ML20059B739
| ML20059B739 | |
| Person / Time | |
|---|---|
| Site: | 05200004 |
| Issue date: | 10/19/1993 |
| From: | GENERAL ELECTRIC CO. |
| To: | |
| Shared Package | |
| ML20059B690 | List: |
| References | |
| PROC-931019, NUDOCS 9310290079 | |
| Download: ML20059B739 (230) | |
Text
{{#Wiki_filter:. PCC TEST PLAN & PROCEDORES
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Doc ne j Rev Page of SIET I l scraone nearrin Innovsiivi i (t @MPPol i O 1 I m NOMENCLATURE Air Operated AO CGA Color Graphs: Adapter CPU Central Process Unit CT Condensate Drain Tank d Throat Diameter / dsameter D inside Diameter DAN Nuclear Arts Dartction DAS Data Acquisition System DL Drain Line DOS Duk Operanve System DRF Design Record File DSSI Disk Storage System Interf ace F Flowrate FCV Flow Control Valve FFT Fast Founer Transtormer FP Feed Pump FWL Feed Water Line GDCS Gravity Dnven Coobng System j h Pressure Tap Height Differerice H Height / Elevation 1 l HCV Hand Control Vahe HV Hand Valve l 1 1.0 Input / Output L Lori l l l I
i D cuanent Rev Page of SIET ; wucrie demuni Iwum rOO9HPP91 0 2 ( 225 INDEX 3 NOMENCLATURE INTRODUCTION 6 PART I - TEST PLAN 7 PART II - TEST PROCEDURES 108 PART III - QUALITY ASSURANCE PLAN 212 ENCLOSURES ENCLOSURE 1 - PANTHERS PCC TEST FACILrrY P&ID: 00209 DD 93 Rev i 221 ENCLOSURC 2 - SCIIEMATIC OF PLANT CONFIGURATION FOR TEST C 03 222 ENCLOSURE 3 SCHEhiATIC OF PLANT CONFIGURATION FOR TEST C-04 223 ENCLOSURE 4 - SCHEMATIC OF PLANT CONFIGURATION FOR TEST H 01 224 ENCLOSURE 5 SCHEMATIC OF PLANT CONFIGURATION FOR TEST H 02 225 i l i 1 l N a> , - , . , , - , . . . . . , , ,,-. , , , ,
i D ( "" Rec Page of SIET l I l ' -eccr.c Resion innovativi >
'(1094PP91 t 0 i 5 225 I
T Temperature TC Thermocouple TCV Temperature Control Valve TP&P Test Plan and Procedures Tw Wall Temperature UGQ Quahty AssuranceOffice V Volume s Fluid Velocity VL Vent Line VME Versa European Module VMS Virtual Memory System i I l l j
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k==' Rn j Page j of , SIET l I f(KNMPP91 1 0 i J f 225 sez2one kcarian innovativi LCV level Control Valve LSB Last Siendicant Bat LVDT Linear VanaNe Differenual Transformer MIPS Mega instruenon Per Second MO Motor Operated NWL Normal Water L. vel OD Outsude Dnameter P Pressure PASTHERS Performance. Analysis and Tesung of Hear Removal Systems PCC Passive Containment Condenser PCV Pressure Control Valve P&ID Process and Instrumentauon Diagram PLC Programmable Logical Controlier PSD %er Spectral Densiues r Radius RAM Random Access Memory RISC Reduced instrucuon Set Computer RTD Thermoreststance RTE Responsable Test Engineer i S Speed SG Strain Gage S,R V Safety / Rehef Valve SBWR Semphfied Bothng Water Reactor ST Storage Tank -i 1 l 1 I l l i
Dac=='a' R'o Pase of SIET l l ffXWAPP91 i 0 l 7 215 scocme Kennon innova:m 4 PART I TEST PLAN TAllLE OF CONTE.VTS 13
- 1. INTRODUCTION 14
- 2. REFERENCE DOCUMENTS 15
- 3. TEST PROGRAM OBJECTIVES 17
- 4. PANTif ERS.PCC TEST FACILITY DESCRIPTION 17 4.1 Test fribty general design 18 42 Test fxthty locauon 19 43 PCC heat exchanger 20 44 PCC containment pool 20 4 4.1 Pool desenpuon 21 4.4 2 Pool make-up and dram system 21 45 Steam supply system 22 46 Noncondensible supply system 23 47 Dr:un and vent lines 23 4 7.1 Dr:un line 23 4 7.2 Vent hne 23 48 Condensate drain tank 24 44 Vent tank 25 4.10 C.atch tank
Docummt l Rev Page j of SIET j
' orXPMPP91 r) I 6 i 225 secone Healton innovativi INTRODUCTION ne tests scafed m this document are pan of the program to design and cendy the SBWR. The PCC ostem penorm vital roles in removing heat from the contamment dunng xcident condaccas. FuD-scala prototypical condenser for t!us systems are to be tested at full pressure, temperature and flow condiuorts.
The test fxtlity specified fcr this prograrn are not representauve of the SBWR systern of which this condenser will be pan. The spectred tests are " component
- tests and therefore the test systern performance a not intended to be representauve of the 5BWR svstem performance.
This Test Plan and Procedures document conststs of 3 parts: Part I contains the Test Plan including a general desenpuon of the PAYlEERS PCC program; its itectnes the expenmental fxti;ty, including the mstrurnentauon. the control system. the data acqu2sition system, the different types of tests including cold and hot shakedowns. Part 11 : contains the specific mstruction on how the testing shall be performed. Part 111 : contains the Quality Assurance Plan. 1 1 l I
b Document R2v Page of i SIET l l ser;one kcuum truwaum 00098PF91 () i o 225 47 7 DATA ACQUISITION SYSTEM Hardware configuranon 47 7.1 53 i2 Software 57 7.2.1 Measurement channel block 57 7.2.2 Alarm condiuon code block 57 7.2.3 Action code block 57 7.2.4 Monitor page block 58 ~ 73 Software qualificaoon 59
- 8. DATA ANALYSIS AND RECORDING 59 4.1 Data reduction 59 8.1.1 Digitally acquired quanuties K.1.1.1 Dtrectly measured quantities 59 Absolute and differential pressures 59 8.1.1.1.1 Temperatures 60 M.1.1.1.2 Dispixements 61 M.I.l.l.3 62 8.1.1.2 Denved quanuties Flowrates 62 8.1.1.2.1 65 8.1.1.2.2 Levels Pool density 67 8.1.1.2.3 67 8.1.1.2.4 Strain Condensation thermal power 68 8.1.1.2.5 71 8.1.1.2.6 Heat flux coefficient 71 4.1.2 Analoeically xquired quantities 72 d.2 Errors evaluauon
Iww.i j ne, j P.a. or SIET l l senone Kcaricri innovenv' ' (000itPPQ1 0 t 4 ! 23 25 4 11 Pipmg and valves 26 !. TEST INSTRUMENTATION 3.1 Instrument type and charactenstics 26
'.l.1 Absolute and differential pressure transminers and transducers 27 4.1.2 Thermocouples and thermoresistances 28 5.1.3 Flowmeters 29 Fluid level sensor 29 5.1.4 5 1.5 LVDT 29 5.1.6 Strain gages 30 5.1.7 Accelerometen 30
<2 Instrument calibrations 31 1
- 6. TEST PLANT CONTROL AND SAFETY CONSIDF*tATION a f 6.l Controls system desenpuon 44 6.1.1 Steam llowrate control loop 44.
6 1.2 Temperature controlloop of the steam .nr miature 44 6.1.3 Air flow rate control loop 44 6.1.4 Condensale tank level Control l00p 45 6.1.5 Pressure control loop 45 6.l.6 KC poollevel controlloop 45 62 S.derv considerauon 46
Docuament Reo Page of SIET l l
- 00@8PP91 ! O I II ! 225 scuane kcanon inruwaim gg 10.72 Test A.3.2 : simulated pneumauc leak test pressunnanorts 89 10.8 Desenpuan of test type A.4 gg 10.9 Descnpuon of test type B.I 90 10.10 Descnpuon of test type B.2 92
- 11. TEST MATRICES 93 11.1 Acceptance entena
- 12. REPORTS 95
- 13. QA REQUIREMENTS
- 14. TEST HOLD / DECISION POINTS !
