ML20082B404

Rev 0 to Nonproprietary Facility Description Rept AP600 ADS Phase B1 Tests

ML20082B404
Person / Time
Site:	05200003
Issue date:	03/31/1995
From:	Brockie A, Miselis V, Nitkiewicz J WESTINGHOUSE ELECTRIC COMPANY, DIV OF CBS CORP.
To:
Shared Package
ML20046D610	List: ML20082B392 ML20082B404 NRC-95-4420, Forwards Nonproprietary & Proprietary Versions of Facility Description Rept AP600 ADS Phase B1 Tests, Performed at Vapore Facility in Casacchia,Italy.Proprietary Version of Rept Withheld
References
WCAP-14304, WCAP-14304-R, WCAP-14304-R00, NUDOCS 9504050139
Download: ML20082B404 (60)

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CurrtNanotmE NON-PRomMTARY CLARE 3

- WCAP-14304 4e i

FACILITY DESCRIPTION REPORT 1

AP600 AUTOMATIC DEPRESSURIZATION SYSTEM PHASE B1 TESTS Revision 0 March 1995 V. V. Miselis A. J. Brockie J. S. Nitkiewicz a

w WESTINGHOUSE ELECTRIC CORPORATION Energy Systems Business Unit P.O. Box 355 Pittsburgh, Pennsylvania 15230-0355 i

C1995 Westinghouse Electric Corporation All Rights Reserved u A1766wcon.wpf:Ib 031795

TABLE OF CONTENTS

jggjig, Title h

1.0 INTRODUCT10N 1-1 2.0 ADS PHASE B1 TSST DESCRIIq10N 2-1 2.1 Test Method 2-1 2.2 Test Facility Requirements 2-2 I'

3.0 TEST FACILITY DESCRIIq10N 3-1 l-3.1 Principal Components 3-1 3.2 Steam / Water Supply Tank 3-1 3.3 Piping 3-1 3.4 Saturated Water Flow Control Valves 3-3 t

3.5

. ADS Valve Package 3-3 3.6 Sparger and Quench Task 34 3.7 lastrumentation 34 3.8 Data Acquisition System 3-8 3.9 Control and Safety Systems 3-9

4.0 REFERENCES

4-1 APPENDIX A - VAPORE FACILITY AS-BUILT DRAWINGS A-1

-=.

a:\\l766w.wyd:1W1295 Q

1.0 INTRODUCTION

The AP600 safety systems are predominantly passive and rely upon the natural forces of gravity, natural circulation, convection, evaporation, and condensation instead of ac power supplies and motor-driven components. Within this framework, the AP600 employs an automatic depressurization system (ADS). The ADS ensures that the reactor coolant system (RCS) is depressurized so that long-term gravity injection is initiated and maintained for passive reflood and core cooling. During emergency conditions, the ADS valves discharge steam and saturated water from the pressurizer into the in-containment refueling water storage tank (IRWST) through spargers located underwater. Two separate ADS flow paths extend from the pressurizer to the IRWST in the AP600 plant. Each ADS flow path has three stages,1,2, and 3; the flow paths open sequentially to provide a controlled depressurization of the reactor coolant system.

Previously, the AP600 ADS Phase A tests generated data to evaluate the hydraulic behavior of the sparger under various steam flow rates. Pressure pulses from the discharge of steam into the quench tank, simulating the IRWST, were measured. 'Ihe results were used for defining the dynamic forcing functions generated by steam condensation and for developing and verifying analytical models that will determine dynamic loads expected to be imposed on the AP600 IRWST during sparger operation.

The Phase B ADS tests were full-sized simulations of one of the two AP600 ADS flow paths from the pressurizer a-:4d included: a portion of the piping upstream of the ADS valves, the ADS valve / piping package, and piping through the sparger. The Phase B tests and the Phase A tests were performed at ENEA's VAPORE test facility in Casaccia. Italy; the AP600 ADS test program is part of a joint technical agreement between Westinghouse, ENEA, and SOPREN/Ansaldo.

The Phase B test program was performed in two parts, Bl and B2:

Phase B1 "Ihe overall system performance was tested with the ADS valves (or simulated valves) fully open. For these tests, flow was initiated by valves located upstream of the simulated APJ00 ADS piping and valve package.

Phase B2 "Ihis portion of the test program is currently being performed. 'Ihe B2 Phase is designed to demonstrate ADS valve operability as part of a test program outside of Design Certification.

This report gives a description of the facility used in the ADS Phase B1 testing program. (A facility description for Phase B2 testing will be presented later in an addendum to this report.) The report provides details of the test facility components, including layout, dimensions, materials, hydraulic characteristics, instrumentation, and data acquisition equipment. information regarding Phase B1 test operation is provided in the test specification, Reference 1.

u u w.wpmb-ono95 1-1

2.0 ADS PHASE B1 TEST DESCRIPTION 2.1 Test Method The ADS Phase B1 tests were system performance tests on a full sized replica o'. Jnc Of the IWo AP600 ADS pressurizer to IRWST flow paths. The tests were conducted with the ADS valves fully open and involved blowdown of either pressurized sened water or pressurized saturated steam from a steam / water supply tank through the ADS valve / piping package to a sparger in a quench tank at atmospheric pressure.

Blowdowns with saturated water from the supply tank were performed using a discharge line from the bottom of the supply tank. The blowdown flow rate and the fluid quality (two-phase steam / water) at the valve / piping package were controlled by presetting the throttle valve in the line to a partially open position and adjusting the supply tank initial pressure and temperature. The supply tank initial conditions and throttle valve positions were selected to otdn Sow conditions at the inlet of the ADS piping / valve package that simulated expected AP600 plant conditions.

