power curve tolerancs

+25.0

[kW)

Definition of RPV oower deviation ^ Power) and standard deviationo):

1 e

APower = Power -1MW.RP.J e N' Power,,: theoretical power e

1 MW.RP./: measured power h

(PowarE MW.RP./ )

0=

  1. of measurements throughout the test l
8. TESTINSTRUMENTATION LIST OF FAILED OR UNAVAILABLE REQUIRED INSTRUMENTS:

Air partial pressure in DW1 MPG.DI.3 Back-up instrument: MPG.DI.2 l

Air partial pressure in DW2 MPG.D2.3 Back-up instrument: MPG.D2.2 LIST OF REQUIRED INSTRUMENTS WITH ZERO NOT IN TOLERANCE OR OVER RANGE OR UNDER RANGE DURING TEST:

None i

9. DEVIATIONS FROM TEST PROCEDURE:

Non I.The power curve analysis has been perfG7diBG consideRnTpower spiiss due to a::cMK between rod groups (see NCR p 013L l

~

ALPHA 60LO PANDA INTEGRAL SYSTEM TEST APPARENT TEST RESULTS TEST M3A

10. LIST OF DEVIATIONS FROM REQUESTED INITIAL CONDITIONS:
11. TEST PROCESSING PROBLEMS:

None HAS THE TEST OBJECTIVE BEEN REACHED:

Yes HAVE THE DATA BEEN CORRECTLY RECORDED:

Yes

12. WATER TEMPERATURE FOR PCC POOL REFILLING
13. REQUESTED INITIAL CONDITIONS DATA ANALYSIS PERIOD FOR INITLAL CONDITIONS:

Data analysis period:

-212 to -152 see Initial conditions are calculated over one minute just before connection of Drywells to RPV (phase n*123.9 of Test Procedure)

l l

ALPHA-604-0 page-8

(

PANDA INTEGRAL SYSTEM TEST APPARENT TEST RESULTS TEST M3A TABLE OF INITIAL CONDITIONS VARIABLE PROCESSID UNIT Average Standard Requested Tolerance Value Deviation Value 1

l l

ENVIRONNENT PARAMETERS Atmospheric pressure MP.EN bar Temperature of saturation for atmospheric pressure (Ts i_gN)

C RPV PARAMFTERS 1

Total pressure MP.RP.1 bar Fluid temperatures:

l Spatial average n_ mea (RP)

C n

l Local MTF.RP.1 C

l MTF.RP.2 C

MTF.RP.3 C

MTF.RP.4 C

MTF.RP.5 C

Water level ML.RP.1 m

DRYWELL PARAMETERS

  • Total pressure 2.94

+/- 0.19 Air partial pressure MPG.D1.1 bar MPG.DI.2 bar MPG.D2.1 bar MPG.D2.2 bar Gas temperatures:

Spatial average ro_ mea (D1)

C n

i Local MTG.Dl.1 C

MTG.DI.2 C

]

MTG.DI.3 C

MTG.DI.4 C

i MTG.DI.5 C

MTG.DI.6 C

  • The Drywell touj ressures are notinfep~endant vanablesTchev are gnen SVTemperatures andir partdf piessures The correspondmg tolerance p

is cajeuiated from temperature and gas partaal pressure tolerances

i A LPH A-60 '-0 page 9

PANDA INTEGRAL SYSTEM TEST APPARENT TEST RESULTS TEST M3A TABLE OF INITIAL CONDITIONS (Cont'd) l l

VARIABLE PROCESSID UNIT Average Standard Requested Tolerance l

Value Deviation Value DRYWELL PARAMETERS (Cont'd)

Gas temperatures:

Spatial average Tc_me.n(D2)

C Local MTG.D2.1 C

MTG.D2.2 C

MTG.D2.3 C

MTG.D2.4 C

MTG.D2.5 C

MTG.D2.6 C

Water level ML.D1 m

ML.D2 m

SUPPRESSION CHAMBER PARAMETERS Totai pressure MP.Sl bar partial pressure MPG.Sl bar MPG.S2 bar Water temperatures:

Spatial average w_ mea (SI)

C n

Local MTL.S t.1 C

MTL.S t.2 C

MR.S I.3 C

MTL.S t.4 C

l MTL.SI.5 C

MTL.SI.6 C

Spatial average w_,nea(S2)

C n

Local MTL.S2_1 C

MTL.S2.2 C

l MTL.S2.3 C

MTL.S2.4 C

TABLE OF INITIAL CONDITIONS (Cont'd)

    • The suppression Chamber air patal presswes are not indF4TniTIirabTe~sTihey are given Sy iempera:ures and total pre ing tolerance is calculated from temperature and total pressure tolerances.

b.1,PHA-604-0 page 10 PANDA INTEGRAL SYSTEM TEST APPARENT TEST RESULTS TEST M3A VARIABLE PROCESSID UNIT Average Standard Requested Tolerance l

Value Deviation Value SUPPRESSION CHAMBER PARAMETERS (Cont'd)

Water Temperatures:

MTL.S2.5 C

MTL.S2.6 C

Gas temperatures.