J LIST OF TABLES l 1 32 Tab.I Explanauon of PCC instrumentauon plant code PANTHERS PCC c apenmental measurement tag list 33 Tab.2 43 Tab.3 PANTlERS. PCC flowmeter device charactenstes Tab.4 - SBWR PANTHERS: Full Scale Prototypes PCC Test. 97 Cold pre-operanonal Test Matna Tab.5 SBWR PANTHERS: Full Scale Protot)Tes PCC Test. ! 98 Hot pre +perational Test Matnx 99 Tab.6 PCC First Pnonty Test Matnx Tab.7 Pan A. Test with two modules. Test tyTe A.I.! 100 Steady State Petfomance Saturated Steam / Atr Mixtures. Test Cordtats
1 i i i Da'"" Rn Page l of SIET l l l secone Hewian innovativi ,{ rn)gRppgl 0 1 10 l 225 Data processing and analvtis 73
<3 54 Data records 73 74 45 Data sheets 9 SHAKED0%'N AND PLANT CHARALTERIZATION 76 Plant characterizauon 76 9i General desenpuon of test C-01 77 9.1.1 General desenpuon of test C-02 77 9.1.2 General desenpuon of test C-03 77 91.3 9.1.4 General desenpuon of test Cet 78 9.1.5 General desenpuon of test H41 78 General descnption of test H-02 70 9.1.6 9.1.7 General desenpuon of test H-03 80 a l.8 General desenption of test H-04 80 9.1.9 General descnpuon of test H-05 80 ,
81 42 Shakedown mainx
- 10. PASSIVE CONTAINMENT CONDENSER TESTS 82 10.1 Tvpes of tests required for the PCC 82 R3 10 2 First pnontv tests 10.3 Desenpuon of test type A.I.1 83 10 4 Desenpuon of test tpe A.I.2 44 10 5 Descnpuon of test type A.I.3 84 10 6 Desenpucriof test type A.2 86 10.7 Desenpuan of test 19e A.3 87
-10.7.1 Test A.3.1 : sitnulated LOCA pressuruzauons 87
Doermeet Rev Page of SET l l l scocnc Heum Innovaim i M RPP91 1 0 i 13 ! 225
- 1. INTRODUCTION ,
Part 1. Test Plan .contams a general desenption of the PANTHERS PCC program: its obreuves the expenmental frihty, including the instrumentation. the control systems, the data acquisiten rystem. the ddlerent types of tests. includarig cold and hot shakedowTis. i
Doc "'"* ' Rn j Pm j of SIET l !
' 225 vnone desun leum n009RPP91 f) i 12 i l l
l Tab.8 Part A. Ten with two modules Test vpe A.I.2 j Steady State Perf omance - Superhealed Ste.am/ Att Mixtures. Test Condiuons 101 l
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Tab.9 - Part A. Test with two modules-Test type A.I.3 I Steady State Pertomance - Steam Only No Air in PCC tubes. 102 Test Condicons Tab.10 - Part A. Ten with two modules-test tvpe A.I.3 Steady Stase Perfomance Steam Only Air in PCC tubes. 103 Test condiuons l Tab. ll - Part A. Test with two modules ! Test type A.2.1 Effect of Pool Water Level- Saturated Steam l Test type A.2.2 Effect of Pool Water Level Saturated Steam / Air 104 , Mixture Test Condnuons l 1 Tab.12 - Pan B. Test with one module test type B.1 I Steady State Perfomance Steam Only. No A2r in PCC tubes. 105 Test Condiuons Tab.13 - Part B. Test with one module test type B.I Steady State Perfomance - Steam Only. Air in PCC tubes. 106 Test Conditions Tab.14 Part B. Test with one module test type B.2 Effeet of Low Denstry Non Condensibles. Test Condiuorts 107 k
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l l Dac= a' Rev Page of SIET l l sesone Mesuri Annovanvi i 0009RPP91 ! 0 l 15 1 225-I i 1
.t . TEST PROGRAM OBJECT &T.S J The general objecuves of the full scale PCC test are iref. 2.1.11: .n Thermalhydraulic : confirm that desigr.ed PCC meets the thermalhydrsuine performance requirements for use in the SBWR I
hi Structural : confirm that the mechanical design of PCC is adequate to assure the structural integnty of the unit for the expected SBWR lifetime service condauons. c) Sinsk Module Test : confirm, with PCC tests, that the test performance of a half urut 1C is an adequate representation of the performance of a full-urut IC. The thermalhydraube specific objecuves are:
.n measure the steady state heat removal capabibly over the expected range of SBWR condinons: I inlet pressure concentracon of noncondensible gases PCC differential pressurt pool side bulk average water temperature pool-side w ater level I l
hi confirrn that when a mixture of steam and noncondensible gases Dows into the PCC. the uncondensed gases will be discharged from the vent line and the condensate will be discharged from the drain ime. c i confirm that tube side heat transfer and flow rates are stable and without large Huctuauons, f di con:irm that there is no condensauon wster hammer dunng the expected startup, shutdowm and operstmg modes of the PCC. ea m:ssure the inside and outside wall temperature at typical tube locauons to:
Doc =""' Rev Pate of SIET l l l senone Hearton innova'm I (0098PP01 1 0 t 14 l 225
- 2. REFERENCE DOCUMENTS i 2.1 (iE documents ii ISOLAT10N CONDENSER & PASSIVE CONTAINMENT CONDENSER 1EST REQUIREMENTS. Document Number 23 A6999 Rev. I 2.2 SIET documents I> PCC TEST FACILITY DESCRIPTION.00094 RI 91 Rev. 0
- 2) IC & PCC TEST FACILITY DATA ACQUISITION. INSTRUMENTATION AND PROCESSING SPECIFICATION .00095 RS 91 Rev.0 h PANTHERS PCC TEST FACILITY P&lD: 00209 DD 93 Rev.1 2.3 Other documents 1i CAPSULATE STRAIN G AGE KHC, KYOWA Operauon manual
- 2) THERMOCOUPLES CLASS!FICAT10N AND STATIC CHARACTERISTICS UN17938 h PLAT 1NUM RESISTANCE THERMOMETERS MARKING AND STATIC CHARACTERISTICS UN17937 4i MEASUREMENT OF FLUID FLOW BY MEANS OF ORIFICE PLATES. NO77f FM OR VE.VTURI TUBES INSERTED IN CIRCULAR CROSS SECTION CONDUITS UNI 10023 i
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L 1 1 Doemet Rn Page of l SIET l n0(98PP91 0 17 225 l senone Reanen innovaim i l I I 4 P ANTHERS PCC TEST FACII.rTY DESCRIPTICN 4.1 Test facility general desean The flow diagram of Panthers PCC test factlary ts shown in tenclosure !). De main components o(the plant are : PCC condenser PCC pool makeup water system
- drain ime vent 1:nc condensate drain tank noncondensible vent tank steam suppiy system noncondensible supply System The design criteria are:
al PCC coed.:sr a full scale prototype of the SSWR Passive Contanment Condenser 2 to PCC pool: the total volume (173 m 3), the pool area (29.84 m2),the botloff operung area (2 m y and the nommal water level 14.4 mi of the ref erence pool. are preserved. The KC pool volume can be reduced by a dsaphragm to perform PCC single module tests, maintaining the same pool area per module ci makeup water system: at allows to mamtain a constant pool level at the maximurn condensauon rate d) dt:un line: it is prototypical as m pracucal with respect to inside diameter 16*) and elevauon difference
Doc u'"' R" P*** o' SIET l I l scuone Mention inncmim ! (009MPP91
- O t 16 l 225 a provuje diagnosuc informanon ior invesugauon of unexpected condenser performance un provide informauon usefut to contirm the understanding of tubessde performance no provide a fundamental data base for conf umauon of TRACG simularrwi of poolside performance.
f1 establish PCC unst pressure losses with air Dow only as a benchmart against whach to compare in plant PCC air flow performance. The structural specific obgctives are: ai measure the stress levels at the entical locations on the PCC in the foUowmg condsuons: o steady operation at dif ferent containment pressure, temperature and air mass fracuon ut pneumatic teak testing I no transition trom operatam at normal containment condiuons to LOCA and severe accident l s onditions. ) i hi measure the vibranon at entical locations on the PCC resulting from th v and/or condensanon. l j
. i demostrate by performing 5 umes the expected number of pressure and thermal cycles that the PCC will i i
successfuuy service 60 years of SBWR. i di confirm. with PCC tests. that the test performance of a half unit IC is an adequate representauon of the l performance of a f ull-unit IC. i l
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! SIET Dac=mest Rev Page . of - ] !
, Senone Region innovativi I (10098PP91 - 0 19 22.5 -e f
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'I a elevauon between the PCC pool bottom and the NWL of the PSP (15210 mm) i 4J PCC best exchanger The PCC heat exchanger consists of the following major components:
at a 10* vemcal ini-t line for steam.azr mixture supply with insegni flange for connection to pool floor , hl a steam-air distributor t c) two 8" horuontal feed ime t dI two horizontal upper and two honzontallower headers (660 mm inside diameterl with integral nozzle _ and bolted covers E t er 496 stainless steel tubes.2* OD i ri iwo 10" verocal dram ime l g) two 6" vertical vent lines h) seven 2" nozzle for instrumentation cable penetranons o ten 1/4" NPT nozzle for thermalhydraulic measurements ,
~ 'i The PCC is composed by two identical modules with total thermal capacity of 10 MW1. The vertscal 10 main steam supply Ime feeds two honzontal headers through an upper distnbutor and two 8* pipes.