Blowdowns with steam from the supply tank were performed using a discharge line from the top of the supply tank. Discharged steam flowed through a separator to ensure the removal of any water carried over from the top of the supply tank during the blowdown. In this way, only high-quality steam was supplied to the ADS piping / valve package in these tests.

1 Each ADS stage in the AP600 plant has two valves in series. In the Phase B1 ADS tests, however, only one of two valves was installed in each stage of the simulated ADS piping valve package. The missing valve in each stage was simulated by an orifice in some tests (series 100 and 200 tests), or by a full piping bore spacer in the 300-series tests. The orifices were sized to simulate the resistance and flow area of a fully open ADS valve.

In summary, the configuration was:

ADS stage 1 4-in. gate valve with 8.0 in.2 flow area simulated by orifice, or

=

4-in. full bore (minimum resistance) gate valve simulated by spacer 4-in. globe valve installed ADS stages 2 & 3 8-in. gate valve installed

=

8-in. globe valve with 20.9 in.2 effective area simulated by orifice, or 8-in. full bore (minimum resistance) gate valve simulated by spacer.

' Die overall objectives and requirements of the Phase B1 testing program are defined in the test specification, Reference 1. Testing was conducted in accordance with applicable requirements of

.:u m.pt:iw3:es 21

ANSI /ASME NQA 1,1986 as defined in Section 10. " Quality Assurance Requirements," of i

Reference 1, and the ENEA QA Plan for the tests Reference 2.

i

~

2.2 Test Facility Requirements t

For the Phase B1 tests, the capabilities required of the VAPORE test facility were:

i To provide an isolable source of saturated water at pressures and temperatures typical of the i

AP600 reactor conditions so as to achieve (or conservatively bound) prototypic volumetric and i

mass flowrates through the ADS. In the AP600 plant, the initia: steam flow from the

[

pressurizer will be followed by low quality steam or flashing saturated water.

To provide a quench tank that contains water, in which the sparger is mounted, to simulate the AP600 IRWST arrangement.

Piping and supports designed to ensure acceptable piping and valve thermal and dynamic strerees during ADS testing.

".o allow purging of air from the discharge piping using steam in order to minimize sparger air clearing loads if test full flow conditions are initiated over a shorter than prototypic time.

l To provide adequate space for the ADS valves, piping, and required supports and instrumentation so that the test can be constructed and operated with efficiency and safety.

{

To provide appropriate instrumentation and data acquisition system (DAS) that can sample at about 1000 samples per second in order to record pressure pulses that have dominant frequencies as high as 100 Hz.

?

To utilize the existing 16-in., Schedule 80 discharge line into the quench tank. The pipe must

=

be routed so as to be level or sloping downward to the quencii tank and must not contain any loop seals.

i To utiliz" the existing ENEA vacuum breakers in the 16-in, discharge piping to prevent water

^

from rit tg into the discharge piping when flow to the ADS sparger is terminated.

l us1 %.w g ib031695 22

3.0 TEST FACILITY DESCRIMION 3.1 Principal Components Most of the major Phase B1 test facility components are the same as those used in the Phase A test program (Reference 8), including the steam / water supply tank, steam moisture separator, steam supply header, main discharge pipe, quench tank, and sparger (Figure 3-1). Other components, such as the demineralized water tank, water chemical treatment system, surge pump, electric heaters, pool heating system, water supply system, sump and drainage system, are also retained. However, Phase Bl test requirements dictated various modifications to the existing facility. "Ihe significant modifications are illustrated in Figure 3-2 and are described in Table 3-1. A schematic piping and instrumentation diagram for the facility is provided in Figure 3-3.

Full details of the components that influence the tests are provided in subsequent sections.

Engineering drawings are provided in Appendix A.

3.2 Steam / Water Supply Tank The steam / water supply tank also referred to as the accumulator or pressurizer is the source of pressurized, heated water or steam for the blowdowns conducted in the tests. It is a vertically oriented cylinder with hemispherical ends made from low alloy steel. All the internal surfaces have stainless steel cladding. The steam / water supply tank volume is 1412.6 ft.'(40 m'); including the support skirt, I

the overall height is 42.11 ft. (12.835 m). Internal electric heaters are inserted through the bottom head, and there are two main outlets: a 10-in. diameter steam outlet at the top, and a central 14-in.

I diameter water outlet from the bottom. The external surface is insulated by 5.91-in. (150-mm) thick fiberglass pads. Principal dimensions and characteristics are listed in Table 3-2. The accumulator is shown in drawing A 1 of Appendix A.

3.3 Piping Steam Supply Line A steam line runs from the supply tank's top outlet, via an isolation valve (VI-1.1) and a control valve (VR 1.1), to the steam moisture separator. Valve VI 1,1 is a hydraulically operated wedge gate type with a closing time of less than 0.5 seconds and an opening time of about 30 seconds. The steam line is 10-in. Schedule 160 up to the control valve and 12 in. Schedule 160 from the control valve outlet to the steam moisture separator. The line is carbon steel with a stainless steel lining, it is insulated externally with 4.72-in. (120-mm) thick fiberglass pads. Principal dimensions and j

characteristics are listed in Table 3-2. The steam line is shown in drawing A 2 of Appendix A.

u:\\l766w.mpf:Ib-031695 3-1

Steam Moisture Separator The separator is essentially a spherical tank. Inside the tank there is a " mist eliminator" that consists of packed, stainless steel lamellar sheets in a " chevron" arrangement. The separator is installed to remove moisture from the steam and is specified to achieve an exit steam quality of 95 percent. The tank's volume is 173 ft.' (4.9 m'). It is made from carbon steel, is clad internally with stainless steel, and is insulated with 150-mm (5.91 in.) thick fiberglass pads. Principal dimensions and characteristics are listed in Table 3-2.

