Text

Non-proprietary WCAP-14056, AP600 Fhfp Integral Sys Test Specification
	ML20070P756
Person / Time
Site:	05200003
Issue date:	05/31/1994
From:	Conway L; WESTINGHOUSE ELECTRIC COMPANY, DIV OF CBS CORP.
To:	;
Shared Package
ML19304C109	List: ML20070P738; ML20070P756;
References
	WCAP-14056, NUDOCS 9405120203
	Download: ML20070P756 (51)
	v • d • e

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L WESTINGilOUSE CLASS 3 (Non-proprietary)

WCAP-14056 1

PDR

AP600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION s

4 INDEX l

Page 1.0 Introduction / Purpose l'

[

2.0 Test Objectives 2

3.0 References 3

4.0 Test Facility Requirements 5

5.0 Test Articles 9

6.0 Instrumentation and Controls Requirements 16 l

7.0 Data Acquisition System 35 8.0 Test Operation 39

]

1 9.0 Test Reports and Data Requirements 47 10.0 Quality Assurance Requirements 48 i

06341/110493 i

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AP600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION 1.0 Introduction / Purpose Westinghouse, ENEAm, ENELm, and SOPREN-Ansaldom have a cooperative agreement for SIET* to perform a set of integral systems tests to provide thermal-hydraulic data for computer code validation and to simulate the operation of the AP600 plant and passive safety systems. The SPES* facility located in Piacenza, Italy and operated by SIET is being modified to simulate the AP600 reactor vessel, reactor coolant system, and passive safety injection system.

Originally the SPES facility was commissioned by ENEA to simulate a Westinghouse 312 pressurized water reactor with Italian specific design features.

The modified SPES facility, SPES-2, will be a full height, full pressure,1/395th volume scale simulation of the AP600.

i

1) ENEA, " Ente per le Nuove Tecnologie, l'Energia e l'Ambiente,"

2) ENEL, " Ente Nazionale per l'Energia Elettrica, S.p.A."

3) SOPREN, "Societa Progettazione Reacttori Nucleari, S.p.A."

4) SIET, "Societa Informazioni Esperienze Termoidrauliche" i

o

5) SPES, "Simulazione PWR per Esperienze di Sicurezza" MNlMN 1

m

AP600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION 2.0 Test Objectives The overall objectives of the AP600, SPES-2 Integral Systems Test are:

Simulate the AP600 thermal-hydraulic phenomena and behavior of the passive e

safety systems following specified small-break loss-of-coolant-accidents (LOCA'S), steam generator tube ruptures (SGTR'S), and steam line breaks (SLB's).

Obtain detailed experimental results for verification of safety analysis computer o

codes.

fe%1'110a9) 2

AP600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION 3.0 References A)

AP600 Plant Description Document, Rev.1, December,1990 B)

AP600 Safeguard Interface Data, GWGLOO2, Rev. 0 l

C)

AP600 Reactor Coolant System (RCS) SSD RCS-M3-001, Rev. 0; NSE-92-0081 D)

AP600 Passive Core Cooling System (PXS) SSD PXS-M3-001, Rev. O, NSE-92-0034 E)

AP600 Steam Generator System (SGS) SSD SGS-M3-001, Rev. 0; NSE-92-0036 F)

AP600 Normal Residual Heat Removal System (RNS) SSD SGS-M3-001, Rev. 0; NSE-92-0031 G)

AP600 Chemical & Volume Control System (CVS) SSD CVS-M3-001, Rev. 0; NSE-92-0082 H)

Reactor Vessel and Internals Drawings:

MV01 VI 001, Rev. I o

MV01 V2 001, Rev. I ee RXS V2 001, Rev. 2 MIOl V1001, Rev. 2 I)

Steam Generator and Pressurizer Drawings:

l MB01 V2101, Rev. 3 MB01 VI 001, Rev. 2 MB01 V2 001, Rev. 2 J)

Primary Loop Layout Drawings:

PLOl V2 001, Rev. 3

)

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l 1

K)

NSSS Systems P&ID's l

RCS M6 001, Rev. 6 SGS M6 001, Rev. 4 j

PXS M6 001, Rev. 4 l

e CVS M6 001, Rev. 5 RNS M6 001, Rev. 3 L)

IMP THRIVE Data, MED-RPV-3403 M)

AP600 Design Parameter List, NSE-90-0334 N)

PRHR HX Design Document, SEE-FS(91)-0179 0)

AP600 General Arrangement Drawings e

1010 P2 001, Rev.1 e

1020 P2 001, Rev.1 1020 P2 002, Rev.1 1030 P2 001, Rev. I e

1040 P2 001, Rev.1 e

1000 P2 901, Rev.1 1000 P2 902, Rev. I e

1000 P2 907, Rev.1 P)

Revision to AP600 Safeguard Interface Data SEE-FS(92)-0254 Q)

AP600 RCS Primary Water Volume Calculation, AFD-2PST-C001,Rev.1 R)

SPES-2 " Scaling Update", SIET Document No. 00185 R192, Rev. O dated November 12, 1992 S)

SPES-2, " Instrumentation and Data Reduction Plan," SIET Document No.

00182P092, dated December 31, 1992.

T)

SPES-2, " Component and Piping Drawings," SIET Document No.-

00189DD92, dated December 31, 1992.

U)

SIET "SPES-2, Facility Description" Doc. No. 00183R192, Draft.

uunun 4

AP600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION 4.0 Test Facility Requirements A scaling, design and verification analysis is to be made to delineate the specific design features to be incorporated and modifications to be made to the SPES facility to simulate the AP600 design. The following general criteria are to be applied to the design of the SPES-2 test facility relative to the AP600 plant design:

AP600 fluid thermodynamic conditions (pressure and temperature) are to be maintained.

The AP600 power over volume ratio is to be matched in each component.

The AP600 power over mass flow rate is to be conserved.

The SPES-2 fluid transit times are to match the AP600 (this is a direct result of meeting the three criteria above).

The heat flux in heat transfer components (core and steam generator) shall match the AP600/SPES-2 power scale.

The SPES-2 main components shall match the AP600 specific and relative component elevations.

Exceptions to the above general criteria shall include:

Main Coolant Loop Piping: the Froude number shall be preserved due to its influence in the slug to stratified flow pattern transition in horizontal tubes.

Pressurizer; volume scaled with the power over volume ratio; height defined according to Wilson bubble rise model.

The existing SPES steam generators shall be utilized.

The following SPES facility features shall be retained:

The SPES power channel will remain the same although tubular pieces shall be inserted at flange eles ations to adjust the rod bundle elevations to match the AP600 fuel elevation.

Of,M111049.1 5

The existing SPES main coolant pumps shall be utilized although their position (side suction and side discharge) will be modified to eliminate any loop seal between the steam generators and the pump suction The steam generator elevation shall be retained (and thus provides the.

reference elevation for the placement of other components).

One n a coolant pump will be installed in each of the two AP600 reactor coolant system loops.

The following AP600 features are to % added to the SPES-2 facility.

Each of the two reactor coolant loops is to include one hot leg (from the -

reactor to a steam generator) and two cold legs (from a single coolant pump discharge to the reactor).

The portion of the reactor vessel above the heated portion of the rod bundle shall include an annular downcomer into which all four cold legs and the two safety injection nozzles are connected.

The following AP600 Passive Safety Injection System Components, associated piping and required valves shall be simulated.

- 2 Core Makeup Tanks (CMT's)

- 2 Nitrogen driven Accumulators

- 1 Passive Residual Heat Removal Heat Exchanger (PRHR HX)

- 1 In-containment Refueling Water Storage Tank (IRWST)

- the Automatic Depressurization System (ADS) function from the pressurizer (Stages 1, 2, & 3)

^

- 2 ADS 4th stages (one on each hot leg)

The capability of the AP600 normally available, non-passive systems (CVCS makeup and normal RHR pumps) to inject water is to be provided, and (SG startup feedwater system /SG PORV) steam generator heat removal function is to be provided, amvun 6

The test facility shall also have the following capabilities:

Provide adequate space for all test components and supporting systems such that the test can be constructed and operated with ease, efficiency and safety.

All test components shall be situated at scaled heights as determined from a scaling study based on prototypical AP600 dimensions.

Provide a controlled electrical supply system estimated to be at least[ ]M kilowatts to power the electrical heater rods in the reactor core model in order to simulate the AP600 core full power. Controls must be such that the decay heat transient can be accurately simulated.

Provide a cold water supply capable of providing uncontaminated cold water at adequate rates for system and equipment fill, CVCS and NRS makeup, and SG start-up feedwater supply. Pumped fill capability must be provided.

The facility shall be insulated to minimize heat losses from the simulated primary system and steam generators (based ogIET's experience with the original SPES facility, heat losses of[

]can be expected).

A means to provide the AP600 safety system actuations is to be provided.

Provide adequate drainage systems to remove water from the test loop as well as any spillages or overflows such that the test facility will not be adversely affected.

Provide a system to condense steam and measure the condensate or flows from the selected break locations (See Section 8.0), from the ADS Stage 1,2 and 3, from the ADS Stage 4, and from the SG PORV discharge.

Provide adequate ventilation to remove steam or water vapor discharged from the test facility.

Provide a data acquisition system (DAS) to record all instrument channels (See Section 6.0) from various sources such as thermocouples, pressure sensors, flow meters. All data shall be permanently recorded on an acceptable electronic media (such as a DEC TK-50 cartridge) for transmission to Westinghouse. (See Section 7.0)

Major operating parameters such as system pressure and temperature shall be visually displayed independent to the DAS system.

Or34dflIDa93 7

1

An instrumentation plan shall be developed and used which will permit e

accurate calculations of transient mass and energy balances for the systems.

The facility shall be capable of performing steady-state experiments as well as transient blowdown tests.

The test performer must submit all designs to Westinghouse Test Engineering for

)

review and approval prior to procurement and fabrication. In addition, the test I

performer has the responsibility of procurement and fabrication of entire test facility which includes instrumentation calibration.

1 1

l ww uw 8

AP600, SPES-2 Integral System Test Specification 5.0 Test Articles A conceptual schematic of the AP600 SPES-2 Integral System Test is shown in Fig.

5.1. The reactor vessel, reactor coolant piping, steam generators, pressurizer, ADS,.

CMT's, IRWST, accumulators, passive residual heat removal exchanger, applicable parts of NRHR, CVCS and steam generator heat removal systems, and interconnecting piping and valves needed to simulate AP600 functions; are regarded as test articles.

All tank.s, piping and valves are to be designed in accordance with applicable code requirements (e.g., applicable U.S. code requirements are ASME Div.1,Section VIII for tanks, B31.1 Power Piping Code for piping) for non-nuclear components, consistent with the below stated working pressure and temperatures, and for the repeated heatup and cooldown transients derived from the tests described in Section 8.

All test articles and interconnecting piping shall be sized and located at the proper elevations based on a scaling study using prototypical AP600 dimensions as the basis.

The test articles are to be instrumented as specified in Section 6.0. The test articles shall include provisions to simulate the breaks and break locations discussed in Section 8.

A.