Steam is condensed inside a bundle of 248x2 stainless steel (SA 213 TP 304L) 2* verocal tubes. with
' .'s.8 mm OD and 1.65 mm of thickness, and is collected in two lower headers.The condensale as rernowd to the d through two 10' pipe connected by means of two 4" pipe, to a common 6" masa drasn line condensate tartk. At the Mader outlet the drain nozzle contams also the vent ime for drrving the 6
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Doc = Rev l Pcte of SIET I i senone desun innossiivi i tiOW8PP91 0 i is 225 ei .ent line: it is prototypical as in practical with respect to mside diameter (10") and elevsoon ditference 0 sondensate drain tank: it reproduces the presence of the GDCS poot it collects the steam
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condensed by the PCC and it keeps the pressure in the drain line equal to the mlet pressire: the tank has been designed to mamtain a good control of water level dunng tesung with the greatest enpected condensate DowTate, by means of 6* internal tube as overflow system or by a bottom discharge hne and a level control system: g; noncondesiele vent tank: it reproduces the presence of the PSP. it controls the discharge pressure of the PCC and collects the atr / uncondensed steam misture separated in the PCC.The tank has beenarranged such as testmg may be performed with the end of vent line either submerged or unsubmerged hl steam supply System: saturated steam is supphed to the PCC at a controllable Dowrate m the range up to 6 6 k g/s with a pressure in the range of 170 to 790 kPa o noncondensible supply system: a:. u :.ippliert to the PCC at a controllable flowrate in the range up to I kg/s with a pressure in the range of 170 to 790 kPa The Panthers-PCC capabihties. summanzed in tref. 2.1.1). cover the range of the SBWR xcident 6 0ndition s. C Test facihty locatkm The Panthers-PCC test taeshty is located m the SIET-Piacenza laboratones and is built mside the *EMILIA" piwer station. The position of main components have been chosen so as to respect the elevauons of the 5BWR reference plant The followmg elevation differences are preserved : .o normal m ater level of containment pool at wi0 mm . N elevations between the PCC pool bottom and the nonnal water level of the GDC5 poola2500 mmi i
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D*cament .Rev .Page . or STET l-0 225-
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00098PP91 21 vaane Reareri innovaim 1 1 The PCC pool is also provided wnh : a a 4* drain hne bi a 2* dram isne i a a 4* overflow ime i d) a 14' emergency discharge line , PCC pool total volume is 173 m3 : PCC pool water volume (at NWL) is 131.3 m): IC pool total volume is 98 m3 :IC pool water volume (at NWL.) ss 74.4 :n3 4.4.2 Pool make-up and draie system j Dunng PCC tesung the IC pool is used as makeup tank. The makeup tank is connected to the PCC pool ty '
- means of an 8' lower line to replace the boil off and the water that overflows through the 2 m2 :
1 opening area. to the exth tank. The PCC pool water level is mamtained constant controlling the IC pool water fewl by means of an cxternal water makeup Ime and an overtlow line. The extemal make up line is designed to mamtmn a constant pool water level at a maximum condensauon rate. The maximum waaer temperature is 40 *C. 4.$ Steam supply system The required thermal power for PCC testmg is supphed usmg superhesied steam bleeded from the ENEL PC-tevante power station. situated neartiy the SIET laboratones. The suwtM steam is bleeded at the followmg condauons: ! T = 540 *C ., P = 17 MPs F max = 6.5 kg/s t ]
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Document Rev Page of
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noncondensible gases to the vent tank. This ime consists in two 8* pipes that yom in a common 10" line. At the ends the headers are closed by two bolted Hat covers. The PCC unit is supported by <=Mies krated at the extremitaes of exh lower headers. For the single module tests the hortzontal 8* feed line of malute 2 will be excluded. I 4.4 PCC containeret pool 4.4.1 Pool desenption The PCC full. scale prototype with inlet, vent and noncondensate drain piping are sneallaf inside a rectangular water tari. This pool is covered and open to the atmosphere. The tank is supported by means of a bolted beam syrtem layed to the fifth Ocor of the building. Dunng testmg the nommal level of the cooling water in the pool is mantamed at 4400 mm : therefore the honzontal Un of the upper header is placed 1.3 m below the pool NWL.The pool floor is prtmded with proper openmgs for the pipe crossmg and have provisions for the saddie supports. The pool wall is provided with a nxtangular opemng of 2 x 1 m . located 250 mm aoove the NWL for bod-off. For manufactunng and transport purpose the PCC pool is composed by 24 panels to be assembled in the I pool installation area. Each panel made of laminated plastic (fiberglass)resaforced by an internal s cel structure. Two conimuous seugens are connected by means of intemal plastac welding and fixed together with stainless steel t.olts. This wlution enshures a good mechanical resistance and thermal insulation. The pool walls and Door can casdy support contamed liquid temperature up to 130 *C. The l iotal average thickness of the lammated fiberglass is 12 mm. Accountmg the mternal steel remforcement and the final fiberglass coating, the total thickness of the pool walls and floor is 163 mm , .l I To control the pool level and replace twJil of f dunng a test the PCC pool is daectly connected to IC pool by means of : l ai sp upper ctreular steam duct. m fiberglass. I m OD and about iI m long : N a lower H" pipe. m cartion steel, for PCC pool wster make up. with stop valve. ..
D**"*en t Rev _ -Page of SET-Secone Reanors innoverm 00098PP91- 0 23 125 manmum delivery perssure : - 2.8 592 -The air produced by the compressors is appropnately dehumidified and sent to the plenuen chamtwes. The air is then sent to the miung pomt passing through a flow < ate regulanon system.a flowrase measurement onfice plane sysaem and a manual valve operatmg as enucal flow onfice. This devre, operanns with - ddierent flow an:a keeps the flowrates mdspendent from the PCC inlet pressure. J.7 Drain and vest line 4.7.1 Drain time The dram line connects the PCC outlet to the condensate tank inlet.The characteristics d the pipe :lengh. volume, cross area. metal surface and weight, with the mstrumentauon locanon are reponed m (ref. 2.2.1). 4.7.2 Vent line The vent hne connects the PCC outlet to the vent tank inlet. The charactensues of the pipe t lengh. volume, cross area. metal surface and weight are reponed m (ref. 2.2.1). 4.8 Condensate drain tank The condensate tank ss a closed, pressunzed tank pantally fi!!cd with water that simulates the funcuans of the reference GDCS pool .The darnensions of the CT have been set accounung the following factors: al dimensions of pre existent structures and other components of the test factisty, b) observance of the elevauon between the PCC pool bonom and the GDCS pool NWL in the SBWR plant (2500 mmi
I l 1 Dac= "' Rev Page of SIET l l vocwe demum Innovaim (OOMPP91 1 0 22 225 ne conditions of the superheated steam available for the test facdity are affected by the heat losses and pressure drops along the adduction inne. ne supernested steam is supplied to the test fxdity by gradaaly opening the valve R)01. The steam n Jesuperheated supplymg cold water at the foUowing maximum temperature, prtssure, and flow-rate onditions : Tmax = 100 *C Pmax = 26 MPa Fmax = 6.5 kg/s The cold water is mixed to the superheated steam in tw mixing points. The first desuperhcanns is obtained through the three way valve R04. Downstream this mixing point the steam is stall superheated iri order to avoid phase change through the flowrate measurement device. The second desuperheanng mixang point n located at the end of the steam supply line and it is used to bnng the steam to the required test conditions. 16 Nnneimdenuble supply s.vstem The noncondensable supply system is composed by : > m two three-stage displacement compressors bi two plenum chambers connected in parallel ei pressure reduction group di Dow. rate measurement system Each air compressor produces: maumum air now : !$00 Nm3/h i
Doc = Ree Page j of SIET 1 l l ~ secone Hewim intmenvi ! 0009RPP91 1 0 i 25 ! 225 Jischarge line to adiust the water level during the tests. Thermalhydraulc instrumentauon is prtmded to monitor the following mam parameters: as steam..ur mtxture discturge flowrate bt gas space temperature and pressure aquid temperature and pressure di water level 4.10 Catch tank The PCC test f acility is provided with a water storage tank that has the function of co!!ccting and measuring the amount of water that overflows from the PCC pool dunng the tests. The geometncal charactensues of the tank with the mstrumentation locauon are reported in (ref. 2.2.1). 4.11 Piping and Valves The stearn/ air mixture mlet ime. the drain and vent lines are made of stainless steel carton steel matenal is used for other piping. flanges bolts and nuts. Panthers-PCC main components are thermal insulated by means of rock wool, The valve specifications of the Panthers PCC are reponed m ref. 2.2.1).