Steam Collector At the steam outlet from the separator, there is a 12-in. ASME venturi-type flowmeter. Imma&~1y downstream of the flowmeter is a large header,25.07-ft. (7.6-m) long. The header is fabricated from 16-in., Schedule-160 and 24-in., Schedule-160 carbon steel with a stainless steel lining. On its 16-in, section are four B-in, flanged tee connections, one of which is binaked. The three open tee connectics are commoned into a 12-in., Schedule 160 carbon steel manifold that terminates with a flange located near the saturated water supply line. The steam collector assembly comprises the flowmeter, header, and manifold and is insulated with 4.72-in. (120-mm) thick fiberglas pads.

Principal dimensions and characteristics are listed in Table 3 2. 'Ihe header is shown in dmwing A and the manifold in drawings A-4 and A-5 of Appendix A.

Saturated Water Supply Line A 12-in., Schedule-160 saturated water supply line runs from the steam / water supply tank's bottom outlet, via two gate valves, to a 12-in. flanged connection near the 12 in. steam manifold flange. A 14-in. by 12 in. reducer is fined to the tank outlet. The line is stainless steel from the tank to the first gate valve and carbon steel thereafter. The line is insulated with 2.36-in. (60 mm) thick rock wool.

Principal dimensions and characteristics are listed in Table 3-2. The line is shown in drawings A-and A-5 of Appendix A. Details of the gate valves, designated VL1-1 and VLI-2, are provided in Section 3.4.

i l

ADS Valve Package Inlet Piping The ADS valve inlet piping runs from the 12 in. flanged connections on the steam manifold or saturated water line to the ADS valve / piping package. Only one connection - steam or saturated

{

water - can be made at a time: an interchangeable,90-degree elbow spool piece is provided for this purpose. The inlet piping transitions to 14-in. and incorporates a prototypic loop seal just upstream the valve / piping packagc. The loop seal's function is to ensure that the ADS valves and seats are always wetted (by condensate). This is important in the Phase B2 tests. The 12-in. and 14-in. p is Schedule-160 carbon steel. It is insulated by 2.36-in. (60-mm) thick rock wool. Principal dimensions and characteristics are listed in Table 3-2. The piping is shown in drawings A-4 and A-5 of Appendix A.

uA1766w.wpf:!b.031495 3-2

ADS Valve Package Discharge Piping De ADS valve package exhausu into a 16 in., Schedule-80 carbon steel discharge header. De header has two 10-in. flanged tee-connections, each of which is connected to a transition pipe containing a bellows section and a 90 degree elbow. The elbows connect to the tee connections on tne header of the line running to the sparger and quench tank.

The quench tank line (16-in., Schedule-80 carbon steel throughout) runs, sloping downwards, for a distance of around 100 ft. to the sparger inlet above the quench tank. Two vacuum breaker valves are fitted near the quench tank to prevent quench tank water from being drawn up when flow stops.

All of this valve package discharge piping is uninsulated. Principal dimensions and characteristics are listed in Table 3-2. "Ihe ADS valve package discharge header and bellows sections are shown in drawings A-4 and A-5 of Appendix A, and the quench tank inlet line is shown in drawing A-6 of L

Appendix A.

3.4 Saturated Water Flow Control Valves Two 12-in. gate valves, designated VL1-1 and VLI-2, are installed in the saturated supply water line for the purposes ofinitiating and controlling the saturated water blowdown flows (see Section 3.3).

The upstream valve, VLI 1, is an Edward wedge-type gate valve; VLI-2 is an Atwood and Morrill (A&M) parallel disc gate valve. "Ihe valves are fitted with fast-operating motor actuators that give l

opening and closing times of about 30 seconds. The valves are insulated to the same specification as the remainder of the saturated water supply line.

VLI 2 is pre-set to a specified flow area for each saturated water blowdown test in order to achieve desired mass flow rate and steam quality conditions. It is opened to the necessary position before flow is initiated: VL1-1 is then opened (fully) to begin the blowdown. The blowdown is terminated by closing VL12.

The specifications of these valves are summarized in Table 3-2 and are detailed in References 3 and 4.

Because VL12 is used to set test initial conditions, it has been subject to special testing and analys to determine its flow characteristics (Reference 5). These characteristics are shown in Figures 3-4 (flow area versus valve opening) and 3-5 (friction factor K versus valve opening). (K is defined as:

unt hw.wpt:lt>031295 3-3

I K = 17.2 d' AP q 1.

where:

d

=

connecting pipe internal diameter On.)

AP

=

pressure drop across valve (psi)'

mass flow rate through valves Obm/sec)

Q

=

b l

Valve opening was measured by the distance from the valve body to the anti-rotation bar on the stem, i

and was recorded for each test.

l 3.5 ADS Valve Package lhe ADS valve / piping package comprises a prototypic matrix or cluster of three parallel flow paths-stages 1,2, and 3-between the inlet and discharge piping described in Section 3.3.

Stage 1 is 4 in. throughout, with a spool piece (to allow later installation of a gate valve) and an Anchor Darling globe valve (VAD-1) downstream. There is a provision for fitting an orifice at the spool piece to simulate the insistance of the missing gate valve; when it is not fitted, a full bore spacer is inserted.

Stage 2 is 8 in. throughout, with an Anchor Darling parallel disc gate valve (VAD-2) and a spool piece (with provision for fitting an oriGce to simulate the resistance of the missing 8 in. globe valve, or a full bore spacer) downstream Stage 3 is 8 in. throughout, with a Westinghouse gate valve (VAD-3) and a spool piece (with provision for fitting an orifice to simulate the resistance of the missing 8-in. globe. valve, or a full bore spacer) downstream.

i The stages are connected to the inlet and discharge piping with reducers and tees. The piping is carbon steel (Schedule 160 on the inlet side and Schedule 80 on the discharge side), while the valve bodies are stainless steel. The valve package is uninsulated.