Reactor Vessel The reactor vessel shall be constructed of stainless steel material and include a representation of the upper and lower reactor plenums, an annular downcomer section, the reactor core and the upper head region. It shall be designed for an opetating pressure of 17.5 MPa and 355 C. Connections for the hot and cold legs and PXS injection nozzles shall be provided in the annular downcomer.

Heat losses from the vessel shall be minimized. The reactor core shall be

. simulated using electrically heated rods; they shall have the capability to simulate with the proper scaling factor the full power and decay power of the AP600, and to account for the differences in heat losses and metal masses. The heater rods shall be instrumented to monitor the bundle temperature as thoroughly as possible and to protect the rods from over-heating. The instrumentation plan of the heater rods is described in Section 6.0.

06 % 1'86049) 9 l

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B.

Reactor Coolant Loop Piping Both the two hot and the four cold leg (of the RCS) p[ipe g.h.

4 stainless steel material and designed for a pressure of g

Heat losses from the loop piping shall be minimized. A tee, to simulate CL breaks, shall be installed on the bottom of the cold leg pipe 2/B which includes a CL to CMT balance line to the normally instrumented CMT.

C.

Steam Generators The two steam generators shall be made of stainless steel on tho.se parts wegted by primary fluid. It sha[1,be designed for a pressure of at leasth

]Itnd a temperature of[

fSince the existing SPES steam generators will be utilized, they need not be completely prototypical scale, but shall approximate the AP600 to the maximum extent possible. The SG/RCP suction piping must incorporate provisions to allow simulation of single and multiple SGTR transients from the pump suction primary side to the SG secondary side. Each SG shall have one or more power operated relief valves to simulate AP600 SG heat removal during simulated transients.

D.

Pressurizer

.t The pressurizer in the test it shall be m(de of stainless steel mat rial and designed for a pressure of[

heater (s) shall be provided to contr]oi the facility pressu Ah5 a temperature of[

In internal pressurizer fluid at prototypic pressure and temperature. The pressurizer shall have a sufficiently large steam space discharge pipe to permit simulation of the ADS, The pressurizer may have additional external heaters to obtain more prototypic heat losses and may utilize the first stage of ADS for overpressure pressure control.

E.

Automatic Depressurization System Valves and pipes shall be provided off the top of the PZR to simulate the first 1

three stage (of the AQS.S a temperature of[

All the pipes and valves shall be designed for a

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The two independent trains of 1-3 stage ADS in AP600 shall be modeled with ~

one train in the test.

An orifice in each stage in the test shall be properly sized to represent the flow area of 2 trains of each stage in AP600.

wwusm 10

The fourth stage of the ADS shall be represented by a piping connection and valve off each hot leg; an orifice shall be provided in each line and shall be sized to simulate the depressurization rate of the AP600 and to take in account the excess metal heat of the facility.

The discharge from ADS Stages 1, 2, and 3 shall be measured, condensed and then drained in a catch tank for mass flowrate measurements. Separate measurements, condenser and catch tank are to be provided foi in the common Stage 4 discharge flowpath.

Note, one of the ADS 4th stage connections shall be shared with the PRHR heat exchanger supply line from hot leg A.

F.

Core Makeup Tanks Two vessels made of stainless steel material shall be provided to gravity drain into the RV through the safety injection nozzles. The design pressure of the vessels and connecting piping shall be consistent with the primary system operating conditions. The CMT's shall be designed such that they contain the proper scaled metal mass and inlet pipe diameter. The CMTs connection lines shall meet the following requirements:

CL to CMT Balance Lines The layout shall closely model the AP600 layout lines slopes.

The lines shall be insulated and heat traced.

The connection to the CL will be located just upstream of the RCS CL bend.

The lines size shall be selected to match the AP600 delta-P at the scaled flow rate.

The lines shall be provided with a drain on the CMT side of the isolation valve to avoid the presence of water before starting the transient.

The isolation valve shall have capability to be opened slowly (

]c, b PRZ to CMT Balance Lines cv The lines can duplicate part of the length of the[

) piping (at the e

same elevation) under the operating deck.

The elevations at which the two lines are connected to the pressurizer Safety -

Valve / ADS piping shall match the AP600.

4 osuniom 11

The connection to the CL balance line must be as close as possible to the 90* elbow above the CMT (and at high point).

The lines shall be insulated and heat traced.

The lines size will be selected to match the AP600 delta-P.

CMT Discharge Lines The end point elevations shall be maintained, and the piping will include a low point where the valves and flow orifice are located.

The lines size will be selected to match the AP600 piping delta-P and therefore should include an orifice that has a delta-P similar to the AP600 CMT discharge line orifice.

The isolation valve shall have the capability to be opened slowly (

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G.

In-containment Refueling Water Storage Tank A stainless steel vessel shall be provided to simulate the IRWST. This vessel b shall be designed for the static head of water and a temperature of

,]%

t Two discharge lines (one to each DVI) will be simulated. The discharge line shall maintain only the end point elevations and delta-P, it will not necessarily duplicate the AP600 layout.

H.

Accumulators Two tanks representing the accumulators shall be designed and made of stainless g

steel material. They shall be designed for at least

)Ndd'will be pressurized with nitrogen or air. The Accumulators discharge lines shall duplicate only the delta-P and end point elevations, not necessarily duplicate the AP600 layout.

I.

Passive Residual Heat Removal Exchanger One 100% capacity of AP600 PRHR HX shall be modeled in the test. The PR.HR HX and connected piping shall be made of stainless steel material and designed to a pressure consistent with the primary system operating conditions.

The exchanger shall be constructed of material similar to AP600, and sized to properly model the heat transfer.

The inlet line layout shall duplicate the AP600 until the ADS tee maintaining the elevations; after this point the piping high point above the IRWST and the ocuenom 12

PRHR HX connection elevation will be maintained. It is not necessary to duplicate all AP600 layout routing. The elevation of the SG channel head connection shall also be maintained. Both the inlet and discharge piping sizes will be selected to match the AP600 delta-P.

J.

Normal Residual Heat Removal System A pumped water source (s) shall be provided to simulate the normal.RHR System. The normal RHR exchangers will not be simulated. Two delivery lines shall be simulated, one to each CMT discharge line. The pump suction maybe from a generic water source or from the IRWST. The Normal Residual Heat Removal system connection with the DVI must be upstream of the CMT flow orifice in order to create backpressure on the CMT discharge that will prevent the CMT from draining below[

]b K.

Chemical and Volume Control System A pumped water source shall be provided to simulate the Chemical and Control Volume System. One delivery line shall be connected to the A loop RCP suction.

The CVCS pump suction fluid may be from a generic water source or the IRWST.

L.

Startup Feedwater System The SG feedwater system shall be capable of providing scaled flow rates similar to the AP600 startu2 $edwater pump. The system g' rovisions f

all be designed to a

[and a temperature of[

]P pressureof[

to assure the proper control of the SG level and the adequate scaled flowrate in all the SG functional conditions expected during transient simulations.

M.

Break System The break system shall simulate the break opening in the location stated in Section 8.0. It shall include a break unit, the blowdown piping condenser and a break flow storage tank (catch tank) for fluid mass measurement. The break unit including the break isolation valve shall be designed for a pressure consistent with the primary system.

1 1

The break unit shall include a break area simulation orifice, a break initiation valve and a gamma-densitometer, turbine flowmeter for two phase flowrate measurements.

3 ocw m m 13

l The catch tank device shall include a steam condenser and a tank to collect the outlet fluid.

]

For tests which are to be double ended guillotine (DEG) breaks, the break device shall consist of two break lines separated by a normally open valve in the process line. Each break line shall contain a normally closed break valve, followed by a gamma-densitometer, turbine meter, condenser, and catch tank.

Note that for the DEG breaks, one set of blowdown piping instrumentation from the ADS can be utilized.

As stated above, similar instrumentation shall be provided for measuring and.

collecting the ADS Stage 1,.2,3: the ADS Stage 4, and for the SG PORV discharge lines, n

N.

Interconnecting Piping All interconnecting piping shall be designed to be of proper size based on the scaling analysis. Adequate pipe strength, support and flexibility shall be provided to insure the integrity of the system. Lines shall be designed and routed to simulate the AP600 routings where specified. Appropriate vents and drains shall be provided to allow proper filling and draining. Important piping runs and ADS lines shall contain replaceable orifices for adjusting the effective pipe delta-P's based on pre-operational testing.

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4 R' Fig. 5 ! - Conceptual Schematic of SPES-2. Facility s

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AP600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION 6.0 Instrumentation and Controls Requirements The following types of instrumentation are to be provided for the AP600 SPES-2 integral system test:

Thermocouples (T/C's) shall be used to measure the temperature of the coolant in the primary and secondary systems as well as any supply or component cooling water. They also measure selected component wall temperatures in order to complete mass / energy balance on the components.

T/C's shall also be used to measure the temperature in selected heater rods simulating the core. Locations shall be chosen within selected heater rods to obtain both the axial and radial temperature distribution within the heater core.

Premium grade thermocuples shall be used and connected through controlled purity extension wire to a low level volt meter and analog to digital conversion circuit in the data acquisition system (DAS),

The response time of the thermcouples shall be consistent with the data acquisition system sampling rate specified in Section 7.0, to assure accurate measurement.

Flowmeters shall be used to provide a measurement on all single phase water mass now rates. The range of these meters must be carefully selected to minimize errors.

Pressure transducers shall record the absolute pressures within various tanks and at selected location in the test loops.

Differential pressure transducers shall be used to record pressure drops and liquid levels in the various tanks and vessels in the test loop.

Two phase flows from the break, ADS, and SG PORV discharge lines shall be routed to condensers for measurement.

These discharge paths shall include volumetric Dow measurement as well as pressure and temperature. Gamma densitometers shall be provided for the break and ADS discharge lines.

The type of flow meters to be used shall be consistent with the expected steam or water flow rates and thermal hydraulic conditions.

16

The individual instrumentation channels to be provided in the SPES-2 facility have been developed with SIET, ENEA, ANSALDO, and Westinghouse input and are specified in i

.Ref. S. A listing of the instruments and their locations are provided in Table 6.1.

Type of Controls The test shall model the AP600 process control where necessary. Controls shall be utilized in the test facility to aid the smooth operation of test runs. Following is a list of process controls to be used in the test. Additional controls may be added as necessary to improve operability of the test facility.

Steam Generator Level Control Water level in the steam generator shall be controlled. This is performed by monitoring the steam generator level which is interlocking with the feed water control valve for both the main feedwater (full power operation) and the simulation of the startup feedwater.

Steam Generator Steam Control l

Main steam pressure is to be controlled with a throttle valve or pressure control valve during full pressure operation. A separate pressure control valve is to be provided to simulate the PORV function.

ADS Actuation The ADS valves are interlocked to open at selected CMT water levels. Valves included in this operation are 1-3 stage ADS valves and 2 fourth stage ADS valves.

CMT Actuation The CMT injection line isolation valves and the cold leg to CMT balance line isolation valves are normally closed and are interlocked to open following a simulated "S" signal or low pressurizer water level. The isolation valves in the pressurizer to CMT balance lines are normally opened and no control is required.