Spatial average ro_m (SI)

C n

Gas temperatures:

Local MTG.S I.1 C

MTG.S I.2 C

MTG.S I.3 C

j MTG.S I.4 C

l MTG.SI.5 C

MTG.SI.6 C

i Spatial a"verage To_

n(S2)

C i

Local MTG.S2.1 C

MTG.S2.2 C

l MTG.S2.3 C

j MTG.S2.4 C

MTG.S2.5 C

MTG.S2.6 C

Water level ML.Sl m

ML.S2 m

l GDCS PARAMETERS Total pressure MP.GD bar j

Fluid temperatures:

I Spatial average w_m (GD)

C n

l Local MTF.GD.1 C

MTF.GD.2 C

MTF.GD.3 C

TABLE OF INITIAL CONDITIONS (Cont'd)

AL?H A-602 0 page 11 PANDA INTEGRAL SYSTEM TEST J

APPARENT TEST RESULTS TEST M3A VARIABLE PROCESSID UNIT Average Standard Requested Tolerance Value Deviation Value 1

GDCS PARAMETERS (Cont'd)

MTF.GD.4 C

MTF.GD.5 C

MTF.GD.6 C

MTF.GD.7 C

Water level ML.GD m

PCCI PARAMETERS Water temperatures:

Spatial average tw_..n(Ul)

C Local MTL.Ul.1 C

MTL.UI.2 C

MTL.UI.3 C

MTL.UI.4 C

MTL.UI.5 C

MTL.UI.6 C

MTL.UI.7 C

Water level ML.UI m

PCC2 PARAMETERS

)

Water temperatures:

Spatial average aw_m.n(U2)

C Local MTL.U2.1 C

MTL.U2.2 C

MTL.U2.3 C

MTL.U2.4 C

MTL.U2.5 C

MTL.U2.6 C

MTL.U2.7 C

Water level ML.U2 m

~.masa

.4._:

(

l A LPH A-604-0 page 12 PANDA INTEGRAL SYSTEM TEST APPARENT TEST RESULTS 1

TEST M3A TABLE OF INITIAL CONDITIONS (Cont'd)

VARIABLE PROCESSID UNIT Average Standard Requested Tolerance Value Deviation Value PCC3 PARAMETERS Water temperatures:

j Spatial average w_mo (U3)

C n

Local MTL.U3.1 C

MTL.U3.2 C

MTL.U3.3 C

MTL.U3.4 C

i l

MTL.U3.5 C

MTL.U3.6 C

l l

MTL.U3.7 C

j MTL.U3.8 C

l MTL.U3.9 C

MTL.U3.10 C

MTL.U3.ll C

i l

MTL.U3.12 C

MTL.U3.13 C

l MTL.U3.14 C

l MTL.U3.15 C

t MTL.U3.16 C

MTL.U3.17 C

MTL.U3.18 C

MTL.U3.19 C

Water level ML.U3 m

e

l/al M3A Test -Vacuum Breaker Opening

,gg P

%d>

M o

50 -

a gk 5

am m em (A

"d F-p m

a 2

45000 50000 55000 60000 65000 Q

I TIME _SEC a

a-*mo

> f&

=

m z

m ef,$dg Ya

>m a BgN"p a~6 00097 e

r usse r

0 P

0

,0 9

l 5

lew teW dn C

a E

S_

l 0

l 0

e i0 E

9 w

3 M I

y T

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,V PR t

0 s

0

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9 T

1 A

3 M

0

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a 0

b

~

1

[

0 0

0 0

0 0

0 0

5 0

5 0

5 0

5 0

3 3

2 2

1 1

0 0

[bar]

M3A Test - Drywell and Wetwell Air Partial Pressures 4.00 3.50 -

3.00 -

2.50 -

~

h ho y%yg 2.00 -

m 1.50 -

EN 1.00 -

un Si 0.50 _.-

o 0.00 -

T

-1000 19000 39000 5>

TIME _SEC

-~

t

?h'

% 'g

[kW]

M3A Test -- RPV Heater Power 1200 2

6 E

1000 -

~

m 800 -

%m>

m O

600 -

yb

o K m m sm d1 m+

400 -

"M hK M

M a

200 -

em 0

-1000 19000 39000 59000 79000 TIME _SEC

I 1

i t

M3A Test - RPV and Drywell Temperatures

[c]

136 -

m kd 134 -

a am ag a mb 132 -

yHy6" s

d M A

130 -

m I

i i

yy 128

-2000 18000 38000 58000 78000 G

f TIME _SEC h

4 O

r t

>a E>

[c]

M3A Test - Wetwell Temperatures 80 5;

78 -

m

~

76 -

a il kh

  • ~

>aa mg 8 *-

M m

N 72 -

70 i

-1000 19000 39000 59000 7

TIME _SEC

M3A Test - PCC Lower Drum and GDCS Return Line

[c]

Water Temperatures 120 100 -

I

-o yk 80 -

a?

  1. 2 d

b N v>bd*

60 -

?

r "! y 4

s~

40 -

dg a

20

-1000 19000 39000 59000 79000 m

u% >

G TIME _SEC h

h 65

] >G l

I M3A Test - PCC Vent Line gas Temperatures

[c) 120 6

a 100 -

m

  • Cm>

80 -

a am a m5

$y 60 -

$a

~

$c6 "N

4 40 -

20 i

~2000 18000 38000 58 78000 TIME _SEC

M3A Test - Main Steam Line & Feed Line Flows 250 m

W m

200 -

150 -

B e

2 Bp w am 100 -

m

~

a m 50 -

m

.o 0 -.

-1000 19000 39000 59000 79000 m

TIME _SEC e?

s

'> ; x > g e d

Oi m>2O> gH8wM y,ga ya

>mm>b3 aFe gm d

5 d n xm>

0 0

0 97 0

l 00 e

9 v

5 e

L 4

re t

a W

l C

o E

o 0

S_

0 P

,0 E

9 C.

3 M IT C

P t

seT A

0 3

0

,0 M

9 1

00

]

0 m

1

[

0 0

0 0

0 0

0 8

6 4

2 0

s 4

4 4

4 4

_

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