Principal dimensions and characteristics of the valve package including valve and orifice specifications are given in Table 3 2. Detailed valve specifications may be accessed in References 6 and 7. The valve package is shown in drawings A-4 and A 5 of Appendix A. The orifices are shown in Figures 3-6 and 3-7.

u A1766w.wpf:Ib431495 34

J 3.6 Sparser and Quench Tank The function of the sparger and quench tank is to condense the steam exhausting from the test facility.

l

~

]" Except for the inlet pipe size (14-in. Schedule 80), its design is prototypic of the AP600 plant sparger.

'Ihe quench tank is a large, concrete cylindrical water tank, built below ground level. The tank has a steel cover that prevents excessive water vapor loss when the quench tank water is hot. 'Ihe cover has

" doors." which are opened during blowdowns to allow the vapor generated by cy=Mng to vent. A water heating system allows tests to be conducted with the tank water at saturated conditions (212*F).

'Ihe tank's internal diameter is 23.3 ft., giving a water volume of 9460 ft.' when filled to its normal depth of 22.2 ft.

The sparger and quench tank are shown in drawings A-7, A-8, and A-9 of Appendix A.

3.7 instrumentation

'Ihe test facility instrumentation for Phase B1 was developed in collaboration between ENEA, Anantda and Westinghouse. Phase B1 instrumentation was based on the previous Phase A ADS test program with extensive additions and changes.

'The following is a descripdon ofinstrumentation locations for the Phase B1 tests. A list of all instrumentation is given in Table 3-3. Figures 3-3,3-8,3-9, 3-10, and 3-11 schematically illustrate the location of the piping, quench tank, and sparger insuumentation.

3.7.1 Temperature Instrumentation The temperature of the steam and/or water throughout the ADS test facility is measured by

^

thermocouples, in general, the thermocouples are located in pipe tappings and are positioned so that they protrude into the flow stream by about 0.5 in. 'Ihe measurements include:

'Ihe temperature in the quench tank line upstream and downstream of the 90-degree elbow above the sparger (TE-01 & 'IE-02)

'Ihe :;icam/ water temperature in the vertical pipe runs in the quench tank just upstream of the sparger (TE-03) and one location in the sparger body (TE 06)

.:um...pt:iw3:495 35

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The steam / water temperature at six locations in sparger arm A (TE 7 to TE 12) and at two locations in the hottom of each of the sparger arms B C, and D (TE-13 to TE-18)

. De quench tank water temperature at four elevations on racks A, B, and C, in twelve locations throughout the tank (TE 19 to 1E 30) 4 The temperature in the 12 in. saturated water supply line from the pressurizer, upstream of valve VLI l (TE-1W)

Temperature upstream and downstream of valve VLi-1 (TE-2W & TE 3W)

Temperature upstream and downstream of VLi-2 (TE-4W & TE-5W)

Temperature in 14-in. ADS valve package inlet piping (TE 6W)

Temperature upstream and downstream of stage I spool piece (TE-7W & TE-8W)

Temperature downstream of VAD-1 (TE-9W)

Temperature upstream and downstream of VAD-2 (TE 10W & 1E-IlW)

Temperature downstream of stage 2 spool piece (TE-12W)

Temperature upstream and downstream of VAD-3 (1E 13W & TE-14W) l Temperature downstream of stage 3 spool piece (TE-15W)

Temperature in ADS valve package discharge header (TE 16W) 3.7.2 Steam / Water Supply Tank inventory Instrumentation The steam / water supply tank water level (LT-01)is used to establish proper tank inventory during tank heatup prior to test initiation. During tests, the mass inventory is also measured using LT-1B; the change in mass inventory is used to determine the mass flow rate in the saturated water blowdown tests.

3.7.3 flow Instrumentation A venturi type flow meter (FT-ISB) is used for measuring the steam flow rate downstream of the j

moisture separator. The venturi delta-P and associated compensating temperature and pressure signa are monitored.'

ual766w.wpf:lt431695 3-6

3.7.4 Pressure Instrumentation 1he pressure in the steam / water supply tank, the steam and saturated water supply lines, ADS valve package, sparger, and within the quench tank are measured. The locations for these pressure j

measurements are specified below:

Steam / water supply tank initial pressure and pressure versus time during the blowdown (M-04)

The steam pressure just downstream of the moisture separator (at the steam venturi) and in the steam collector header (M-61 A & N-10)

The steam pressure in the header of the 16-in. quench tank line (M-61B)

Pressure measurements at approximately one-half of the length of the quench tank line, and pressure measurements in the quench tank line just upstream of the 90 degree pipe bend above the water surface of the quench tank (M-18 & PE-21)

A vacuum gage is installed in the quench tank line just outside the quench tank near PE-21 (PE 22) i Pressure measurement at the 90-degree elbow above the sparger (PE-1)

The steam / water pressure in the sparger body (PE-2)

Pressure at three positions inside sparger arm A (PE-3 to PE-5) and a single pressure measurement in each of the three remaining sparger arms B, C, and D (PE-6 to PE-8)

Twelve pressure incasurements are made within the quench tank. These pressure measurements are made at two radial positions, one extending from sparger arm A and one rsdial position between two adjacent arms A and B. Each radia' position consists of one pressure measurement at the bottom of the tank at the sparger arm radius, ~three pressure measurements spaced between the sparger arm radius and the tank wall at the arm elevation, and two pressure measurements at the tank wall spaced at higher elevations. (PE 9 to PE-20)

The pressure in the 12-in. water discharge from the steam / water supply tank, upstream of valve VLI l (M-lW)

Pressure upstream and downstream of valve VLI-l (PE-2W & PE 3W)

Pressure upstream and downstream of VLI 2 (PT-4W & PE-5W)