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0009MPPQ1 1 0 24 225 s ciaone Measton innovative ! i The CT is located beneath the PCC pool at an elevation such that the tank NWL is 2500 mm kreer than the PCC pool bonom. The condensate drain line is connected to the CT bencain the water level and has a 2500 mm loop seal inside the tank with an outlet section at 250 mm below the NWL. The drain ime can also be connected to a nozzle at an elevation 5250 mm lowr than the PCC pool bottom. This connectson can be j used to perform tests with a controlled water head. In order to masntain the CT gas space pressure at the sarne value as the PCC inlet steam air mixture line, the CT dome as connected to the test secson inlet line bv a l' OD pipe provided with a spectacle flange. De CT gas space pressure can also be controlled by
-I means of an att I injecuon line and a gas l' outlet hne. In this case the spectacle flange wdl be closed. The air injection ime as connected with the main air supply line and is equipped with a pressure control valve. A constant water level in the tank is mamtained by use of a 6' OD drain lirie. This hne is equrpped with a level control valve and a flowrate measurement device. The hne drains water through a pipe situased inade ,
the tank with an inlet secuon at the tank NWL. The drain hne can also be u,. .cced darectly to a 4* nonde f near the bottom of the tank. Thermalhydraulic instrumentation is provided to momsor the following main parameters:
.o condensate Dowrate e
i ht hqusd temperartee and pressure , b ci gas space temperature and pressure di w ater level 4.9 Vent tank The vent Tank i VT) is a closed. pressunzed tank. The VT is located bencain the PCC pool at an eleva's uch that the NWL is 15210 mm below the PCC pool bottom. The noncondensible gases seperated in we PCC and the entramed uncondensed sacarn are vented through a 10' OD line to the vent tank. The vent ime is connected to the tank beneash water level
.it 7.80 mm below the NWI, ' e gases are discharged from the ven; tank directly to the atmosphere through
. control valve. This va!.t controis the pressure of the circuit. The ver.t tank is also provided with a 3"
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)
i
, re, = . - . - . , . . _ . _m _.________m __m_____.__
Doe:"'*
- Rev Page of SIET l l l senone Keatum innovaim n0@RPPQI l 0 l 27 225 the instrument type the instrument plant code ,
ine instrument span the measurement unit the instrument measurement rcuracy the instrument SIET code the ref erence dramng of documents SIET 00095RS91 A)0209DD93 5.1.1 Absolute and differential pressure transmitters and transducers Absolute and differenual pressures ase measured by means transmitters and transducer. The transmittets haw e the foUowing main features: Siiscon piezoresistave sensor: Microprocessor based electronics: l Compensauon of temperature and stauc pressure changer: l l Mcasunng ranges: 0-10 MPs: 0 2 MPa: 0 100kPs: 0-250 kPs: 0-700 LPa:
)
Ranneability: 5 or 10: i Accuracy: =+/-0.25 %: +/-0.5%: +/- I% of cahbrated Span: l l
- a. . . - , . - .- . . . . - . - .
l A D***mee t Rev Page of , SIET .l .i
- 4 0009RPP91 0 26 225 senone Reman innovaim 't ,
i
!. TEST LNSTRUMENTATION 5.1 Instrument type and characteristks The thermalhydrauhc parameters to be measured are both direct quantstics (absolute and differennal pressure, temperature displacement and vibrauon) and dmved quantaues (densty. Ilowrase level and -
str:un). Different methods are used to measure the above parameters:
- 1) Pressure - pressure transmitters h
21 Differenual pressure - differenual pressure uansmitters
- 3) Temperature - thermocouples/thermorcsrstances
.3
.t) Level - differenttal pressure transmitters h Pool density - differential pressure transmitters s N Rowrate - differential pressure across onfices. ventun tubes and vanable area ortlices ;
- 7) Displacement LVDT(linear vanable differentsal transformer)
- 8) Differential clongauon/ strain stram gages m Vibrations - Acelerometers The overall instrumentauon location on the plas.t is reponed in the documents SIET 00095R591 and 00:09DD931 enclosure 1).
The explanauon of the measurement idenuficauon t.ag is shown in Tab.1. Tab. 2 reports the measurement . Itst with: b
- the instrument component or hne location i t
Docuent Reo Page of SIET I l 00098PP91 l 0 29 225 secone Reanan innovativi i Diameters: 0.5-3 mm:
- Sheat matenal: Inconel 600/AISI 316:
Measunng range: 2731533 K: Accuracy class: ANSI special (min.+/ 1. !'K): Time constant: 0.2-0.3 s. The temperatures of the fluid in the PCC pool will be measured using RTD thermoresistances type PT100 t DIN 43760)l00, dsarneter = 4 mm. 5.1.3 Rowmetres The flowrste of single phase fluid (water, steam /str) is measured by using different pnmary elements: cahbrated onfices. Ventun tubes and vanable area onfices "GILFLO*. Flowra measurement devre specifications are given in Tab. 3. 5.1.4 Ruid levei sensors Liquid level in smgle phase or collapsed level in two-phase are measured by differentral pressure transmitters. 5.1.5 LVDT Displacements and positions are measured by means og high temperature waterproof transducers type LVDT itinear vanable differential transformert having the followmg features: l
^
1 Doe ="a ' Rev Paste l of l SIET l l semme Memon Inixwaim 00m RPP91 i n i 28 I 225 , I 1 A ppications: I a pressure drops on piping.onfices and Ventun tutes; b absolute pressure measurements; I a hquad and collapsed level measurements, l 1 l In some cases pressure drops on pipmg are measured using differential pressure transducers (instead of . transmitters) having the following main features: i stram gage sensor l i l measunng range : +/- 34 LPs xcuracy 5 +/- 0.25 +/- 0.5 +/ 1.0 % f.s. J.l.2 Thermocouples and thermoresistsoces The temperatures of the Guid pipmg components and pool water are measured usmg undergrounded I heathed thermocouples type K. The Guid thermocouples will be installed on the plant pipelmes normally with the hot Junction on the prpe
.tus iD/2); some thermocouple wdi be mserted mio the pipe with different entenon (s.c. D/4). Welded plate l
a all thermocouples are mstalled on the PCC heat exchanger mixture inlet ime upper and lower headers tube hundle and dr:un line. Brated wall thermocouples are mstalled on the PCC heat exchangers tube bundle. The deta.tl of the instrumentanon location is reponed m document SIET 00095RS91. The charactensucs of the type K thermocouples are: Cromel-Alumel unction; J Isolation by MgO:
Docuiment Rev Page of SIET 0009RPP91 1 0 i 31- 225 secone Reances innovoim 1 3.2 Instrunneet calsbrances . The absolute and differenual pressure transmitters and transducers wdl be cabbrated in laboratory before >" ihe installabon on the plant XCordmg with SIET 00ll8PO91 procedure. The transmmers maumurn error .
*di te calculaird comparing the cahbrahon pomis to the comspondent values calculated with the
-i ,
manufacturer mstrument constants, ne transducers mammum error wdl be calculated performmg the least square method lancar interpolanon of the calibrauon points, if the calsbrauon error is lower or equal than the assigned accuracy, this one will . he assumed as mstrument maximum ermr. else the higher accuracy raung will be assumed. The thermocouples wdl be cahbrated m laboratory before the installauon accordmg with SIET 00165PO92 l procedure: if the mstrument meets the ANSI MC96.1 special specificanon. the relative ANSI special i xcuracy (* 1.1 *C or 0.4% whicherer is greater ) wdl be assumed to evaluate the measurement error, else . the cabbrauon erTor will be assumed. The thermoresistance wdl be cahbrated m laboratory accordang with SIET 00166PO92 procedure: if the cahbranon error is lower or equal than the error defined by UNI 7937 specificauon this one wdl be assumed I as instrument mammum ermr. else the cahbranon error will be used. l
' The flowrates measuremems wdl be performed usmg cahbrated noules xcordmg with SIET 00221PP93 procedure. Flowrate error will be calculated talang into account the noule Oux coefficient cabbranon errors; tor not cahbrated nonles (i.e. D>=50 mm) the flux coefficient error as suggested by UNI 10023 pecificauons will be used.