Steam Generator Isolation Valves Controls Each steam generator main steam line and main feedwater line shall contain a l

normally open valve which is interlocked to close on an "S" signal. A startup feedwater isolation valve is to be provided on each steam generator which closes on high level.

wwnun 17

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-i-Reactor Vessel Heater Rod Control Power to heater rods is interlocked to shut off at high heater rod temperature.

The heater rod power level vs. time to simulate the transition from full power to decay heat power shall have the capability to be automatically and continuously controlled to a predetermined power vs. time, and is actuated when the reactor pressure reaches a low pressure setpoint. NOTE: Heater rod power will be used to compensate for facility heat losses following initiation of the transients to be simulated.

The SPES-2 decay heat vs. time curve will be determined based on evaluation of AP600 analyses and other factors including:

- the ANS 1979 decay heat curve with no consideration of uncertainties

- compensation for the metal heat stored in the AP600 core

- delayed fissions

- AP600 reactor trip actuation and rod drop time

- SIET's power supply control capabilities

- compensation for facility heat losses. NOTE: < heat loss compensation is to be terminated when the reactor system depressurization rate (and temperature decrease) results in excess metal heat release; e.g. compensation is terminated when ADS Stage 1 is actuated during simulated 2-in. break test.

Safety Injection Signal Actuation The safety injection signal ("S" signal) referred to in the above control descriptions is actuated when the reactor pressure reaches a low pressure setpoint.

PRHR Discharge Line On/Off Control PRHR discharge line isolation valve is interlocked to open on several Protection System signals when heat removal from the SG's is not available, at the actuation of the first stage ADS valve, or when the pressurizer water level is high following a CMT actuation.

Other on/off valves are CVS and RHR pump discharge isolation valves.

i i

NOTE: The actual setpoints for various parameters discussed above will be provided by separate documentation. These setpoints will be based on the actual AP600 setpoints and/or pre-test analysis results.

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l TABLE 6.1 SPES-2 INSTRUMENTATION LIST- _ -

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3 Locaton lype log Rongo Measurd Hydrouhc Potomeles Potometer DP DP unft head M

Q Maurnian Vokie Monunurn voh n t CL A1 DP - Transmeet DP A0t1P

-25 25 kPa CL A2 DP - Transmeet DP-A012P

-25.25 kPa SG A nser DP - Transmeer DP-A01S 0.50 kPa DC annular - CL A1 DP - Teansmeer DP-A021P O:50 kPa DC annular - CL A2 DP - Transmeer DP-A022P O : 50 kPa SG A riser DP - Transmeer DP-A02S 0:70 kPa l

SG Airvout DP Transmear DP-A03P

-100 :400 kPa SG Aseparator DP - Transmeer DP-A03S

-50 : 50 kPa HL A DP - Transnutter DP-A04P 40 : 60 kPa l

SG A separator DP - Transmeer DP-A04S

-10 '10 kPa SG A U-tube hat sde DP - Transmeet DP A05P

-60: 120 kPa SG A dryers DP - Transatter DP-A05S 0 10 kPa l

g SG A U tube has sde DP - Transtmeer DP-A06P 40 : 60 kPa l

SG A user DP - Transnutter DP A06S 0.30 kPa SG A U tube cold sde DP - Transmuer DP A07P

-30.70 kPa SG A U tube cold sde DP - Transmuer DP-A08P

-60 :100 kPa Pumpsuction A DP - Transmeer DP A09P O: 100 kPa PC Upper pienurn - HL A DP - Transmeer DP-A1SP

-15 : 15 kPa HL A - Uppet plenurn DP - Teanstmeer DP-At 6P O. 20 kPa Ace A insecten hne -

DP - Transmaer DP-A20E 50 50 kPa PRZ CMT A balance bne DP - Transmiter DP A28P O.t00 kPa CMT A dscharge hne DP - Transmiter DP-A40E O:100 kPa CMTA DP - Transatser DP-A4 t E O 18 kPa CMTA DP - Transmiter DP-A42E O. I8 kPa CMTA DP - Transm ;er DP-A43E O:18 kPa CMT A DP - Transoner DP A44E O.18 kPa CMT A CL balance kne DP - Transatter DP A45E

-50 : 50 kPa IRWST dscharge kne A DP - Transatter DP A61E o-100 kPa PRHR supply hne DP - Transetter DP A8IE 50 50 kPa PRHR supply - return DP - Transratter DP A82E 50. 50 kPa PRHR returnime DP - Transtatter DP A83E O 50 kPa Cold kg t/B DP 1:ansintter DP B00tP 0 50 kPa

_ _ _ _ _ _ _ _ <j

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TABLE 6.1 SPES-2 INSTRUMEN_TATIOfL LIST _

_ a r a or is

,J tocolson lype log Range Moosure Hydroutc Potometer Posomelet DP DP unit head M

O Maunnem Volue Mammum Voh m Cold leg 2,B DP - Transmeter DP B002P O 50 kPa RPB DP - Transmeer DP BOOP O - 700 kPa SG B battle DP - Transmeer DP B00S

-25.25 kPa CL Bt DP - Transmeer DP-90t tP 25 25 kPa CL B2 DP - Transmeer DP-8012P 25: 25 kPa SG B nser DP - Transmeer DP-BOIS 0 : 50 kPa DC annular - CL Bl DP - Transmeer DP-8021P 0. 50 kPa DC annutar - CL B2 DP - Transmeer DP 8022P O : 50 kPa SG B nser DP - Transmeer DP-802S 0:70 kPa l

SG B erVout DP - Transmeer DP-803P

-100.400 kPa SG B separator DP - Transmeer DP-803S

-50 : 50 kPa C

Hot Leg B DP - Transmeer DP B04P

-40 :60 kPa SG B separator DP - Transmeer DP-804S

-10:10 kPa SG B U-hbe hot sade DP - Transmeer DP-805P

-60 :120 kPa SG B dryers DP - Transmeer DP-BOSS 0: 10 kPa SG B U tube hot sede DP - Tsansmeer DP 806P

-40 :60 kPa SG B riser DP - Transmeer DP 806S 0:30 kPa SG B U-tube cold sado DP - Transmeer DP 807P

-30 :70 kPa SG B U hee cold sade DP - Transmeer DPB0SP

-60 :100 kPa Pump =w*an B DP - Transmeer DP-809P 0:100 kPa PC Upper pienurn - HL B DP - Teansmeer DP B15P

-15:15 kPa HL B - Upper plenum DP - Transmeter DP-B16P O : 20 kPa Acc 8 insection hne DP - Transmdier DP B20E 50 50 kPa PRZ CMT B balance bne DP - Transmdter DP-828P O:100 kPa CMT B discharge kne DP - Transmdier DP-840E O 100 kPa CMTB DP - Transmater DP B4lE O 18 kPa CMTB-DP - Transmeter DP B42E O:18 kPa CMTB DP - Transmdter DP B43E O -18 kPa CMTB DP - Transmdter DP 844E O IB kPa CMT B CL balance hne DP Tsan*,metter DP B45E 50 50 kPa IRWST discharge hoe B DP Transmdter DP B6tE O 100 kPa.

CVCS DP Transmdter F 001 A 0 tuo kPa b W

~ ~ -... _

h i

TABLE 6.1 SPES-2 INSTRUMENTATION LIST PAge 4 or ic Locolson Type Tog Range Measurel Hydraulic Potometer Potometer DP DP und head M

O Ma m usu vakso Maximum vokse Tubular downcomer Veresri-DP F-003P O:80 kPa ithular downcomer Venturi - DP F 003P 0;6 kPa j

DC -UH bypass Venhari DP F 014P O:100 kPa DC -tMi bypass Venhari-DP F-014P 0 to kPa NRHR A Onkce - DP F-A00E O:700 kPa CL Al venturi-DP F A01P O:60 kPa

-- t CL Al Venturi-DP F-A01P O;5 kPa

[

i MFW A Ortce - DP F-A01S 0:200 kPa CL A2 Venturi-DP F-A02P O :60 kPa CL At Venturi-DP F A02P O;5 kPa SG A downcomer Venturi - DP F-A02S 0:100 kPa 1

SG A downcomer Venturi - DP F-A03S 0:100 kPa MSL A Ventun - DP F A04S 0:500 kPa l

m kPa SFW A Onhce - DP F-A20A 0:100

_ kPa Amumusamos A sigacmonis.

Ventun - DP F A20E O 50 CMT A insection kne Venturi-DP F A40E O 20 kPa iRWST anpoctionkne A Ventun - DP F-A60E O 20 kPa

(

PRHR raturn hne Venturi-DP F-A80E O 30 kPa t

NRHRB Onkce - DP F-800E O:700 kPa l

CL 81 Venturi-DP F-801P Ot60 kPa

~

CL BI Ventari - DP F-801P 0,5 kPa MFW B Onkce DP F BOIS

.0:200 kPa CL B2 Veneurs - DP F B02P O:60 kPa l

CL B2 Venturi DP F-802P '

O.5 kPa

(

l' SG B downcomer Ventun - DP F-802S 0-100 kPa i

SG B downcomer Ventun - DP F B03S 0:100 kPa I

MSLB Ventun - DP FB04S 0.500 kPa-l ll SFW B Onhce - DP F-B20A 0: 100' kPa l

Aaumun.co, e ine. coon ism.

Venturi - DP F-B20E

'O 50 kPa l-CMT B insection kne venture - DP F-840E O 20 kPa j

1RWST engection line B Venturi DP -

F B60E O 20 kPa PHZ DP Transnutter L 010P O 66 2'3 kPa 1

[

g.

TABLE 6.1 SPES-2 INSTRUMENTATION LIST Pacc 3 of u,

Locofion Type log Range

Measused, Hydsouhc Posometes Potometer DP OP unit hood M

Q Muumimu Vokse Moumum Vint n-IRWST DP - Transmuoi L-060E O-100 kPa SG A DP - Transmeer L-A10S 0 :134 16 kPa Accumulator A DP - Transmeer L-A20E O. 70 kPa SG A DP - Transmeer L A20S 0 2609 kPa CMTA DP Transmeer L-A40E O 61 kPa SG B OP Transmeer L-BIOS 0:134 16 kPa Accumulator B DP - Transmeer L-820E O : 70 kPa SG B DP Transmear L-B20S 0 ;26 09 kPa CMTB DP - Tsansmeer L-840E O :61 kPa Tubular downcomer P - Transmeter P-00 t P O 1 : 20 1 MPa ADS 1.2.3 header P - Transmeter P-003P 01:201 MPa PC Upper Head P - Transmeter P-017P 01:201 MPa PHZ P - TransnWier P-027P 01 : 20 t MPa un ADS 1,2,3 header P - Transmeter P-030P

'O.1 :20 1 MPa ADS 4 headet P - Transmeter P-040P O i : 201 MPa MFW A P - Transmeter P A0tS 01;101 MPa HL A P - Transmeter P-A04P 01:201 MPa MSL A P - Transmater P-A04S 01:101 MPa Accum2!asor A P - Transmeter P A20E O 1 : 10 t MPa CMTA P - Transmeter P A40E 0.1 : 20.1 MPa MFW B P - Transmeter P B01S 0 t : to 1 MPa HL B P - Transmeter P BO4P O 1 :20 1 MPa MSL B P - Transmeter P B04S 0t to 1 MPa Accumulator B P - Transmeter P-820E e 1.101 MPa CMTB P - Transmeter P-B40E O 1. 20 t MPa Break hoe c=-=_---

DE-00tPA 1 - 1000 kg/m2 Break hne c _- -:

DE-001PB 1-1000 kg/m3 ADS 1.2.3 header c=- --

_u DE-030PA 1 1000 kg/m3 DE 030PB l-t000 kg/m3 ADS 1,2,3 header c=

ADS 1,2,3 header G.mnammis*=mn DE-030PC 1-1000 kg'm3 ADS 4 header cm n.mnis==nn=n DE-040PA 1-1000 kg'm3 kom3l DE 040PB I 1000 ADS 4 i eader u.m ia-n C

TABLE 6.1 SPES-2 INSTRUMENTAILON_ LIST._.