Pressure in 14 in. water supply piping for ADS loop (PT-6W) uAIMw.wyf:lt431295 3-7

R

. Pressure upstream and downstream of stage I spool piece (PE-7W & PE 8W)

Pressure downstream of VAD-1 (PE-9W)

Pressure upstream and downstream of VAD 2 (PT-10W & PE-IlW)

Pressure downstream of stage 2 spool piece (PE-12W) i Pressure upstream and downstream of VAD-3 (PE-13W & PE-14W)

Pressure downstream of stage 3 spool piece (PE-15W) l Pressure in ADS loop discharge header (PE-16W)

• Pressure in valve body and bonnet for VLI-l (PE-17W & PE-18W)

Pressure in valve body and bonnet for VLI-2 (PE-19W & PE-20W)

Pressure in valve body and bonnet for VAD 2 (PE-21W & PE-22W)

Pressure in valve body and bonnet for VAD-3 (PE-23W & PE-24W) h 3.7.5 Accelerometers Three accelerometers are mounted on a 90 degree elbow above the sparger. The location of these accelerometers is shown in Figure 3-8. (YE-1 to YE-3) 3.7.6 Strain Gages Two sets of axial and horizontal (circumferential) strain gages were placed C0 degrees apar sparger pedestal (XE-1 to XE-4)

Four axial strain gages are mounted at 90-degree intervals on sparger arms A and B, as close to the sparger body as possible (XE-6 to XE 12) 4 Four axial strain gages are mounted on the ADS loop piping at the 90-degree elbow, downstream of VAD 2 (XE-13 to XE 16)

Four axial strain gages are mounted on the ADS loop piping at the 90-degree elbow, downstream of VAD-3 (XE-17 to XE-20) s:\\lMw.w@lt431295 3-8

One axial strain gage is mounted to two of the support columns (one on each column) for the ADS loop piping structural platform to measure the strain on the support columns (XE 21 to XE 22)

Eight axial strain gages are mounted on the ADS loop piping at the tee downstream of Stage 3 spool piece at the ADS discharge header (XE-29 to XE 36) 3.7.7 Piping Position Two LVDTs are mounted near the water discharge nozzle under the pressurizer to measure the axial and venical motion during the transient (ZT 6 to ZT-7). These instruments are used for facility protection only, 3.7.8 Valve Parameters 1

Each of the saturated water flow control valves VLI 1 and VL12 is equipped with a set of sensors that is part of the MOVA~I3 valve monitoring system. The sensors measure:

actuator motor current and power e

valve stem torque and thrust e

valve stem position "open" and " closed" limit switch state spring pack displacement e

3.8 Data Acquisition System For the Phase B1 tests, three separate data acquisition systems (DAS) were used: one for the' quench l

tank temperatures, one for the valve data, and one for the remaining pressurizer, piping, and quench tank data. Figure 3-12 shows a schematic of the DASs. The three systems are referred to as the IBM system, the MOVATS system, and the Prosig system respectively. All three systems are PC based digital DASs. A trigger signal from the main control room was used to start these three systems simultaneously,just seconds prior to the stan of the transient.

1 i

Descriptions of the three DASs used are as follows:

A schematic of the flow diagram for the IBM system used to record the quench tank temperatures during tests is shown in Figure 3-13. This schematic shows the DAS and signal conditioners (Euromisure INOR Model SE5000) used to condition the thermocouple data prior to recording.

this DAS consists of a 30-channel,12 bit analog to-digital converter and an IBM XT PC. This system records the data from the thermocouples in the quench tank at a rate of 4 samples per second (sps),

ual?66w.wyd:ltWD1695 39

~l A schematic of the flow diagram for the MOVATS system used to record the characteristics of the valve performance is shown in Figure 3-14. The DAS is a standard 12 channel,3500-series signal conditioning unit and Dolch 486/33MHz PC supplied by ITI MOVATS. This system recorded valve torque / thrust, position, coil current, limit switch state (open/close), motor power and current, and upstream / downstream pressures. These data are recorded at a rate of 1000 sps.

A schematic of the flow diagram for the Prosig symem used to record data from the pressurizer, downstream piping, sparger, and quench tank is shown in Figure 315. Some of these signals are conditioned prior to the Prosig DAS. The DAS consists of a 136-channel, high-speed digital DAS manufactured by Prosig. This system consists of signal conditioners, filters, amplifiers, and 14-bit analog-to-digital converters housed in several units. A Viglen 486/33ME PC is used to record the data from the Prosig DAS units. The data are recorded at a rate of 1000 sps.

Prior to start of the Phase B1 tests, these systems were setup and a functional / validation checkout was performed. The data acq"Htion hardware was found to be accurate within 24%.

3.9 Control ar.d Safety Systems A programmable logic control system running on a Hewlett Packard PC is used for plant control. The system is used to control the supply tank pressure / temperature (by switching the heaters on and off) prior to test initiation and to control the operation of valves and DAS during the tests. The control sequence for the saturated water blowdown tests is shown in Figure 316.

The supply tank level is monitored and manually controlled so that the levelis typically 5 60 percent prior to steam blowdowns and s 80 percent prior to saturated water blowdowns.

During blowdown, heater operation and feedwater addition to the supply tank are terminated.

The test facility safety system consists of two spring-loaded safety valves mounted on top of the supp'y tank. "Ihese valves are set to open at a pressure of 2785 psig (1.2 barg).