The LVDT will be cahbrated in laboratory before the mstallauon accordmg with SIET 00235PO93 procedure. The accelerometers will be cahbrated in laboratory before the installauon according with SIET 00234PO93 procedure. l Cahbrated stram gage will be used. the cabbration certificate will be given by the manufacturer. 5 6 5 P
--. - ..,_m. . , . -. 4 -
D* * " " ' Rev Pase of SIET l l vnone Reuion innovenivi i n0098PP91 ! 0 10 ! 25 i l I i l l Range:. +i 25 mm l Lineanty: 0.5 4 f.s. l The LVDTs are installed on the steam distnbutor, the conjunction between feed line and upper header module I and on the PCC heat eschanger suppons. The detail of the LVDT locauons is reponed in SIET document 00095RS91. 5.1.6 Strain gages The PCC local strains are measured by means of capsulated high temperature strain gages. The strain gages are installed on the PCC misture inlet hne. upper and lower header, tube bundles. supports and drain line. The stram gages sicaih matcnr.!:s SUS 314 The detail of the strain gage locanons is reponed in SIET document 00095RS91. 5.1.7 Accelerometers High temperature waterproof xcelerometers with built in electronics are installed on the steam distnbutor. ihe upper header of module I and at mid length of some condensauon tubes. The main charrtenstics of the , Acelerometers are: Range: +/ 10ry) g Resolution, +/ 0 02 g Frequency range: +/- 54: 1 5000 Hz Resonant frequency:: > 40 k Hz The detail of the xcelerometer locations is reponed in SIET document 00095RS91.
lab 2 Pu llit lh I't T e mperiment 4l measurement tag list ._ - l Plant unic Spn mu An ur ai y SitT ank RefD*g ! Gunpment us line im mum in,uument type , b g (TPt R liF ADFit MODUI E I I Al T0Kols hg i Intemel Du=1 temperature (bak sule) Thernunouple K T AWI O.200 T +/II T Internal Guid temperatuse (fn=* side) Thernuumple K T A002 0:200 0 : 21V) T T
* / I l *C
+/II T TEK029 TCK 247 bg i bg I fg gg Neer ba k cover nange (mi . sue ) l') Thenmuouple K TW A001 Thenmrouple K TW A002 0:200 T +/ 1I T KK248 ha i _ H Neu bak coves nanze test . mi)(*) TCK249 Fig I g Near bmk covee nange (mt . mr)(*) Thenmrouplc K TW A001 0 : 200 T e/ I l T Thennucouple K 0 : 200 T +/ I I T TCK 250 Fez 1 J Fnmi cover. me (*) , _ W AmM TUK25 Feg i {
Thermocouple K TW Ams 0 : 200 T 4/ II T ' Fnmi cover. est (*) TEK252 Fig I Near bak suver nange (es . sup )(*) Thermocouple K TW Antw 0 : 200 T +/- t I T i DP Translucer DP015 -M.+M kPa 0 25 % f TSD026 h u 2.1 -
Urrer heades iuk 2 A elevatum c DP Transluter DP(14 at:+M kPa 0 25 % f a TS9027 Fru 2.1 (fpper header - sube IC, elevatum c bgg 2.1 DP m7 11 : + 14 kPa 0 25 % f a TSD02 Upper header + tube 4D. elevatum c DP Transducer DP Translucer DP m8 - 18 . + M kPa 0 25 % is TSD029 b u 2.5 Upper hendes - tube 3R,elevatum c DP Transfocer DP G79 M : +M L Pa 0 25 % f a TSDoll bgg 2.1 3 p Urper header - ruhe SR. elevasum c S M DP 027 31 : + M kPa 0 25 % f a TSDol2 has 2.1 l'pper hemics tube SY. elevatum c DP Translucer DP010 -M:+H kPa 0 25 % (s. TSDOM b u 2.1 % h Upper heades - tube UR. elevstum c DP 1ranslucer 2 3 DP Transluter DP oll .M : + M kPa 0 25 % f s TSD017 har 2.i ~ ~
Umer heater . sube IV. elevatum c kPa 0 25 % is. TSD016 has 2.1 Upper header tube 5-l. elevaanm c DP Translucer DP012 -M : + M
-M : +M 0 25 % f: T3tXM1 hag 2.1 Upper hende - tuk 5 6 elevstum c DP Teansluter DPOil kPa O:10 MPs 0 25 % i s. TMA014 Fig 3 intemal fluid pressure P-Treneminer P AUDI Thermocouple K TW AB001 0:200 T +/ I I T TUK125 ha i _ _
Fnet cover lule, angulw on I (*) inme eoves tels. angular en 2 (*) Thenmrnus4e K TW AB002 0 : 200 T +/ 1.8 T TCK226 Fig i Thermacnuple K TW AB001 0 : 200 T +/II T TUK127 Fiz I Frime cover tv4e. angular ow 3 (*) o E VH A001 0:500 g 0 02 g AtXuit ha 1
- Ba k cover, X duct 1=si Accelm . 4'ar VB A002 0:500 s 0 02 g ACG02 bz I Dak cover, Y direstam Act etu s..xter VB A001 0 : 500 g 0 02 g ACmol Fig I _
Bat k cover, Z dres1mm Attelm .. wies -- Siram gage DX- A008 + /- 0 5 % mm/mm + /- 5 % m v . SCG2 ha 1 Near bak Range (ens . sup . as the) SC@3 ha i Strun gage DX AfM2 +/- 0 5 % mm/mm +/- 5 % m v N Near bat k Dange (eat , sup . cir. dir) 5 am game DX A001 +f- 0 5 % mm/mm +/- 5 % m v SC@4 ha I " Near bu k Dange (ins . sup . at das) DX A0(M +7 0 5 % mm/ min +/- 5 % m v. 5G075 Fez i Neas bm k nange (mi , sup , car dis) Sirein nage Sunon ange DX A005 + /- 0 5 % mervmm +/- 5 % m v SCM6 - ha i Near bak flange test , int , as der) SC@7 Fig i Near bak Hanse test , mt , sir, dir) Strain sage DX A006 +/- 0 5 % mm/mm +/- 5 % m v. DX A0(I7 +/- 0 5 % mm/ man +/- 5 % m v. SC@8 Fez i Near ban k flange (ma ,inf , as dir) Siram gage DX AOLE +/- 0 5 % mm/mm +/- 5 % m v. SCG9 Fig I Near back finaze (mt .mf-.cir dir) Strain sage h, I.
+/ 5 % m v. 50080 Feg 1 Fnma cover cenaral punum (mt.), X dir Sirain rage DX A0lW +/ 05 % mm/mm
. .v. ,t. . + /- 5 % m v . 5G081 Fes 1 Fnma w.a central positum (int ), Z dir Sirein game DX A010 +/- 0 5 % T Stamin game DX Anil +,- 0 $ % ;w,t.T. +/- 5 % m v. 50082 Fig I __
Fnmt cnver ceneral pnsitum (ess ), X die
+/. 0 5 % mm/inm +/-5 % m v. 500R3 ha i Pnmi cove aeniral emtsm (eat ), Z die Stemin game DX. A012
+/- 0 5 % rrun/mm +/.5 % m v- 50084 Fez I Fnmi cover bots I, pm E Stenin gaze DX AB001
---m---_m..._ _,,._________,_________ _
Da* *"' Reo Page .l of SIET .I .! scuane Hemen Innovatm 1 0009RPP91 i 0 12 ! 225 Tab.1 Explanation of PCC irtstrumentation plant code X - Y Z' T 1
'l 1
I ahere: X = PHYSICAL P AR_6 Y = PLANT LINE OR COMPONENT I Differenual pressure I = Steam inlet line i DP = \ 2 = Non condensible annet hne DX = Differentsal elongauon 3 = Desuperheaung line F = Flomvate
= Level 4 = Mixture mlet line L
5 = Condensate draan line P = Absolute pressurt 6 = Vent lane PO = Postoon
= Fluid temperature 7 = Steam bypass hne T