Pag s or ic Locolson Type Tog Hongo Measure Hydroulec Potometes Potometer DP DP unsi head M

Q Momtsn Votue iMonmorn Vota-i k

DE 040PC 1 - 1000 kym3 l

ADS 4 header Gammmennaamma.

k/m3 DE A0tPA 1-1000 0

I HL A DE A0tPB t-1000 kg/m3 HL A HL A Gasemmennems DE-A31PC 1 - 1000 kym3 Tubular downcomer Turtune F-002P

/

m3/s Break kne Turtune F-005P

/

m3/s Surge hne PR Turtune F-0ISP

/

m3/s ADS 1,2,3 header Turtune F-030P

/

m3/s ADS 4 header Tustane F-040P

/

m3/s HL A Tustune F-A10P

/

r.13!s PC power busbar Shunt 101P O:10000 Ac c PC power busbar Shunt 102P O:10000 Ac c PC power busbar Shust I03P 0:10000 Ac c m

PC power busbar Shunt 104P O:10000 Ac c PC power busbar Shunt 105P 0:10000 Acc.

PC power busbar Shunt 106P O:30000 Ac c RP A Amp meter I-A1P

-140:140 Ac c RP B Amp meter i BtP

-140:140 Ac c.

SG A. SG B outlet mass Catch tank IF001S 0:1400 kg IF005P O: 1400 kg Break kne Catch tank e

ADS 1.2.3 header Catch tarA IF030P O:1400 kg ADS 4 header Catch tar

IF040P 0:1400 kg RP A achymeter S A1P 6000 :6000 RPM RPB tachymeter S BIP 6000.6000

RPM, CVCS Thermoucouple K T-001A 50 :400

C

/

24 1993 3 9262

/

A Tubular downcomer Thermoucouple K T 00tP 50 :400

C

/

24 1993 3 9262

/

'r Tubular downcomer iismocouple K T-001PH 50.400

C

/

24 1993 3 9262

/

Tubular downcomer Thermocouple K T-00lPL 50.400

C

/

24 1993 3 9262

/

MFW header Thermoa de K T-001S 50.400

C

/

24 1993 3 9262

/

Tubular downcomer Ttemoucouple K T-002P 50 400

'C

/

24 1993 3 9262

/

t Tubular downcomer Thermoucouple K T003P 50 400

-C

/

24 1993 3 9262

/

lTututar downtomer Thesmoccuple K T 003PH 50 400 C

/

24 1993 3 9262

/

n m

u

I TABLE 6.1 SPES-2 INSTRUMENTATION LIST iwr i a ic i

Locoton Type lo Range Measure Hydroutc Potometer Posometer DP DP w

unit head M

Q Msunun Value Mournum vih -

Tubular downcomer Themwayde K T 003PL 50 : 400

C

/

24 1993 3 9262

/

DC lower pienum Therma-Ja K T 004P 50. 400

C

/

24 1993 3 9262

/

DC - UH bypass Thermocouple K T-Ot4P 50 :400

C

/

24 1993 3 9262

/

Upper pienum Thermocouple K T-015P 50 :400

C

/

24 1993 3 9262

/

Upperhead ThornwaT a K T-01GP 50 : 400

C

/

24 1993 3 9262

/

d Surge hne Thermocouple K T-018P 50 :400

C

/

24 1993 3 9262

/

Su'Debne Thermocouple K T-019PH 50 :400

C

/

24 1993 3 9262

/

Su'De noe ThernwaT e K T-019PL 50.400

C

/

24 1993 3 9262

/

d Surge bne Thornwayde K T-020P 50 :400

C

/

24 1993 3 9262

/

PRZ Thermocouple K T-021P 50 : 400

C

/

24 1993 3 9262

/

PRZ Thermoccupie K T-022P 50 :400

C

/

24 1993 3 9262

/

PRZ Thermocouple K T-023P 50 : 400

C

/

24 1993 3 9262

/

PRZ Thermocouple K T-024P 50 : 400

C

/

24 1993 3 9262

/

m PRZ Thermocouple K T-025P 50 :400

C

/

24 1993 3 9262 i

/

y PRZ Therrrwa yde K T-026P 50 :400

C

/

24 1993 3 9262

/

ADS 1.2.3 he&

Thermoccuple K T-030P 50 :400

C

/

24 1993 3 9262

/

Annular downcomer Thermocouple K T-031P 50 : 400

C

/

24.1993 3 9262

/

Annular downcomer Thernoccuple K T 032P 50 : 400

C

/

24 1993 3 9262

/

Arwular downcomer Thermocouple K T-033P 50.400

C

/

24.1993 3.9262

/

Annular downcomer Thernwayde K T-034P 50 :400

C

/

24 1993 3 9262

/

Annular downcomer Thermocouple K T-035P 50 :400

C

/

24 1993 3 9262

/

-)

f Annular downcomer Thermoccuple K T-036P 50 : 400

C

/

24 1993 3 9262

/

ADS 4 header Thernwayde K T-040P 50 :400

C

/

24 1993 3 9262

/

Annular downcomer Themocouple K T-041P 50 :400

C

/

24 1993 3 9262

/

Annular downcomer Thermocouple K T-042P 50 : 400

C

/

24 1993 3 9262

/

Annular downcomer Thermocouple K T 043P 50 :400

C

/

24 1993 3 9262

/

Annular dowrcomer Thermocouple K T 044P 50 :400

C

/

24.1993 3 9262

/

Annular downcomer Thermocouple K T-045P 50 - 400

C

/

24 1993 3 9262

/

Arwular downcomer Thermoccuple K T-046P 50 400

-C

/

24 1993 3 9262

/

I l

IRWST RTD - PT100 T 06tE 20 - 120 "C

/

IRWST RTD - PT100 1 062E 20 - 120

-C

/

{

IHWST RTD - PT100 T 063E 20-120

-C

/

)

t QW

- - _ - - _ _ _ -. _. _ ~.

TABLE 6.1 SPES-2 INSTRUMENTATION _UST eAcca or in I

Localson Iype log Range Measur 3 Hydrouhc Porometer Porometef DP DP unit heott M

O Mnantan value Monunum Vokie IRWST RTD - PT100 T 064E 20 -120

C

/

jY,

/

tRWST RTD - PT t00 T 065E 20 - 120

C

/

t.

?

I DVIA Therrrwayle K T A00E 50 ' 400

C

/

24 1993 3 9262

/

O CL NI Pump outbt Thermocouple K T A011P 50 400

C

/

24 1993 3 9262

/

CL N2 Pump outht Thermocouple K T-A012P 50 :400

C

/

24 1993 3 9262

/

PurTp A outlet Thermoccup&e K T-A0 t P 50 : 400

C

/

24 t993 3 9262

/

MFW A Thermocouple K T-A01S 50:400

C

/

24 1993 3 9262

/

CL N1 DC miet, vert. pos Thermocouple K T-A021PL 50 :400

C

/

24 1993 3 9262

/

CL N1 DC inlet, honz. pos Thermccouple K T-A021PO 50 :400

C

/

24 1993 3 9262

/

CL N2 DC miet. vest. pos Thernwaple K T A022PL 50 :400

C

/

24 1993 3 9262

/

CL N2 DC miet, horu pos Thermocouple K T-A022PO

$0 : 400

C

/

24 1993 3 9262

/

NRHR A Thermocouple K T-A02E 50 : 400

C

/

24 1993 3 9262

/

SG A downcomer Thermocouple K T.A02S 50 :400

C

/

24 1993 3 9262

/

CL At bend, vert pos.

Thermoccupde K T-A03tPL. 50'400

C

/

24 1993 3 9262

/

CL A2 bend, vert pos.

Thermocouple K T-A032PL 50 :400

C

/

24 1993 3 9262

/

HL A. vert pos.

Thermocouple K T-A03PL 50 :400

C

/

24 1993 3 9262

/

HL A. hortz. pos.

Themwaple K T-A03PO 50 :400

C

/

24 1993 3 9262

/

SG Adowncomes Thermocouple K T A03S 56 : 400

C

/

24 1993 3 9262

/

HL A SG mlet Thermpie K T-A04P 50 :400

C

/

24 1993 3 9262

/

MSL A Thermocouple K T.A04S 50 :400 "C

/

24 1993 3 9262

/

SG A U tube hot sade Thermocouple K T-A05P 50 :400

C

/

24 1993 3 9262

/

SG A nser hot side Thermocouple K T A05S 50 :400

C

/

24 t993 3 9262

/

SG A U-tube hot sede Thermocouple K T-A06P 50 : 400

C

/

24 1993 3 9262

/

SG A nser hot sde Thermocouple K T-A06S 50 : 400

C

/

24 1993 3 9262

/

SG A U tube top Thermocoupie K T A07P 50 : 400

C

/

24 1993 3 9262

/

SG A nser Thermocouple K T A07S 50.400

C

/

24 1993 3 9262

/

SG A U-tube cold sade Thermocouple K T-A08P 50 : 400

-C

/

24 1993 3 9262

/

SG A nser cold sade Thermocouple K T. A08S 50 400

C

/

24.1993 3 9262

/

SG A U-tube cold sde Thermocouple K T-A09P 50 ~ 400

-C

/

24 1993 3 9262

/

SG A user cold sde Thermocouple K T A09S 50.400 "C

/

24 1993 3 9262 PS A SG outlet Thermocouple K T A10P 50 400

'C

/*

24 1993 3 9262

/

't Purm suction A Thermommie K T At1P 50 400

-C

/

24 1993 3 9262 I

/__

Emm

l TABLE 6.1 SPES-2 INSTRUMENTATION LIST exac9 or u.