If pressure reaches 2683 psig (185 barg), power to the heater rods is electronically cut off. When the supply tank level reaches less than 9.2 ft. (2.8 m), differential pressure cells cut off power input to the heater rods. Override functions provide two alarms. One alerts the operator when pressure reaches 2741 psig (189 barg), and the other alens the operator when level reaches 7.2 ft. (2.2 m).

f

.:uww. g:iunis95 3 10

TABLE 31 PRINCIPAL MODIFICATIONS TO VAPORE FACILTIY FOR ADS PHASE B1 Modification Purpene Addiuon of a 12 in,ime, with two isolanon valves, Supply the ADS valve package with sanrned water from the bonom of the supply tank to the ADS up to 2300 psig. Expected saturated water flowrate a

valve / piping package up to about 500 kg/s (1100 lb/s).

Addition of a new steam collector downstream of To ensure the proper steam feed to the ADS valve moisture separator package Addition of the prototype ADS pipmg and valves Simulanon of stage 1,2, and 3 valve arrangement Addiuon of new skscharge collector at ADS loop To connect the exisung discharge line and the ADS outlet loop Installabon of high pressure bellows and structural To ensure integrity dunng test conditions verification of the existing discharge line Addition of a quencher stand to elevate the sparger To *ahance test nimislarian of the actual plant to 14.5 ft. above the bouom of the quench tank component arrangement Addition of an interchangeable spool piece to To avoid mechanical stress since due to thermal provide the ADS loop with saturated water or expansion since only one of the two feed lines will saturated steam be utilized at a time Addiuon of new instrumentanon (about 50 new To ensure complete monitonng of the ADS Phase instruments) and data acquisition systems Bl test Addition of new programmable logic control system To allow control of additional equipment u:\\l7e6=.wpf:lh031295 3.}]

TABLE 3 2 PRINCIPAL DIMENSIONS AND CHARACTERL% TICS OF TEST FACILTTY COMPONENTS Staam/ Water Supply Tank Volume 1412.6 ft.8 (40 m')

Design Pressure 2860 psig (197 berg)*

i Design Temperanse 6897 065'C)

Material Wall Low alloy steel laternal Claddag Austenitic stamiess steel laternal Diameser (nmmal) g3.74 in. (2.127m)

Wall Thickness: Top Dome (min) 1.90 in. (48.3 mm)

Cylinder (min) 3.g2 in. (97 mm)

Bonom Dome (min) 2.74 in. (69.6 nun) i Cladding Thickness (mm) 0.13 in. O.2 nun)

Overall Height (including skirt) 42.11 ft. (12.835 m)

Outlets: Steam (top) 10-in. nommal bore Water (bonom) 14-in. nommal bore losulanon:

Type Fiberglass pads (glass wool encased in zinc mesh for physical stability) of density 90-100 kg/m'/ aluminum sheet cover Thickness 5.9) in. (150 mm)

Steam Line Design Pressure 2860 psig (197 berg)

Design Temperature 6897 (365*C)

Material Wall Carbon steel I.ining Austenitic stainless steel Bore: Up to Connel Valve VR I.1 10-in. Schedul 160 After Control Valve VR.I.1 12-in. Schedule 160 Lining Thickness (nonunal) 0.12 in. (3 mm)

~

Insulation:

Type Fiberglass pads (density 90-100 kg/m')/alummum sheet cover Thickness 4.72 in. (120 mm) 9 wu?66=.wpcim:295 3 12 i

TABLE 3 2 (Cont.)

PRINCIPAL DIMENSIONS AND CHARACTERISTICS OF TEST FACILITY COMPONENTS Separator Volume 173 ft ' (4.9 m')

i Design Pressure 2860 psig (197 barg)

Design Temperature 689'F (365'C)

Material: Wall Ca6on steel Internal Claddmg Austenitic stamiess steel Internal Diameter 6.9 ft. (2.1 m)

Wall Thickness (minimum) 3.4 in. (86 mm) 1 Cladding Thickness (nommaD 0.12 in. (3 mm)

Insulation: Type Fiberglass pads (density 90-100 kg/m')/ aluminum sheet cover Thickness 5.91 in. (150 mm)

Steam Collector Design Pressure 2860 psig (197 barg)

Design Temperature 689'F (365'C)

Ventun Flowmeter.

Throat Diameter 7.72 in. (196 2 mm)

S Ratio 0.753 Header:

Wall Material Carbon steel Lming Material Austenitic stainless steel Bore 16 in. Schedule 160 & 24-in. Schedule 160 Linmg Thickness (nominal) 0.12 in. (3 mm)

Manifold: Material Carbon steel Bore 8 in. Schedule 160 (branches) & 12-in. Schedule 160 (common pipe)

Insulauon: Type Fiberglass pads (density 90-100 kg/m')/ aluminum sheet cover Rickness 4.72 in. (120 mm)

Saturated Water Line Matenal:

Up to Gate Valve VL1-1 Austenitic stainless steel After Gate Valve VLl-1 Carbon steel Bore 12 in. Schedule 160 Insulauon: Type Rock wool / aluminum sheet cover Thickness 2.36 in. (60 mm) u:\\l766w.wid:lW)31605 3 13

TABLE 3 2 (Coet.)

I PRINCIPAL DIMENSIONS AND CHARACTERISTICS OF TEST FACILITY COMPONENTS ADS Valve Package laiet Mptag Matenal Carbon steel Bore:

Upstream of 1. mop Seal 12 in. Schedule 160 Loop Seal and Upstream 14-in. Scheasle 160 of Valve Clumer Insulation: Type Rock wool / aluminum sheet cover Thekne<<

2.36 in. (60-mm)

ADS Valve Package Discharge Mping Material Carbon steel Bore:

Valve Package Discharge 16-in. Schedule 80 Header Two Transition / Bellows 10-in. Schedule 80 Secuans Quench Tank Line 16-in Schedule 80 Insulauon None Valve VL11 Size / Type 12-in. wedge type gate valve Manufacturer Edward Model Figure B120ll (WCC) DDUWY (Class 1500)

Matenal:

Base A216 Grade WCC Trim A216 Grade WCC Actuator Liarhorque SMB-3 Stem Travel Full Closed-Full Open 10.2 in.