TW = Wall temperature 8 = Main desuperheaung line Vibrapon A = Upper header module 1 VB = B = Tube bundle module 1. C = Lower header module I , D = Upper header module 2 i E = Tube bundle module 2 j Z = PROGRESSIVE NUMBER F = uwer header module 2 G = Drain line first length ' , l = Vent tank , T = SPECIAL TAG L = Condensate tank M = Make up Ime i = internal wall N = IC/PCC pools connecung hne 2 = caternal w all O = Catch tank sm = wnbe mark P = PCC pool r = nght side Q = IC pool ;
= left side R = IC/PCC pools draan line I
S = Vent tank air. steam discharge line U = plenum charnber f f 4 i e m , y , . . . , . , . , -~,
lab 2 Cwi J Geng=mient us line im asum insuument illw the u=le Spa mu Au ur a y SIET unk ikiD=g y TUBE BUNDI E AlODl1E I (86 Tube 18.elevatum e. anzular om 7 (*) &nnu nuple K W pml 0: 200 *C +1 i i T TCK225 KK229 hag 8.9 Fita 8.9 { /) Tube iR.elevaium a anaular pm. 7 (*) hermampic K TW B002 0 : 200 *C T
+1Il T KK230 has 8.9 g (%
q Tube IR.clevatum I anauler poa 7 (*) Wrwrouple K TW Bunt 0: 200 el lI T Tde S A.eleva!um 1. annular pm I (*) Wrmmouple K TW B00% 0: 200 T +1Il T KK231 has 8.10 [ Tube 7 A.elevolkm e. ansular em 1 (*) hermwouple K TW pmre 0: 200 *C + /- 1 I T TUK232 has 8.10 S Tube S A, elevethm a. angular pm 3 (*) Nrmorouple K TW Bonn 0 : 200 T +/II T TUK231 has 8.10 $- Uppa -lower beader DP. Transducer DP 026 - 34 : + 14 kPa U25 % fi T50045 00209 DIM 1 _ Tube 85,elevaimm a. anautar pm 3 (*) nennwouple K IW BOIN 0: 200 *C +/- 1.8 T KK134 has 8.10 -- - Tuk SS, elevstum 1. anzular pos 3 (*) Thermornuple K 1W Bolo 0 : 200 *C */ I l T TCK131 Fias 8.10 Tube I A elevetum e.ent well nerwwwpie K TW Bolle 0:200 *C +/- 1 I T TUK056 han 1. Il Tube i A clevMkm a.et wall neswruuric K TW Bolli 0:200 T +/ I l T TUKQ57 hat I. Il
^
Tube I A elevskm b.ent wall nermocouple K TW Bol2e 0:200 *C +1 1.1 T TCKQ58 bas 3.11 Tube I A cleveikm b. ine well nemurcuple K TW Bol26 0:200 T +/-I.I *C TCKQ59 has 3.1l h Tube I A elevstum c. ene wall Thermwouple K TW -B01le 0:200 *C +/-1I *C TUKono Fina 3.Il 4 g tun I A elevnimm c. me wall Thermoruuple K TW Bot 3. 0: 200 *C +/ II *C KK061 has 3.1I 3
~
3
~
Tube i A eleveekm J. cat wall hrmmouple K TW BOI4e 0 : 200 *C +/- 1.l T TCK062 Fina 3. Il Derwrounde K TW-Bol4i 0:200 T +/ I I T TCK063 Fina 3.11 Tube l A cleverum J. ma w all . Tube I A elevatum e. cia m all nermoccuple K TW Bol5e 0:200 T +1 1.1 *C KKOM has 3.Il Tube I A clevetum e. me =sti - nerwrouple K TW Bol56 0 : 200 T +/- t I *C TCK065 has 3.II .__ Tube i A elevenem f. cut wsti TL.- u de K TW BoI6e 0 : 200 *C +/-1I *C TCK066 Fina 3. Il Tube I A elevanke f ins well Thermocousde K TW-80166 0 : 200 *C +/- I I *C TUK067 has 3. Il Tube l A elevetsm a.est wall Tube I A eleveemm a. ine well Thermocouple K neW K TW-8017e TW Bol7e 0 : 200 0:200 T
*C
+ /- 1.1 *C
+/.l.1 *C TCK068 K K069 Fina 3.18 Fias 3. Il o {
Tube l A clevnikm h. est well Thermaromsde K TW Bolse 0 : 200 *C +/- l l *C 10K070 Fina 3.11
~~
Tube l A ctevneke h. int. wall Thermoruuple K TW-Bolse 0 : 200 *C + /- l .1 T KK071 has 3.11 Tube I A enevetum i,ent =nti nerwrouple K TW-Bol9e 0:200 *C +/- l I *C TCK072 Fina 3.11 Tube I A elevetum i . ine. well Thermmouple K TW B019 0:200 *C +/- 1.1 T TUK073 Fina 3. Il v Tube 4 A elevethm e. cat wall Thermocouple K TW B020e 0 : 200 *C +/- 1.I "C TCK074 Fian 3.11 k' Tube 4 A elevatum a. inn. =eli nermocouple K TW B020e 0 : 200 *C +/- 1.I T KK075 Fina 3, il Tube 4 A eleveaum b. ent well Thermacwpic K TW-8021e 0:200 T +/. l .1 *C KK076 011 3, Il -- Tube 4 A elevaram b. inn. =all hermoccuple K TW B02ii 0:200 *C +/- 1.1 *C KK077 Fina. 3. Il Tube 4 A elevetum c. cat wall 1R..-~ tK TW B022e 0 : 200 *C +/- I .I *C TCK078 Fina 3. Il y Tube 4 A ctevenum e ine. wnli Thermoccuple K TW-8022 0 : 200 *C +/ lI *C KK079 Fias 3, Il U I. Tube 4 A elevneum d. ese =all Tkm._,.4 K TW B023e 0 : 200 - T +1 l.I *C TCK080 has 3.II Tube 4 A elevasum d. ine =all TL.. 4 K TW Bolli 0: 200 *C + /- I .1 *C TCK081 Fina. 3. Il __ i Tube 4 A elevetum e, cut well Hermocouplc K T W 9024e 0:200 T +/ l .I *C TUK082 Fias 3. 51 Thermorouple K TW B024: 0:200 *C +/ l.l T TEK0a3 Fias 3.11 Tube 4 A elevatam e. int w ell 6
- , , ~,- , v w - ,,e. --vr - - - --
. v-y.- , - - - . .
r I
- l i
l ! I I ai, 2 r. a J 4 D e Civiipmeine us line its alism linitumesu typ l'lant ude Span mu Au ur a y Sil'Tta=k NciD*g ; w E *"* 1 1:PPER llE4tlF R MODI'l t I l Al ' ~ 6 M Inimt tuver kit 1. pn i Sir mn g age l)X Ahm2 ,/ 05 4 nun /mm *I 5 % m v SGm1 bg i 2
-~
q j I nne tower Mit [g t: Sumn gage DX Aftml e/ 05 % mm/mm */ 5 % m v S0086 bg 1
- Fnet cover Nti 2. pn i Stiam gnge DX AR(ut e/ 05 % mm/mm +/ 5 % m v. 50087 Fig i t Fnet cover Nlt 1. pn E Siren asne DX ABotts_ +/ 0$ % mm/mm +/ 5% mv SG088 Fig I
5 MIXTt!NE INI.E l' l.INE (41 l ' lbanstream mismg pime Anmroui e d K T *nt 0: Im T 4t-1I T WK 010 tai 2tNDin ! _. ._ , Inlet seetum (outside Irc p. s) hrmample K T *02 0 : 200 T + / 1 1 *C TrKoll bg 4 [ Helow sicam aninhuhu Nrmocouple % T4ml 0 : 200 T +I I I T WKol2 Fig 4 lbwstream mismg punt P transminer P *Ill 01:1.2 MPs 0 25 % f 5 TMA(n7 (U2f 6 DIN l Inlet seter.m (outside 100 pm,1) P tiansmuter P *n2 01:12 MPs 025% fs BlA006 (02(NDIM1 ; 7 i DP Tranimities DP ml o : Im k Pa 0 25 % is TMD024 002(NDlW) $ R Inlet sessum unwr heaJes mid i Dntribuhm upper hemier irud I DP Transmuter DP ml 0.25 k Pa 0 25 % is TMDl68 In209Dtw1 4 g Inlet settum upsws heades mai 2 DP m2 0:100 kPa 0 25 % f i BlD162 00209D!N I g g . _ DP Transmuter " Dninbuen . upper hendes nni 2 DP Transmuner DPUN O:20 k Pa 0 25 % f s TMDIN) 002(NDlW l - [ ifg3rr part of steam distrihubir (*) hemmmple K TW4ml O : 2tn T +Ii1 T WK251 ha 4 , hermmuuple K TW .*U2 0: 200 T +1 I I T WK 254 bg 4 I ced line curse stad I. mirados (*) , Feed line surve mid I. estr adin (*) henmmourde K TW 4001 0: 200 T +/ I l T WK255 ha 4 - ' i tipper he ader nud I ami . pm 7 (*) Nrmmouple K TW 4(n4 0: 200 T */ I I T WK256 Fss 4 Thermucouple K 1W4005 0 : 200 T e/II T TCK157 Fig 4 tirper hendee em=1 I cimi . pm I t*) tfpper part of steam dutnbutas. X du Accelertwneter VB 4mi 0:500 g 0 02 g ACG O4 bg 4 3 f ! Fig 4