Locolson Type log Rongo Measure Hydrouhc Potomeles Porceneter DP DP unat hood M

Q Mounum Value Moxwnum Voka-CMT A CL balanco toe Thermocouple K T A14tP 50 400

C

/

24 1993 3 9262

/

CMT A CL balance Ine Thermocouple K T. A142PH 50 : 400

C

/

24 1993 3 9262

/

CMT A CL balance toe Thermocouple K T A142PL 50 :400

C

/

24 1993 3 9262

/

CMT A CL balance lee Ttwmamp K T-A143P 50.400

C

/

24 1993 3 9262

/

PRHR Thermarr=gde K T-A18t E 50 : 400

C

/

24 1993 3 9262

/

PRHR Therrrwr= gda K T A182E 50 :400

C

/

24 1993 3 9262

/

SFW Ther m ydaK T-020A 50 :400

C

/

24 1993 3 9262

/

Accumulator A Themwr=gda K T-A21E 50 :400

C

/

24 1993 3 9262

/

AauneAmear A mentaan ins Thermocouple K T-A22E 50.400

C

/

24 1993 3 9262

/

aaumusmein A spchan nne Thermocouple K T A23E 50:400

C

/

24 1993 3 9262

/

PRZ CMT Abalance kne Thermocouple K T-A27P 50 : 400

C

/

24 1993 3 9262

/

PRHR Thesmocouple K T-A281E 50 :400

C

/

24 1993 3 9262

/

PRZ CMT A balance Ime Thermocouple K T A28P 50 : 400

C

/

24 1993 3 9262

/

m PRZ CMT A balance kne Thermocouple K T-A29P 50 : 400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T-A401E 50 :400

C

/

24 1993 3 9262

/

CMT A Thermamgde K T-A402E 50 : 400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T-A403E 50 : 400

C

/

24 1993 39262

/

CMTA Thermocouple K T-A404E 50 :400

C

/

24 1993 3M

/

CMTA Thermocouple K T A405E 50 : 400

C

/

24 1993 3 9262

/

l CMTA Thermocouple K T A406E 50 :400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T-A407E 50 : 400

C

/

24 1993 3 9262

/

I CMTA Timmocomple K T A408E 50.400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T-A409E 50 : 400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T-A410E 50 :400

C

/

24 1993 3 9262

/

CMTA Thermo60uple K T-A411E 50 :400

C

/

24 1993 3 9262

/

CMTA Tiemoccuple K T-A412E 50.400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T-A413E 50.400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T A414E 50.400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T-A4ISE 50 400

C

/

24 1993 3 9262

/

CMTA Thermocouple K T A416E 50 400

-C

/

24 1993 3 9262

/

CMTA Thermocouple K T A417E 50.400

~C

/

24 1993 3 9262

/

CMTA Themmoople K T A4iBE 50 400

-C

/

24 993 3 921,2

/

TABLE 6.1 SPES-2 INSTRUMENTATION l.lST rAc.c to or u.

Location Type 109 Range Measuse Hyorouhc Potometes Potonicles l>P DP urut head M

Q Maumum Vokse Maxunum Vokn-CMIA Thermoccuple K T-A419E 50 :400

C

/

24 19S3 3 9262

/

C M T A air Themwaple K T-A41 A 50 : 400

C

/

24 1993 3 9262

/

CuiA Thermocouple K T-A420E 50 400

C

/

24 1993 3 9262

/

CMT A insectionime Themwapaa K T-A421E 50.400

C

/

24 1993 3 9202

/

CMT A wipection kne Themwa pia K T-A422E 50 :400

C

/

24 1993 3 9262

/

CMT A air Thermocoup3e K T-A42A 50 :400

C

/

24 1993 3 9262

/

IRWST discharge hne A Thermocouple K T-A66E 50 :400

C

/

24 1993 3 9262

/

PRHR supply hne Thermocouple K T-A8tE 50 :400

C

/

24 1993 3 9262

/

PRHR supply hne Thermocouple K T-A82E 50 :400

C

/

24 1993 3 9262

/

PRHR resum kne Thermocouple K T A83E 50 :400

C

/

24 1993 3 9262

/

PRHR retum kne Thermocouple K T-A84E 50 : 400

C

/

24 1993 3 9262

/

DVIB Thermocouple K T-800E 50 : 400

C

/

24 1993 3 9262

/

CL B/2 Pump outlet Thermocouple K T-8011P 50 :400

C

/

24 1993 3 9262

/

0 CL B/2 Pump outnet Thermocouple K T-8012P 50 :400

C

/

24 1993 3 9262

/

m Punp B outlet Thermocouple K T-BOIP 50 : 400

C

/

24 1993 3 9262

/

MFW8 Thermocouple K T-801S 50 :400

C

/

24 1993 3 9262

/

CL B/l DC inlet. vert. pos.

Thermocouple K T-8021PL 50 : 400

C

/

24.1993 3 9262

/

CL B/1 DC intet. honz. pos Thornwapaa K T-8021PO 50 :400

C

/

24.1993 3 9262

/

CL B/2 DC enlet, vert pos.

Thermocouple K T-8022PL 50 : 400

C

/

24 1993 3 9262

/

CL B/2 DC inlet, honz. pos Thornwa pfe K T-8022PC 50 :400

C

/

24 1993 3 9262

/

NRHRB Thermocouple K T-802E 50 : 400

C

/

24 1993 3 9262

/

SG B downcomer Thermocouple K T-802S 50 :400

C

/

24 1993 3 9262

/

CL Bt bend, vert. pos-Thermocouple K T 8031PL 50 :400

C

/

24 1993 3 9262

/

CL B2 bend vert pos.

Thermocouple K T 8032PL 50.400

C

/

24 1993 3 9262

/

HL B. vert pos.

Thermocouple K T-803PL 50.400

C

/

24 1993 3 9262

/

HL B. horiz. pos Thermocouple K T-803PO 50.400

C

/

24 1993 3 9262

/

SG B downcomer Thermocouple K T-803S 50 :400

C

/

24 1993 3 9262

/

HL B SG ndet Thermocouple K T-804P 50 :400

C

/

24 1993 3 9262

/

I MSLB Thermocouple K T B04S 50 400

C

/

24 1993 3 9262

/

l SG B U tube hot side Thermocouple K T B05P 50 400

~C

/

24 1993 3 9262

/

SG B nser hot side Thermocouple K T-BOSS 50 400

-C

/

24 1993 3 9262

/

SG B U-tube hot side Thermocouple K T B06P 50 400 C

/

24 1993 3 9262

/

_j

_____..__._.___________________.__._._.________.__________________mm

TABLE 6.1 SPES-2 INSTRUMENTATION LIST nuC n or i6 Locotion Type fog Range Measure Hydrouhc Potomete Potometer DP tw urut head M

O Mainnuen Vosue Moumwn Vukie SG B reser hot sade Thermocogie K T 806S 50.400

C

/

24 1993 3 9262

/

SG B U-tube top Thermnemple K T-807P 50 ~ 400

C

/

24 1993 3 9262

/

SG B nser Thermarmfaa K T-B07S 50 :400 C

/

24 1993 3 9262

/

SG B U-tube cold sade Thermammfaa K T-806P 50 : 400

C

/

24 1993 3 9262

/

l SG B reser cold sade Thermnm=,aa K T-BOSS 50 :400

C

/

24 1993 3 9262

/

SG B U-sube cold sade Thermneafaa K T-809P 50 400

C

/

24 1993 3 9262

/

SG B nser cold side Thermnem9am K T 809S 50 : 400

C

/

24 1993 3 9262

/

PS B SG cuttee Therm 9am K T-B10P 50 :400

C

/

24 1993 3 9262

/

Purg suction B Therm 9aa K T-911P 50 :400

C

/

24 1993 3 9262

/

CMT B CL balanceline Ther m @ K T-B141P 50 :400

C

/

24 1993 3 9262

/

CMT B CL balance inne Thermocouple K T-B142PH 50 :400

C

/

24 1993 3 9262

/

CMT B CL balance hne Thermocouple K T-B142PL 50 :400

C

/

24.1993 3 9262

/

M CMT B CL balance hne Thermarmpaa K T 8143P 50 : 400

C

/

24 1993 3 9262

/

Accumulasor B Thermnempaa K T-821E 50 : 400

C

/

24 1993 3 9262

/

Accumutamm e mystman kna Ihermnempse K T-822E 50 :400

C

/

24 1993 3 9262

/

Accuma.== a agacaon hne Thermnemf e K T-B23E 50 :400

C

/

24 1993 3 9262

/

i PRZ CMT B balance boe Thermnem paa K T-827P 50 : 400

C

/

24 1993 3 9262

/

PRZ CMT B balam:e bne Thermarmele K T-D28P 50 : 400

C

/

24 1993 3 9262

/

PRZ CMT B balance boe Thermarmpia K T-329P 50.400

C

/

24 1993 3 9262

/

CMTB Thermocouple K T-B401E 50 ;400

C

/

24 1993 3 9262

/

CMTB Thermaemf e K T-B403E 50 - 400

C

/

24.1993 3 9262

/

i CMTB Thermocouple K T B405E 50 : 400

C

/

24 1993 3 9262

/

CMTB Thermocouple K T-8407E 50 : 400

C

/

24 1993 3 9262

/

CMTB Thermocouple K T-8409E 50 :400

C

/

24 1993 3 9262

/

CMTB Thermocouple K T B411E 50 : 400

C

/

24 1993 3 9262

/

2 CMT B Thermocouple K T-B413E 50.400

C

/

24 1993 3 926?

/

CMTB Thermocouple K T-B41SE 50 :400

C

/

24 1993 3 9262

/

CMiB Thermocouple K T 8417E 50 400 "C

/

24 1993 3 9262

/

CMT B air Thermocouple K T-B41 A 50 :400

C

/

24 1993 3 9262

/

CMTB Thermocouple K T B420E 50 :400

'C

/

24 1993 3 9262

/

CMT B insection bne Thermocouple K T B421E 50 400

-C

/

24 1993 3 9262

/

CM T B wisection bne Thermocouple K T-8422E 50 400 C

/

24 1993 3 9262

/

i___

~~------____m.__.______________

f l

TABLE 6.1 SPES-2 INSTRUMENTATION LIST eAct i2 01 it Locotson Type log Range Measure Hydroubc Potometer Poroinefer (3'