Opetung Time (to full open) 30 seconds max.

Full Open Flow Area 67.2 in.2 (manufacturer's data)

Full Open C, 6850 (manufacturer's data)

Valve VL1-2 Size / Type 12 in. parallel disc gate valve Manufacturer Atwood & Morrill Model 12-in. class 1500 Dwg. #166S4-0 u Alhw.wp:Ib-031295 3-14

TABLE 3 2 (Cont.)

PRINCIPAL DIMENSIONS AND CHARACTERISTICS OF TEST FACILTTY COMPONENTS Material Base A 216 grade WCB Trun Stataless steel 4

Actuator Liminorque SMB 3 Stem Travel Full Closed - Full Open 9.5in.

]

Closing Tune (from full open) 30 seconds max.

Full Open Flow Area 58.5 in.2 (manufacamer's data)

Full Open C, 7150 (manufacamer's data)

ADS Valve Piping Package Stage 1 Pipe Bore 4-in. Sduulule 160 (inlet side) 4-in. Schedule 80 (outlet side)

Pipe Masenal Carbon steel Orifice (for simulation of gate valve)

Inside Diameter 3.189 in.

Profile Parallel bore, square-edged, with two 0.118-in. radius notches to i

drain condentaar Thickness 0.453 in.

$ Ratio 0.927 Valve VAD-1:

Type Globe Manufacturer Anchor Dartmg Model 4-in.1707# linear plug Material Stamiess steel (body)

Actuator Limitorque SB-125 Full Open Flow 8.78 in.2 (manufacturer's data)

Area 140 (manufacsurer's data)

Full Open C, Stage 2 Pipe Bore 8-in. Schedula 160 (inlet side) 8 in. Schedule 80 (outlet side)

Pipe Material Carbon steel Valve VAD-2:

Type Parallel disc gate valve Manufacturer Anchor Darhng Model 8-in.-1707#

Material Staines steel (body)

Actuator Limitorque SB 2-80 Full Open Flow 30.68 in.2 (manufacturer's data)

Area 3275 (approx.)(manufacturer's data)

Full Open C, u:\\lhw.wpf:lkO31295 3-l$

__= - _ - _ _

TABLE 3 2 (Cont.)

PRINCIPAL DIMENSIONS AND CHARAC'IERISTICS OF TEST FACILITY COMPONENTS Orifice (for simulation of globe valve) loside Diameter 5.161 in.

Prorde Parallel bore, square-edged, with two drain holes at pipe wall posidan Thickness 0.379 in.

$ Ratio 0.756 Stage 3 Pipe Bore 8-in. Schedule 160 (inlet side) 8-in. Schedule 80 (outlet side)

Pipe Manenal Carbon steel Valve VAD-2:

Type Wedge-type gate valve Manufacturer Westingbouse Model 8-in.-Class 1725 dws. #6437E31 Masenal Samnican steel Actuator Limitorque SB 3 Full Open Flow Area 28.8 in.* (manufacturer's data)

Full Open C.

N/A Orifice (for simulation of globe valve)

Inside Diameter 5.161 in.

Profile Parallel bore, square-edged, with two drain holes at pipe wall position Thickness 0.630 m.

$ Ratio 0.756 Note:

(1) Barg refers to bar gage. I barg = 10' pascals.

1 u:\\l%w.wpf:Ib-031295 3-16

-. ~

TABLE 3 3 LIST OF INSTRUMENTS Type of Specified Transducer I.D.

Transducer Make/Madel Range Accuracy Quench Tank I

TE 01 to TE 30 Thermocouple Euromisure K01 32 - 572*F 14'F l

(Type K)

(0 - 300'C) 2 (1 2*C)

XE-1 to XE-12 Strain Gage Eaton Ailtech N/A N/A (120 ohms)

SG-125-01 Piping Pressure j

PE2W PE8W, Pressure Transinstruments 0 - 3625 psig 10.2% of full PEllW, PE13W -

(Paezoresisuve)

BHL-4251 (0 250 barg) scale PE15W, &

PEl7W - PE24W PE9W, PE12W. &

Pressure Transinsuuments 0 - 2320 psig 0.2% of full PE16W (Piezoresisdve)

BHL-4251 (0 - 160 barg) scale DNP-01 Delta-P VLI-2 N/A N/A N/A ADS Loop Piping Strains XE 13 to XE-36 Strain Gage KYOWA N/A N/A (120 ohms)

SKW-10057 Quench Tank Pressures PE-01 Pressure Transinstruments 0 - 870 psig 0.2% of full (Piezoresisuve)

BHL 4225 (0 60 barg) scale 40MO PE-02 Pressure Transinstruments 0 - 362.5 psig

+0.2% of full (Piezoresisuve)

BHL 4225 (0 25 barg) scale 40MO PE-03 to PE-07 Pressure Transinstruments 0 232 psig

' O.2% of full (Piezoresisuve)

BHL 4225 (0 - 16 barg) scale 40MO PE-08 Pressure Transinstruments 0 - 232 psig 1 2% of full I

0 (Psezoresisuve)

PROMAN (0 - 16 barg) scale C252230/2a PE-09 to PE-20 Pressure Transinstruments 0 - 36 psig 0

1 2% of full (Piezoresisuve)

BHL-4240 (0 - 2.5 barg) scale 40MO Discharge Piping Before Sparger PE-21 Pressure Transinstruments 0 - 870 psig 1 2% of full 0

(Piezoresisdve)

BHL-4225 (0-60 barg) scale PE-22 Pressure Hartmann-B 0 - 36 psia 2 2% of full 0

(Piezoresisuve)

ARK 210 (0 - 2.5 bar scale absolute) vai m.w g ib.031695 3-17

TABLE 3 3 (Cont.)