- tigswr part of steam distnhuku. Y das Ac t elettuncier VB 4001 0 : 500 g 0 02 g ACTul5 At a ciertwncter VB 4001 0:500 g 0 02 g AOCUO6 bg 4 j lipper part of seeam dnenbuenr. Z der tipper para of sieam dninbutor iVDT IU 4ml 0:10 mm +/-05 % is LDTY101 Fig 4 - -
tiggwr heades smal I cent swn 7. X die I.VDT 10 4m2 0: 2 mm +10 $ % f s. LD1102 Fig 4 iVDT 10 501 0.10 mm +/- 0 5 % f s LDT001 Fig I o tliter header nud I toni . pn 7. / der , 8-tipper hemier mal I simiumtum. pis i St nlw muk DX 41sm mrn Fig 4 h Su em aage DX 4001 +/ 05 % mm/ nun +/- 5 % I s. SGou9 Rg 4 Feed ime autse (mal 1). esuaJos Feed lee curve (mial l). mtradim Su am asse DX 4002 +/-0 5 % mm/mm +/- 5 % f a SG)90 ha 4 __ tiggwr hraler rmd I aimpuutum pis 7 Suaan gage DX 4(01 +/05% mm/mm +/ 5 % f e. SG)91 bg4 Us,cr hemier mal I <<mpmrtum. pos I Strain gage DX 40N +/-0.5 % mm/mm + /- 5 % f a. 50092 Fig 4 ' i)PPER HEADER MODUL E 210) y% Fluid tempressure. bait side.pos D hernuanuele K T-luol 0 : 2m T +/.II T WKOM bg 5 a Near back flange, est , angular pu I (*) hermanuple K TW 0001 0 : 200 *C +/11 T TEK238 Fin 5 Near back flange. cat , angular em 5 (*) herrmwouple K TW DfU2 0: 200 T +/ I I T W K259 Fig 5 tigter header - sube IV. elevatum e DP Teansducer DP 015 u : +M kPa 0254 fa nDol5 hag 6,7 DP Transdurer DP 028 -M:+M kPa 0 25 % is TSD044 bgg 6. 7 1ower heades . sube SR. elevstum e 1 - -- -- - . - - - .. . ._
1 A. 2 4 ona il Ciaiy mmt in Imc lim emm 1%ni mie Span mu Au ur ao Silfi mk id e i II. g g imin ument inr
'9 ll:BE BUSill E MillWI E I (H) lherminouple K IW Halla 0 . 2t N) T +/ 1.8 T TOK l21 Figg 1, i l l (/1 Tube 8Q elevalum f ms wall Tube SQ clevstumi 3. eit m all thenmanuple K TW BM4e 0 2m T +1II T K K122 Fiat 1. I I %
Tube 80 elevatum g. me w all Therminuuple K TW BM4s 0:200 T +/ II T TCK121 Fin 1.II y lhenmrouple K 1W Bn45c 0 : 2t'X) T +11I T KK124 Figg 1, I l T Tube SQ elevatum h ess = all Tube SQ elevatavi h m w all Thenmanuple K IW Bn45i 0:200 T +/ I I T TCKl25 Fin 1.11 Thermirouple K TW B046c 0 : 200 T +1 1.1 T TCKl26 Figa 1.Il 3 Tube 80 elevaimm i . e nt m all - Tube SQ elevstum a , mi =all Therm <nouple K TW Bat 6 0 : 200 T +11I T TCK127 Figa 1.II DP Transducer DP014 . u : + 14 kPs 0 25 % i s TSDGli Figg 2,1 - - Tube 3R. elevseem c - low er header Tube 3 A. angular oss 1. X du,el g Ac cclatuncier VB R001 0 :500 g 0 02 g ACITU7 Fin 8.10 Tube 5 A. angular pis 5. Y de. el a Act elcre encier VB BfXf2 0:500 _g 0 02 g ACG08 Figg 8.10 Tube 7 A. angular em 3. X de. el g Au eleneneter VB B001 0 : 500 g 0 02 g ACOMN Fin 8.10 Tube 7 A. angular paa 5. Y dar, el g Au clerinneter VB nons 0:500 g o 02 g ACGIO Figg 8.10 g p Tube iB. angular pn 7. X dar.el a Accclainneier VB B005 0:500 g 0 02 g ACGIl Figg 8. 9 g X Tube IB. angular en 5. Y da.cl g Ac c clauwneier VR B006 0:500 a 0 02 g A(TD B 2 Fegg 8. 9 % l Tube iR. angular en 7. X dir el a Au ctenancier VR B007 0:500 g 0 02 g ACOll) Figg 8. 9 3
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Tube 1R. angular en 5. Y dir el a Au claseneter VR B00R 0:500 g o 02 g Acrol4 Fin 8. 9 Au cleriencier VB B(MN O:500 g 0 02 g ACY DIS Fin 8,10 Tube 85. angular p.s 1. X Jer, el g Auelenuncier VB Bolo o : 500 g 0 02 g AC G l6 Figg 8.10 Tube 85 angular pos 5. Y de .el n Tube ST. emir . ci e angular swn I k rde mark DX B Ism mm Fin 8.10 _.__. DX R 2am mm Figg 8. 9 Tube IS. cats , el n. angular pu 7 Side mari Scribe mari DX-B-3sm mm Fing 8,9 Tube 3 A. cit , el a. angular em 7 Tube S A, catr , el e, anguiu paa 3 Tube 7 A el s. angular pia 5 Stran gage Siram aage DX.8001 DX-8002
+/- 0 5 %
+/- 0 5 %
mm/mm mm/ men
*/ 5 % m v.
+ /. 5 % m v-SG091 SOM4 Figg 8,30 Fin 8.10 o
{ Sien.n gage DX B003 +/. 0 5 % mm/mm +/- 5 % m v 5G095 Figg 8.10 Tube 7 A, ents , el a angular pas i -- Stram gage DX B004 +/- 0 5 % mm/mm +/- 5 % m v S0096 Figg 8. 9 Tube IB. enir . el a. angular pm 7 Saram sage DX B005 +/- 0 5 % mm/mm +/- 5 % m v. SG097 Frag 8.9 Tube IR. emir , el a. angutar en 7 5 Siram gage DX - B006 +/- 0 5 % mm/mm +/. 5 % m v. SG098 Figg 8.9 - Tute IR. el s. angular en 5 " Tube 85.ents .el s angular paa 3 Siratn gage DX B007 +/- 0 5 % man /mm +/- 5 % m v. 5G099 Figg 8,10 h DX B008 +/- 0 5 % mm/mm +/- 5 % m v. 50800 Figg 8,9 Tube IR. eats ,el B. angular em 7 Stiman game Siram gage DX BalN +/- 05% mm/mrn +/- 5 % m v. 50101 Figg 8.10 _ _ Tube 5 A.cl I. angular pn.1 Sarmin gage DX BOIO +/- 0 5 % mm/mrn +/- 5 % m v. 50802 Figg 8. IO Tube 85 ents , cl.1. angular em 1 TUBE BUNDI.E MODUI.E 2 (El g Tube iR.el n. est. = all. angular pn. 7 Thenmrnuple K TW FJnol 0 : 200 T +/-1 I T KK216 Figg 7.12 U2 TW B002 0 : 200 T +/ I I T KK237 Figg 7.12 Tube IR.cl f.ent well, angular pas 7 1herm<rouNe K Thermocouple K TW B001 0:2m T +/- 1 I 'C TCK218 Figg 7,12 Tube S A, el a,cas well. angular pna 1 Thenmrtmaple K TW B004 0 : 200 T +1II T TCK219 Figg 7.12 Tube 5 A, el I, eas wall, angular pos 3 Tube 85, el s. eai wall, angular om i lhermiruupic K TW B005 0 : 200 T +/II T TCK240 Fin 7.12 TW E4106 0: 200 T +/ I IT TCK241 Fig 1, i 2 Tube BS el 1. eut =all. angular p.1 _, Therm <rnople K l