DP orut htxx1 M

Q Ma urin an Vuh ne Monunurn vohr CMT B aw Thermnen ple K T B42A 50 40G

C

/

24 1993 3 9262

/

IRWST discharge bne B Therrrwaple K T B66E 50 -400

C

/

24 1993 3 9262

/

Armular downcorner Thermnent e K TW 00tP 50 400

C

/

24 1993 3 9262

/

i Annular downcomer Thermnea@ K TW-002P 50 -400

C

/

24 1993 3 9262

/

Annular downcomer Thermnra@ K TW-003P 50 -400

C

/

24 1993

_ 3 9262

/

Annular downcomer Thermnempia K TW-004P 50 ;400

C

/

24 1993 3 9262

/

Annular downcorrer Thermaca @ K TW-005P 50 :400

C

/

24 1993 3 9262

/

Annular downcomer Thermnea paa K TW-006P 50.400

C

/

24 1993 3 9262

/

Annular downcomer Thermoccupie K TW 007P 50 : 400

C

/

24 1993 3 9262

/

Annular downcomer Thermocouple K TW 008P 50 :400

C

/

24 1993 3 9262

/

SG A U tube hot sede Thermocouple K TW A05S 50 :400

C

/

24 1993 3 9262

/

SG A U tube hot sde Thermnea vie K TW-A06S 50 :400

C

/

24 1993 3 9262

/

o SG A U-tube Thermneapaa K TW A07S 50 :400

C

/

24 1993 3 9262

/

SG A U tube cold sade Thermocouple K TW-A08S 50 :400

C

/

24 1993 3 9262

/

SG A U tube cold sde Thermocouple K TW409S 50 : 400

C

/

24 1993 3 9262

/

SG A downcomer Thermocouple K TW-AlOS 50: 400

C

/

24 1993 3 9262

/

SG A reser Thermocouple K TW At1S 50 : 400

C

/

24 1993 3 9262

/

PRHR Thermocouple K TW-A181E 50 :400

C

/

24 1993 3 9262

/

PRHR Thermocouple K TW-A182E 50.400

C

/

24 1993 3 9262

/

PRHR Thermocouple K TW A183E 50.400

C

/

24 1993 3 9262

/

PRHR Thermnemple K TW A281E 50 : 400

C

/

24 1993 3 9262

/

CMT A contaavnent tar

Thermocouple K TW A41 AE 50 :400

C

/

24 1993 3 9262

/

CMT A containment tar

Theemnem pie K TW-A41 Al 50 -400

C

/

24 1993 3 9262

/

CMT A Thermnemple K TW-A41E 50 : 400

C

/

24 1993 3 9262

/

CMT A containment tar

Thermocouple K TW A42AE 50 : 400

C

/

24 1993 3 9262

/

CMT AcontarvnenttarA Thermocouple K TW A42Al 50 '400 "C

/

24 1993 3 9262

/

CMTA Thermocouple K TW-A42E 50 : 400

C

/

24 1993 3 9262

/

CMTA Thermocouple K TW A43E 50 400

C

/

24 1993 3 9262

/

CMTA Ihermocouple K TW A44E 50 400

~C

/

24 t993 3 9262

/

CMTA Thermocouple K TW A45E 50.400

'C

/

24 1993 3 9262

/

CMIA Itemocouple K TW A46E 50 400

-C

/

24 1993 3 9262

/

lCMIA Thesmocouple K TW A47E 50 400 C

/

24 1993 3 9262 i

i I

l l

i i

TABLE 6.1 SPES-2 INSTRUMENTATION LIST PAGE 13 or s o

(

l 1.ocation Type log

(?onge Measure Hydsoulic Poromeles Porometer DP DP unal head M

Q Muunum Virtue Mamanum Vish.e l

j-CMTA Thernwagna K TW-A48E 50 : 400

C

/

24 1993 3 9262

/

l SG B U tube hot sade Thornwayda K TW BOSS 50 : 400

C

/

24 1993 3 9262

/

SG B U tube tw4 sade Themwag=a K TW-806S 50 :400

C

/

24 1993 3 9262

/

SG B U tube Thornwayda K TW B07S 50 :400

C

/

24 1993 3 9262

/

SG B U te cold sade T: = - ' -d-K -

TW-908S 50 : 400

C

/

24 1993 3 9262

/

/.

SG B U tube cold sade Therriw aapimK TW-BOCS 50 :400

C

/

24 1993 3 9262

/

SG B downcomer Therrrwayda K TW-BIOS 50:400

C

/

24 1993 3 9262

/

i-SG B reser Thermocouple K TW-B11S 50: 400

C

/

24 1993 3 9262

/

CMT B containment tark Thererwayda K TW-841AE 50 :400

C

/

24 1993 3 9262

/

CMT B contasnment tar

Thorstwayda K TW-841At 50 :400

C

/

24 1993 3 9262

/

CMTB~

T hornwagda K TW-84IE 50 : 400

C

/

24 1993 3 9262

/

CMT B containment tare Therivwayda K TW-B42AE 50 :400

C

/

24 1993 3 9262

/

l CMT B containment tar

Ther e geaK TW 842Al 50 : 400

C

/

24 1993 3 9262

/

w

~

CMTB Thorstwagda K TW B44E 50 :400

C

/

24 1993 3 9262

/

CMTB Thornwagna K TW-846E 50 :400

C

/

24 1993 3 9262

/

CMTB Thornwap K TW 848E 50 :400

C

/

24.1993 3 9262

/

PC rod bundle Thornwagen K TWO11P07 100 :600

C

/

24 1993 3 9262

/

i PC mdbunde Thorvewayda K '

TWO1IP11 100:600

C

/

24 1993 3 9262

/

PC rod bunde Thornwagda K TWO11P53 100 :600

C

/

24 1993 3 9262

/

PC sod bunde Thorstwaqda K TWO11P82 100:600

C

/

24 1993 3 9262

/

PC sod bunde Thereqda K TWOI tP83 100:600

C

/

24 1993.

3 9262.

/

PC rod bundle Thorstwagda K _

TWO11P91 100:600

C

/

24 1993 3 9262

/

PC md bundle Therstwagde K TWO12P47 100 :600

C

/

24 1993 3 9262

/

PC rod bunde Thermccouple K TWO12P71 100:600

C

/

24 1993 3 9262

/

PC rod bunde Thermocouple K TWOt3P61 100:600

C

/

24 1993 3 9262

/

i PC rod bundle Thermocouple K.

TWO13P68 100 :600

C

/

24 1993 3 9262

/

PC rod bundle Thernwmyea K TWO14P41 100:600

C

/

24 1993 3 9262

/

PC tod bundle ihermocouple K TWOt4P44 100.600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWOI4P49 100 :600 "C

/

24 1993 3 9262

/

PC rod bundle Thesmocouple K TW0 4P68 100-600

C

/

24 1993 3 9262.

/

PC rod bundle Thermocouple K IWO1SP07 100 :600

~C

/ '

24 1993

.3 9262

/

PC sod bundle Therir+_v _W K TWOISP11 100 600 C

/

24 1993 3 9262

/

i e

m 1__,_._.

-w-

TABLE 6.1 SPES-2 INSTRUMENTATION LIST eAue 14 or is Locolson Type log RonOo Moosure Hydroulo Posomete Potometer DP DP unit head M

O Mamum Volue Maximum votoe PC rod bundle Ttwmoccuple K TWOt SP23 100:600

C

/

24 1993 3 9262

/

PC rod tundle Therrwr= yde K TWOtSP39 100.600

C

/

24 1993 3 9262

/

PC rod bundle Thornwrwgaa K TWO15P53 100.600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TW015P83 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocogie K TWOt$P91 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TW016P14 100 :600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWO16P37 100:600

C

/

24.1993 3 9262

/

PC rod bundle Thermocouple K TWO16P41 100 :600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TW016P44 100 :600

C

/

24 1993 3 92r

/

PC rod bundle Thermocouple K TW016P68 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TW016P82 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWOt7P03 100 :600

C

/

24. t993 3 9262

/

PC rod bundle Thermocouple K TW017P27 100 :600

C

/

24 1993 3 9262

/

g PC rod bundle Thermocouple K TWO17P64 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TW017P79 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWOt8P03 100 :600

C

/

24 1993 3 9262

/

PC sod bundle Themocouple K TWO1SP07 100 :600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWO18P37 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWOt8P44 100:600

C

/

24.1993 3 9262

/

PC rod bundle ihermocouple K TW018P64 100:600

C

/

24.1993 3 9262

/

PC rod bundle Thermocouple K TWO18P91 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWOI9P03 100 :600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWO19P37 100 600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWOI9P41 100.600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWO19P64 100:600

C

/

24 1993 3 9262

/

PC tod bundle Thermocouple K TWO19P82 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWO20P03 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWO20P07 100:600

C

/

24 1993 3 9262

/

PC tod bundle Thermocouple K TWO20P27 100'600 "C

/

24 1993 3 9262

/

PC eod bundle Thermocouple K TWO20P37 100 600 "C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K 1WO20P41 100:600

~C

/

24 1993 3 9262

/

PC rod bundle Ihermocouple K TWO20P44 100 600

'C

/

24 1993 3 9262

/

TABLE 6.1 SPES-2 INSTRUMENTATION LIST cAct 13 or u, Localon Type fog Range Measure Hydroulac Potomete Potomete#

DP DP und head M

Q Mrsnman Votue Maxwnum Vok as PC rod bundle Then@ K TWO20P49 100:600

C

/

24 1993 3 9262

/

PC tod buncte Th-- -yde K TWO20P53 100 -600

C

/

24 1993 3 9262

/

PC tod bundle Thermocouple K TWO20P64 100 :600

C

/

24 1993 3 9262

/

PC rod bundle Thermocouple K TWC20P68 100 :600

C

/

24 1993 3 9262

/

PC tod bundle Thermocouple K TWO20P79 100 :600

C

/

24 1993 3 9262

/

PC rod bundle ThermamW K TWO20F82 100:600

C

/

24 1993 3 9262

/

PC rod bundle Thermoccuple K TWO20P91 100 :600

C

/

24.1993 3 9262

/

PC tod bundle Voltmeser V-01P 0:160 DC

/

RPA Voltmeter V-AIP 400 :400 DC

/

0 08 0

/

RP B Voltmeter V-B1P

-400 : 400 DC

/

0 08 0

/

PHZ Wattmeter W-027PE1 0.6000 W

/

w PRZ Wattmeter W-027PE2 0 :6000 W

/

PRZ Wattmeter W 027PE3 0 6000 W

/

PHZ Wattmeter W-027P1

O:6000 W

/

PRZ Wattmeter W 027PEM 0:6000 W

/

PRZ Wattmeter W-027Pt 0:24000 W

/

ADS 1 Limd swdch Z-001PC

-1 : 1 bd

/

ADS 1 Lamd swach Z-001PO

-1 : I bd

/

ADS 1 Lwnd swech Z-001PC

-1 : I bd

/

ADS 1 Limd swech Z 001PO

-1. I bd

/

ADS 2 Lwt* swech Z-002PC

-1 : 1 bd

/

ADS 2 Lwnd swech Z-002PO

-1 : 1 bd

/

ADS 3 Land swdch Z-003PC

-1.1 bl

/

ADS 3 Lims swech Z-003FO 1:1 bd

/

MFW Aisolaton valve Lund swach Z-A02SC

-1 : 1 tut

/

MFW AisolationvaNe Lund swech Z-A02SO

-1.1 bd

/

ADS 4 A Lund swach Z-A04PC

-1,1 tut

/

ADS 4 A Lund swdch Z-A04PO

-1 1

tut

/

MSL A isolaton vane Land swach Z-A04SC

-1 1

tut I

/

MSL A esoiaton valve L:ma swech Z A04SO

-1 1

bit

/

i SG A PORV Lwne swdch Z-A06SC

-1 1

bit

/

SG A PORV Luis switch Z A06SO 1 1 bet

/

-/

/

i

W TABLE 6.1 SPES-2 INSTRUMENTATION LIST eAce is or is locolson Type log Range Moosure Hydroulac Porarnetes Pororneter DP Op unal hood M

Q Mawntan Value Moxwnusn Voto.-

l CMT A insecten hne Larut swech Z-A40EC

-1. I txt

/

I CMT A syecten kne Lotut swech Z-A40EO t.I txt

/

CMT A CL balance hne Luvut swech Z-A45PC 1I txt I

/

CMT A CL balance hne Luvut swech Z-A45PO

-1 : 1 twa

/

PRHH supply kne Luna swech Z-A81EC 1:1 txt

/

PRHR supply kne Linut suech Z-A81EO

-1 : 1 tat I

/

MFW B esolaten valve Lune swech Z-B02SC

-1 : 1 txt

/

MFW Bisotalenvalve Luna swech Z-802SO

-t. I tnt

/

ADS 4 B twns swech Z-804PC

-1 : 1 tut

/

ADS 48 Lwrit swech Z-904PO

-t ; 1 tut I

/

MSL B isolation valve t.une swech Z-804SC

-1 : 1 tut

/

MSL 8 isolaten va6ve Lwns swech Z-804SO

-1 : 1 tut

/

SG B PORV Lens swech Z B06SC 1:1 twt

/

SG B POf'V Luna swech Z-806SO

-t ; I tut

/

CMT B wp kne Lt.la swech Z-840EC

-1 : 1 tut

/

I CMT B sjecten hne Lima swech Z 840E0 1:1 twa

/

CMT B CL balance hne Latutsw ch Z B45PC

-1 : 1 tut

/

i CMT B CL balance tw'.a Lwns swech Z B45PO

-1 : 1 tut

/

S O

3

~-

.~w v

.-~--s

~

m

i AP600, SPES-2 Integral System Test Specification 7.0 Data Acquisition System The test facility shall provide for a data acquisition system (DAS) that shall include the equipment necessary to monitor and transmit the output signals generated by the various -

instruments used both in the control and monitoring of the test loop.