LIST OF INSTRUMENTS Type of Speelnad Transducer I.D.

Transducer Make/Model Range Accuracy Discharge Piping Aher Moisture Separator frT61A Pressure Transinstruments 0 - 2320 psig 10.5% of full (Mezoresistive)

BHL 42064)0-(0 - 160 barg) scale OlMO IrT61B Pressure Transinstruments 0 - 1450 psig 0

1 5% of full (Mezoresistive)

BHL-4206 (0 - 100 barg) scale OlMO l'T 18 o aure Transinstruments 0 - 870 psig 0

1 5% of full (hezoresistive)

BHL 420600 (0 - 60 barg) scale FT 10 Pressure Transinstruments 0 - 2320 psig 10.5% of full (Piezoresistive)

BHL-4206 00 (0 - 160 barg) scale FT-15 Venturi Hydromes 0 - 507 paid N/A TH-DVA (0 - 35 bard)

Pressurizer I'T-04 Pressure Rosemount 0 - 2900 psig 10.5% of full (Mezoresistive)

Il44-G6000-A22 (0 - 200 barg) scale LT 1 Delta-P Bellows Rosemount 0 32.8 ft N/A Type 151INPE22B1 (0 - 10 mH,0)

(level)

LT1B Delta-P Bellows Rosemount 0 79380 lb N/A Type 151INPE22BI (0 - 36000 kg)

(mass)

Discharge Piping l'TlW. PT6W, &

Pressure Transinstruments 0 - 3625 psig 0.5% of full PT10W (Mezoresistive) 4600-BOC-2500 (0 - 250 barg) scale COUE j

l'T4W Pressure Transinstruments 0 - 2320 psig 0

1 5% of full (Piezoresistive)

BHL-4207-00 (0 160 barg) scale YE-01 to YE-03 Acceleration Endevco 7703A-100 g N/A j

(Mezoelectric) 100 TElW to TE16W Thermocouple Euromisure K01 32 - 572'F 4'F (Type K)

(0 - 300*C) 2 (1 2*C)

Surge Line Displacement ZT-6 to ZT-7 Displacement Monitran z 0.4 in N/A (LVDT)

MTN/EGR010 (t 10 mm)

I u Alm..wpt:1Mn695 3 18

TABLE 3-3 (Coot.)

LIST OF INSTRUMENTS Type of Specined Transducer I.D.

Transducer Make/Model Range Accuracy MOVATS Transducers N/A Torque /Tirust Cell ITI MOVATS 0 - 200000 lbs 2

1 % of reading (Strain Gage Type)

Type RF thrust 1 5% of full 0

0 6000 ft.-lbs.

scale torque N/A Current Probe Fluke Y8100 0 - 200 amps dc

_6% of full scale

+

(Clamp-On)

N/A Displacement Pulsonic 2000 0 - 10 in.

+2.5% of readmg

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3-Surge pump 11-Main control valve (10"xt2")

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'5-Steam accumulaser 13-Secondary comrol valve (3"x4")

21-Backpressure control valve 6-Electric heaters 14-Moisture separator 22-Water tank ($=M m. h=10 m) i 7-Safety /rehef valve

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4.0 REFERENCES

1. Brockie, A.J., AP600 Automatic Depressurization System Test Specification (Phase B1) Revision 2, PXS-T1 P004, WCAP-14112 (Proprietary), February 1995.

2.

Quality Assurance Plan

Description:

AP600 Test Program Conducted at the VAPORE Plant in ENEA Casaccia (Phase B), RCS-T1H 001 (ENEA Document AP600-GQ9402).

3. ADS Test Valves 12 in. Edward Valve Field Manual, PV60-VTM-001 (Proprietary).

4.

ADS Test Valves Atwood & Morrill Valve Field Manual, PV60-VTM-002 (Proprietary).

5. Peters, F. E., Automatic Depressurization System Phase B1 Final Data Report, RCS-T24-100 March 1995.

6. ADS Test Valves Anchor Darling Valve Field Manual, PV60 VTM 003 (Ptoprietary).

7. ADS Test Valves Westinghouse Valve Field Manual, PV60-VTM-004 (Ptoprietary).

8.

VAPORE Facility Descripdon Repon - AP600 Automatic Depressunzanon System Phase A Test, i

Revision 0, WCAP-14149 (Proprietary), August 1994.

\\

u:\\lhw.wpf:IbO31495 41

t t

e i

t APPENDIX A VAPORE FACILITY DRAWINGS l

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sA1766w.wyf:1b.030995 A-1

E O

TAltl.E A 1 f

I'llASE H-1 val' ORE FACil ITY DRAWINGS 1

Drawing Ref Title c-5 Organization / Drawing No.

Revision Ihte 3

A-I Accumulator - assembly ANSALDO 6

7 June 1985 8

7.083.901 A-2 Piping layout, lines FBM 3

29 May 1985 001-12 in.-G-10-C 39698 sheet 1 001-10 in.-G-10-C A-3 Test header FBM 3

' June 1985 39700 A -4 '

Composite piping - kop ADS ANSALDO O

20 May 1994 VAP0001 DMBX2260001 A-5' isome....ain lines-hop ADS ANSALDO O

20 May 1994 VAP0001 DMLX 22500001 O

A-6 Assembly of quench tank inlet line FBM 4

15 May 1986 39763 A-7 Quench tank ANSALDO I

27 January 1992 VAP0001 DMYX0413 A-8 Quench tank ANSALDO O

3 July 1991 VAP0001 DMYX0814 A-9 Sparger Vincent's Weklir.g 0

22 April 1991 074-91-1 Note:

(1) These drawings are not included in the non-proprietary version of this document.

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