A.

DAS Components The DAS is taken to include those signal amplifiers, signal conditioners, signal transmitters, signal converters (analog-to-digital and others that may be I'

used), switch panels, interface electronics, computers, power supplies, displays f

(CRT, strip chart recorders, gages, etc.), power supplies, and interconnected wiring, as needed to accomplish the test.

B.

Input Channels The DAS shall receive analog signals from various temperature and pressure sensors, flow meters, accelerometers, valve position indicators, and other l

instrumentation utilized for test operation and monitoring, and record them in a digital form. Shielded wiring shall be used for all signal input leads to minimize the pickup of noise in the signal. High frequency filters may also be used, where i

shown to be appropriate and agreed to by the test sponsor.

The test performer shall be responsible to assure that the DAS is capable of accepting and processing the range of output signals that can be generated by the various instruments that may be used during the course of testing.

C.

Control Functions The DAS shall provide control functions /actuations required to properly actuate the various valves and rod power power control discussed previously in Section 6.0.

D.

Sampling Rates The sampling rate of the instruments by the DAS shall be set by the physical phenomena being monitored and the response time of the instrument itself. To monitor rapidly changing or oscillating phenomena, rapid scanning rates are desired, while fewer scanning rates are acceptable for slower phenomena or slow response instruments. Thus, to provide for the efficient collection, storage, and handling of meaningful and useful data, the DAS may both sample different instruments at different rates during the course of a test, and may vary the sampling rate for various instruments at various times during a test.

06%1/H0493 35

The minimum sampling] rates for the instruments planned fo b ote that this sampling rate is a minimum value; N

faster sampling rates are acceptable. The use of slower sampling rates is to be reviewed and approved by the test sponsor prior to testing.

E.

System Accuracy Measurement errors associated for the various channels from sensor to DAS shall be documented. The following accuracies are desired:

Thermocouples e

e Flow Meters e Pressure Transducers e All other instrumentation F.

On-Line Data Storage The DAS shall have sufficient storage capacity in order to capture and store all digital data collected from a given test. The maximum duration of a test is not expected to exceed five (5) hours.

To provide for the basic instrument signals to be used for post-test data reduction and analysis, the data shall be stored by the DAS in the units of the instrument output (millivolts, milliamps, etc.), not in engineering units or SI units. An exception to this may be thermocouple output; it shall be acceptable to cenvert thermocouple output directly to units of temperature and store that converted signal during test.

G.

On-Line Display The DAS shall provide for the continuous on-line display of selected instruments or calculated test parameters before (pretest), during, and following (post-test) each test performed. In general, the information displayed shall be sufficient as to allow the test loop operators to assess the following:

o Initial test loop conditions meet those specified.

Expected events (valves opening or closing, flow passing along a flow path) o occur.

o No unexpected test events that might negate the test have occurred.

All data displayed on-line shall be in the appropriate engineering units; temperature, pressure, flow, and quality, as applicable.

mmm 36

The on-line display shall be by CRT. An echo to print file for inclusion in day of test reports is desireable.

H.

Test Validation i

The DAS shall have the ability to perform a post test validation check on the test performed. In general, a valid test shall satisfy the following three criteria; Sufficient instrumentation must be operable and recorded by the DAS to o

permit a mass balance and an energy balance to be calculated for the facility, o

Sufficient instrumentation must be operable and recorded by the DAS to assure that the data needs addressed by the test are satisfied.

Test conditions experienced should reasonably match those called for in the o

test matrix.

To guide in determining test validity, a test validation " check list" shall be established. This check list shall be reviewed by the DAS to summarize key parameters associated with the test. For parameters such as desired flow or pressure histories, a plot showing the desired history, the history observed during the test, and limits of variation about the desired history, may be an appropriate presentation for use in test validation. The check list and associated plots shall be printed post-test, along with a summary of other instrument outputs that are determined to be critical to a successful test, for review by the cognizant test engineer in assessing test validity.

I 1.

Data Transmittal Following post-test validation of the test, the test data shall be provided to the Westinghouse Electric Corporation on a magnetic medium (DEC TK-50 cartridge). As a minimum, the data tape is to contain the following information; o

Test Run File Header, containing the test run ID, date, and other pertinent information.

o Channel Assignment Table, associating instruments with specific DAS channels and identifying other information pertinent to instrument identification, Calibration file, containing all information necessary to account for shifts in o

zero settings and convert raw instrument outputs from volts to engineering units.

I i

WMIIM 37

.__m 2.

4-1 1

l o

Data, all the data from one channel, presented one channel at a time.

4 o

An end-of-file mark at the conclusion of the data for a given test.

i The specific format of the magnetic medium shall be approved by the test sponsor 1

prior to the initiation of testing. Also, a " prototype" data tape, containing signals typical of those to be provided during testing shall be provided to Westinghouse at least 30 days in advance of the initial testing in order to assure that the data l-file can be read by equipment available to the test sponsor.

J t-a 06ML110493 38

AP-600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION 8.0 Test Operation j

The operation of the test facility shall be established and documented in the test operating J

procedures. These operating procedures are to be provided by the testing organization and submitted to Westinghouse for review and approval (See Section 10, Quality 4

Assurance Requirements). Operating procedures shall be prepared for (but not be limited to) the following tests:

8.1 Facility Shakedown - Cold Pre-operational Tests 1

2 The following tests will be performed to assure the facility can be operated safely and to characterize, establish and verify that the piping DP's and flowrates are properly scaled to match the AP600. Instrumentation and control system l

calibration and function are to be verified as part of these tests.

l j

A.

Core Makeup Tank (CMT) l Each of the two CMT's shall be filled with cold water and drained by fully opening the tank discharge line isolation valve. The simulated primary system shall be at atmospheric pressure and shall be vented and drained so as to not j

affect the CMT draindown rate. Testing shall include:

l l

a)

Confirmation of the CMT level instrument calibration during filling and draining of the CMT's.

l b)

Confirmation of the operability of the CMT in-tank and tank wall l

thermocouples during filling and draining of the CMT's.

f c)

Individual draindown of the CMT's (with the CL to CMT balance line

~

l isolation valve fully open and the PRZ to CMT balance line isolation valve I

fully closed is to be initiated by opening the CMT discharge line isolation valve. The primary purpose of this test is to set the CMT discharge line resistance to be equal to the AP600, and verify the CMT discharge line flow measurement instrumentation.

Information to be obtained shall include:

CMT levels vs. time The CL to CMT balance line DP vs. flow (and CMT level)

Record the CMT discharge line and DVI line DP's Record the CMT discharge line flow vs. time oo+u lw) 39

d)

Individual draindown of the Chit's (with the PRZ to Chit balance line isolation valve fully open and the CL to CMT balance line fully closed),

initiated by opening the Chit discharge line isolation valve. The primary purpose of this test is to measure the resistance (DP vs. flow) of the PRZ to ChfT balance line, and characterize Ch1T draindown during this mode of operation. Information to be obtained shall include:

Chit level vs. time PZR to Ch1T balance line delta P vs. flow Chit discharge line and DVI line DP's CMT discharge line flow vs. time B.

Safety Injection (SI) Accumulator Each of the two Si accumulators shall be fully filled with cold water to verify level instrument operation, drained to 87.5% level, and then pressurized to ~700 psig with N gas after the N gas temperature has come to thermal equilibrium 2

2 the accumulator shall be drained at a range of initial flowrates by opening the accumulator discharge isolation valve to different throttling positions. The reactor coolant system is to be vented, via the ADS, to atmosphere during these tests in order to avoid pressurizing the RCS during the accumulator blowdown.

The main purpose of this test is to simulate the range of draindown rate and times that is expected to occur during the LOCA transient, to set / establish the accumulator discharge line resistance, and to measure the N gas expansion 2

coefficient. Information to be obtained shall include:

SI accumulator level vs. time SI accumulator discharge line DP vs. flow SI accumulator gas pressure and gas and water temperature vs. time C.

In-Containment Refueling Water Storage Tank (IRWST)

The IRWST shall be filled with water to a range of initial levels above the DVI nozzle elevation, and drained via both of the two IRWST discharge lines. The reactor coolant system is to be vented, and drained to atmosphere for these tests to avoid affecting the IRWST water driving head. The main purpose of these i

tests is to set / establish the IRWST discharge line resistance to be equal to the AP600. Information to be obtained shall include:

IRWST level vs. time IRWST discharge line and DVI line DP vs. flow 06%L'llo4M 40

4 D.

CVCS Makeup Pump and Normal RHR Pump The flowrate vs. discharge pressure of the high ar d low pressure pumped injection pumps shall be established to match the AP600 CVCS and NRHR pumps. The DP across each CMT discharge line orifice during NRHR pump operation should be determined.

E Steam Generator Start-up Feedwater Pump The flowrate vs. discharge pressure of the pump (s) to be used to simulate the AP600 SG startup feedwater pumps shall be established to match the AP600 startup feedwater pump head vs. flowrate.

F.

Primary Loop Flow and Dp's The primary system shall be filled and pressurized with N (to provide sufficient 2

RCP NPSH ) and the RCP's shall be started to establish and verify that the main 3

coolant loop flowrates and DP's simulate the AP600. In addition, these cold flowrate tests will provide the DP's throughout the reactor coolant system and the PRHR heat exchanger / piping. Information to be obtained shall include:

Cold leg DP's and verification that CL flows are equal DP and flowrate through the PRHR HX and piping with the reactor coolant pumps running Tests shall be run with 1 RCP running to establish loop reverse flow flows and DP's and the circumferential flows and DP's around the armular downcomer.

RCP coastdown time is to be measured and compared with the AP600 RCP coastdown time.

G.

Hydrotest A cold high pressure leak test shall be performed as required by applicable pressure vessel standards to establish the integrity of the test facility. This test should include identification of leaks and quantification of RCP seal in/out leakage.

H.

Test Facility Volume The volume of each of the main components of the SPES-2 facility including each section of the power channel shall be documented.

This may be done by calculation or by fill and draining or a combination of both.

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8.2 Facility Shakedown - Hot Preoperational Tests The following tests will be performed at hot and pressurized conditions to complete the facility characterization and to enable proper facility operation, measurement and interpretation of the simulated AP600 transients that will be performed. Tests to be performed will include the following:

A.

Steady State Heat Losses The facility shall be heated to and held at five constant temperatures, in order to determine the steady state heat losses from the facility. These heat loss tests shall be designed to enable the heat losses vs. temperature from the following individual components to be determined:

~

Power channel riser, upper plenum and upper head Downcomer (both annular and tubular sections).

Steam generators.

Reactor Coolant Pumps including heat loss due to seal injection / leakoff.

Pressurizer.

Hot and cold leg piping.

Surge line.

The temperature range for which heat losses are to be determined shall be from near 149 C (300*F) to 2 315'C (600*F) for the primary components.

However, the pressurizer heat loss shall be determined for temperatures from 175 C (350*F) to 343 C (650 F). In addition, the pressurizer heat loss test shall i

include measurements with only the pressurizer external heaters on and with only the pressurizer internal heaters on.

B.

Facility Heat Capacity A test shall be performed to quantify both the metal and water heat capacity of the facility and individual components. The tests shall be designed to enable the heat capacity of the following individual components to be determined.

Power channel, riser, upper plenum and upper head.

Downcomer (annular and tubular).

Steam generators.

Reactor coolant pumps.

Pressurizer.

Hot and cold leg piping.

Note, calculations for individual components can be performed in lieu of, or in addition to actual tests, however, an overall facility heat capacity test shall be performed.

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C.

Simulated Full Power Operation.

The facility shall be operated at normal full power pressure, and temperature at the scaled full power rod bundle power (~4.95 Mw). ' This test shall be used to verify proper operation of all components and instrumentation. This test shall include:

A determination of the facility in/out leakage.

Verification of RCP flow and loop flowrates.

Measurement of the individual component DP's and temperatures.

Verification of proper operation of the SG heat removal system (feedwater, level control, pressure control, steam condenscr, feedwater heaters, etc.).

Verincation of proper operation of the heater rod bundle and instrumentation.

Verification of the pressurizer heater, makeup water and PORV control systems.

D.

Hot Shutdown / Natural Circulation.

The facility shall be transitioned from the full power operating condition to a hot shutdown / natural circulation mode of operation. This test shall include:

Verincation of the rod bundle power transition to the proper decay heat vs.

time power level.

Characterization of the primary loop natural circulation flowrates vs. power level.

Verification of the proper RCP coastdown rate.

Verification of proper operation of the SG heat removal system at decay heat power levels.

Characterization of the PRHR heat exchanger flowrate, and heat removal rate vs. RCS temperature.

Characterization of the natural circulation heatup of each CMT at hot shutdown conditions.

E.

Low Pressure, Safety System Actuation.

A " low" pressure depressurization from approximately 400 psig using the ADS with CMT draindown shall be performed to demonstrate proper operation / control of plant trip (heater rod power control), SG feedwater isolation, CMT actuation, PRHR heat exchanger actuation, ADS, etc. These test results will be utilized to provide an initial sizing verification for the fourth stage of ADS and to provide a comparison with the Oregon State University, low pressure, part-height AP600 test facility.

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F.

Full Pressure, Safety System Actuation.

A test shall be performed from full power conditions to demonstrate actuation and i

performance of the safety systems including fourth stage ADS and IRWST 1

delivery. The heater rod power shall be controlled to match the scaled AP600' decay heat. This test shall be initiated by opening the first stage of the ADS.

8.3 AP600 Simulated Transient Tests The transient tests which shall be performed are listed and described in Table 8.1. These tests include:

Test Nos.1,2,3, and 4 which are ~ 1-inch and 2-inch pipe size, primary system cold '

leg breaks. These breaks are to be located in the bottom of the cold leg that contains the balance line to the normally instrumented CMT.

Test Nos. 5 and 6 are breaks in the direct vessel injection line of 2-in pipe size and a double-ended quillotine break of the DVI nozzle. The 2-inch break is to be located in the bottom of the DVI line and both breaks are to be in the DVI line connected to the normally instrumented CMT.

Test Nos. 7 and 8 are a 2-inch pipe size break and a double-ended break of the CL to CMT balance line. These breaks are to be located in the balance line to the normally instrumented CMT.

Test Nos. 9,10, and 11 are simulated steam generator tube ruptures (SGTR's).

Test 9 and 10 are to simulate a single ruptured tube, one with operator action and active systems and one with just the passive systems, and automatic actuations for accident mitigation with no operator actions. Test No.11 will simulate 3 ruptured tubes with only passive system and automatic actuations with no operator actions.

The actual break size areas to be modeled for each of the above test are specified in Table 8.2.

Tests 1 through 11 are to be initiated from conditions simulating AP600 full power operation.

Initial conditions for Test 12, the large steamline break, are to simulate plant startup conditions,0% power, no decay heat, with RCP's initially operating.

The SPES-2 initial conditions, actuation setpoints, and heated rod power shall be selected to provide a realistic simulation of the expected AP600 plant performance for the transients tested. Note that SPES-2 specific pre-test analyses of the above transients are to be performed to verify the plant initial conditions and to confirm the setpoints for actuations of I

both the passive safety system components and active components.

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Table 6.1 Test matrix.

TEST TEST TEST DESCRIPTION ( APG00 STATUS NON-SAFE'IY N O.

TYPE TRANSIENT SIMULATED)

SYSTEMS SINGLE FAILURE COMMENT 1

SBLOCA inch CL break (Note 2) of loop B CVCS, NRilR, and SFW oft 1 of 2 4th stage valves CMT hestup with PRilR operating (Note 11 2

SBLOCA

~1-inch CL break of loop B CVCS, NRilR Off; SFW On 1 of 2 4th stage valves CMT lleatup without PRIIR (Note 4) operating 3

SBLOCA 2-inch CL break, bottom of Loop B CVCS, NRilR. and SFW Off I of 2 4th stage valves Referena CL break 4

SBLOCA 2-inch CL break, bottom ofIeop B CVCS, NRIIR, and SFW On No effect Non safety / passive system (Note 4) interactions 5

SBLOCA 2-inch DVI break, bottom of DVI pipe CVCS, NRilR and SFW Off 1 of 2 4th stage valves Asymmetric CMT performance 6

SBLOCA DEC break of DVI CVCS, NRilR and SFW Off I of 2 4th stage valves Complete loss of one-of-two PXS subsysteme N

7 SBLOCA 2-inch break of a C14CMT balance line CVCS, NRilR and SFW Off I of 2 4th stage valves Examine effect on CMT drain down 8

SBLOCA DEG break of a C1/CMT balance line CVCS, NRIIR, and SFW Off I of 2 4th stage valves No delivery from faulted CMT between valve and CMT 9

SGTR Design basis SGTR (1 tube)

CVCS, SFWS On; Operator No effect Recovery with proper operator action to isolate SG, subcool, action; show recovery, margin depreneurire 10 SGTR Design basis SGTR (1 tube)

No CVCS. SFWS On until isol.

No effect Recovery with no operator action by ill SG level, no operator actaon 11 SGTR Beyond design basis SGTR (3 tubes)

No CVCS, SFW On until til SG No effect Examine performance beyond design level, no operation action unless basis isol. on 12 SLB Large SL break CVCS OIT: Note 4 PRIIR llX On Notes:

11 Loop B is the CMT side of plant, Loop A is PZR side of plant.

21 Break sizes are "a broken pipe of the indicated diameter *, e g.,2 in. break is 3.146 in.8

3) CMT irdection and PRllR heat exchanger operation are actuated by Protection System signals 41 SG main feedwater isolated on S signal and SFW initiated SFW on untal isolated by Protection System signale Wi344 Iin4W3

TABLE 8.2 AP600 SIMULATED TRANSIENT TESTS AP600 Break to AP600 Test be Simulated Pipe Area SPES-2 Break Area SPES-2 Break Diameter f

No.

1,2

~ l in. pipe

-0.7854 in.2 Aib&

3,4,5,7 2 in. pipe 3.1416 in.2 6,8 DEG of 8-in.

36.46 in.2 Sch.160 pipe (each end) 9,10 Single SGTR

.2894 in.2 (each end) 11 3 SG tubes ruptured

.8681 in.2 (each end) 12 Main steamline break 1.388 ft.2

~

1 NOTE: 1) The actual SPES area will be based on pre-test analysis results.

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AP-600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION 9.0 Test Reports and Data Requirements The test data is to be documented by means of two types of reports; a day of test report, and a final test report.

A.

Day of Test Report All data collected from each test are to be transmitted to Westinghouse as soon as l

practical following completion of a test run as a Day of Test Report. This report shall include a brief summary of key information to judge the validity of the test.

]

B.

Post-Test Facility Report Within one week of the Day of Test Report, a more complete test report shall be provided to Westinghouse. This report shall include:

A copy of the signed-off test procedure used in performing the test.

A copy of the key instrument outputs to confirm the validity of the test.

i Deviations and comments / observations pertinent to the performance of the e

test.

Westinghouse AP600 Test Engineering shall utilize the information in the Day of Test Report and Post-test Facility Report to assure the validity of the test and to provide the test data to appropriate organizations for analysis on a timely basis.

C.

Final Test Report Upon completion of testing, the test performer shall prepare and submit a final test report to the test sponsor.

The Final Test Report will serve to summarize, compile, and formally complete the experimental activities of the program. The required format of this report will be specified at a later date.

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i AP-600, SPES-2 INTEGRAL SYSTEM TEST SPECIFICATION 10.0 Quality Assurance Requirements Testing quality assurance shall conform to ASME NQA-1-1989 edition trough NQA-lb- -

1991 Addenda. As this is a safety related test, the Code of Federal Regulations title 10 Part 21 (10CFR21) also applies. To incorporate the requirements of NQA-1, the following measures shall be taken in the detailed test procedure:

1.

Provisions for ensuring that those performing the tests are qualified and trained in the quality assurance requirements of the test specification.

2.

Provisions for ensuring that changes to the test procedure are reviewed and approved to the same extent as the originals.

3.

Provisions for ensuring that the latest approved revision of the test procedure is used.

4.

Provision for calibration of test equipment, traceable to recognized national standards. If no such standard exists, a description of the calibration method shall be included.

5.

Provisions for verification and configuration control of computer software (if any) used to collect or reduce data.

6.

Provision for reporting and reconciling deviations from the approved test procedure.

7.

Provisions (such as a signed checklist) for ensuring that test prerequisites are met.

Test prerequisites include calibrated instrumentation, appropriate equipment, trained personnel, condition of test equipment and item (s) to be tested, suitable environmental conditions, and provisions for data acquisition.

8.

Provisions for ensuring that necessary monitoring is performed and that test conditions are maintained. (A test long containing periodic signed entries that include any pertinent observations or information not captured elsewhere is recommended.)

9.

Documented evaluation of test results by the test sponsor to ensure that test requirements were met.

10.

Identification in the test records of items tested, date of the test, instrumentation and data recorders, type of observation, results and acceptability, action taken in connection with noted deviations, and person who evaluates the test results, man 48

11.

The testing organization shall verify and document that the instrumentation I

calibrations have been performed prior to testing. This documentation must be submitted to Westinghouse.

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- Westinghouse Non-Proprietary Class 3 O

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ML20070P756

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