lh2 timi d Gunpuwniiu luse lm.nism in,se uncni type limi sale Span mu Ait ur y SIEl m ne lhi lN g , S Il att BilNill E Mullt'l I. I (14 g Tube 4 A elevatem i.ent m all nenma.mi dc K Iw lio25e u : 200 T +111 T 1CKtEl bra i ll_ henmuuuple K TW B025: 0:2m T +11I T TCK085 baa 1.11 f t/) Tube 4 A elev atse f. ine w all Tube 4 A ctevetum a ese well h muumpicK IW B026e 0: 200 *C +/ II T K K086 TCK087 has 1. ll Fina 3. Ii h Tube 4 A eleveien s. int m all knmuuuple K TW B026: 0:200 T +11I T _ . -l Thenmuuuptc K TW B027e 0 : 200 *C +/ I I T TCK088 Fina 1.13 3 Tube 4A cteveiac h. cat well Tube 4 A cteveiun h. int w ell Nnwrouptc K 1 W B027i 0: 200 T +1 l.l T TCK089 Fina 1.11 ] Wnmrimple K TW R028e 0:200 T +/ 11 T TCK090 Fins 1.11 i Tube 4 A elevaihm i. ent w ell ~ Tule 4 A elevstum i. ine = all hennmoupleK T W B0286 0:200 *C +1 1.1 *C TCKWl has 1. II Thenmwouple K TW B029e 0 : 200 T +/-tI T TCK092 has 1. II - - Tube SQ elevetum e.cs w ell Tube SQ elevesem e, int =all The....w.aple K TW B029. 0 : 200 *C +I 1 I T KKW3 han 1. Il hennmouple K TWBoloe_ 0:200 *C + / 1.8 *C TCKIN4 Fina 1.Il Tube 50 elevstum b. eat = all Wnnmouple K TW BOV. 0: 200 *C +/-1I *C KK095 Fina 1. Il Tube 50 elevstum b. int wall Tube 5Q eleveikm c. cat well nenmxouple K TW Rolle 0:200 T +1 l I *C TCK096 Fina 1.88 8 p
*C + /- 1.1 *C K K097 has 3.II @ M Tube SQ elev naum c. int =all nennmouple K TW BolIi 0 : 200 Tube 50 elevetum J. eat = ell Thenmsw,k K TW B012e 0 : 200 *C + /-- 1 I *C TCKU98 Fina 3 II 5 h Tube 50 ele,eine J. me wall knmrouple K TW B012e 0 : 200 T + / 1.1 *C TCK099 has 3. II ~3 ~$
Thenmrouple K TW-Bolle 0: 200 *C +/-1I *C K K100 has 1. II Tube 50 eleveaum e. cut = all Thenmsuuple K TW Bolle 0 : 200 *C +/- 1 I T TCKlot has 3. Il Tube SQ elevaise c. me = all Tube 50 eleveike f est wall Thenmrouple K TW Bon 4e 0:200 T +/- 1 I T TCK102 _ han 3. Il has 3.18 4 nenmre k K TW-80146 0 : 200 *C + /- 1 I *C TCK101 _ _ Tube SQ elev esnm f. int =all nenmue ,k K TW-9015e 0: 200 T +/ 1.1 *C KK104 Fina 3.II Tube 50 elevaikm a. eat =all TCK105 Fina 3.Il nenouxc_;'.: K TW-90156 0 : 200 *C +/-1.1 *C Tube SQ clevethm a me wall = 'E Tube 50 clevatum h.ent well Thenmrouple K TW-Bo %e 0 : 200 T +/- I.I T TCK106 Fina 3.11
- Th... e ;k K TW-2036i 0:200 T +/ I I *C TCK107 Fina 3.Il Tube 50 elevstum h. ine = all Thenmxcuple K TW-8037c 0: 200 *C + /- 1 I *C TEKIOS Fian 3.11 Tube SQ elevetum i , ent w ell Thenmu, *; K TW-9017: 0:200 *C = /- I .1 *C TCK109 Fina 3. II Tube 50 elevstum 6. me =all TCKilo Fina 1.11 Thennaimpic K .T W-B018e 0 : 200 *C + /- 1.1 *C Tube 80 eleverum e.ent well TCKli t has 3. Il '
Thenwrimple K TW B018 0:200 T +/-1.1 *C " Tube SQ elev stem a. inn. =all TCKl12 Fina 3.11 Thenmwimpic K TW B019e 0 : 200 *C + / - 1.1 *C Tulw SQ clevenumI eat wall KKII) han 3.11 Thenmrimple K TW B019i 0 : 200 *C +/- 1.1 *C Tube SQ elevenum b. int =all nenmwi ;'. K TW-3040e 0: 200 T +/-1.1 *C TCK114 Fina 3.II - - Tube SQ cleveske e,eit = Il knmsimple K TW B040i 0 : 200 *C +/- 1 I T TCKI15 Fias 3. II Tube SQ elev enum c. mt. wall n eniinc -,k K TW 9041e 0:200 *C + /- l . l *C TCKil6 Fina 3. 8 8 ,, Tube 80 eleveeme d. cat well Thennix-- f- K TW B04ti 0 : 200 T + /- 1.1 T - TCK117 Fina 3.Il M I. Tube SQ eleveamm d. inn. w mit Thenmruuple K TW.8042e 0 : 200 *C * /- I . I *C TCKIls Fina. 3. Il Tube SQ elevetum e est = ell Tube SQ elevetum e, int. .all Tha-o,:e K 1W-90426 0 : 200 T + / l .1 "C TCK119 Fina 3. Il __ Thenwrnucle K TW B041e . 0 : 200 T +/- I I *C TCK 820 Fina 3. Il Tube SQ clevetum f. est = ell I
Iab 2 Camid A t-Inwirmnent type 1%nt unic Span mu Auur an SILT unk HeiD*g g Cisnpiment or ime 1 = aJum f (f3 116t 41N I INE (t;;5) F irst kngth, mal I. (upper header / tar ll) DP Temmuuter D1' 019 0: 50 kPa 0 25 % f 0 25 % fi TMDl65 1M Dl57 oti2tPJDIN l fr>209DD91 q First kngth, rmd 2,(urper header / tan C) DP Transmitte: DP 020 0:50 kPa Ihcimempic K T Sml 0: 2m T +/.II T KK018 Fig 15 [ lin&v Tce tuni (umumm length, pna S A) , Thenmsouple K TSW2 0: 200 T */ I I T TCK019 (M1209DfN l S { CT inlet sectan C4=nmem tenght DP Transmater DP 029 0 : Im k Pa 05%ie TMD156 00209 DIN) { f 0l:10 MPa 0 25 % i s 1M A010 Fig 15 Tee umjurutum tunnm<m length. p s i A) P Transmitter P 5001 in=ct hen &r mal I umi (ang p s l} S(sibe maA DX G ism mm Iin IS -. - DX G 2sm mm Fig 15 Inwet hea&t ad I omi (ang p s 7) Soibe maA DX CODI +/ 0 5 % mm/mm +/ 5%mv SGil6 bg 15 In*er hen &v ad I ami (ang pns l) Sira n asse DX C402 +/ 05 % mm/mm */ 5 % m v. 5G117 bg 15 inwer hen &v rmal I ami (ang pos 1) Sir aan gage VEN T LINE M) Fig 45 Thenmanupic K i6n01 0: 2m T +/II T KK 040 Under Tee umimmine (pn 6A) VT mlet sc< sum Thermaounde K T 6002 0: 200 C +/ 1I T KK041 (U209 DIN I y l in=cr leeder m.4 1 - Tee esmiurnium DP Transmates DP Ull 0: Im kPa 0 25 % f e 1MDl85 00209 DIN) 3
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DP Teansmdier DP 022 0 :100 kPa 0 25 % f s IMDl84 00209 DIN L l 1ower header ud 2 Tec umiurmium m2tWDin t DP Transmnier DP040 0 :60 kPa 0 5 % i s. TMDON Ca nnm<m icrig sh DP023 0 : 50 kPa 0 25 % f s 1MDig ! Or2mDis t VT anlet settum Vent iank DP Transmaier NON CONDEMllit,E IM ET 1,5NE (2) - '~ Thenmut=pk K T-2till 0: 200 *C */-1I T TCKG42 Mt209DtW I tbwnstream mhe TM A01) m1209 DIN 3 P-Teansmeter P 2001 0:1 MPa 0 25 % i e tipstream or fke Onfice - DP F 2001 0 : 200 kPa i % i s. TMDol7 (X1209 DEMI o F* thsh flootste mensmement devue TMD025 002&JDIM) Onrne - DP F 2002 0:100 kPa 0 25 % i e inw 00=vair meesseement devue STEAM INI ET 3.INE (l) KK001 002fNDIN) (be nstre nm mhe Thenmuuuple K T itr)l 0: 5fX) T +/- 2 T P 1001 0 1: 20 i MPs 0 25 % f a TMR077 00209DD91 Upstream or Ne P Tiansminer N F Init 0 : 700 kPa 015 % i e TMD028 00209DD91 , High flomvate measuremens devnt Onfice DP
- Onfice - DP F 1001 0 : 100 kPa 0 25 % f a TMD007 00209DD9) $
Meshum flows sie measuremens devn e 00209DD91 Onlice - DP F 1001 0:10 kPa 0.25 % fa TMDl71 tow flowrote measurernent devier 00209DD91 Desuperheating ime (=ater temperature) Thermmwe re 4 T 3001 0: 150 T +/ 1. I T TCK011 _ _ F 3001 0 : Ifn kPa 0 25 % i s TMD006 00209DD91 Desupertwatmg Ime Vennui - DP PCC POOt. (P) Fig 16 y 2 DP Teansmitter DP in)I O : 30 kPa 0 25 % f a TMDI58 inc. F6,isp ekvata m 5650 - 3220 mm (1) i 0 : 30 kPa 0 5 % f s. TMDl78 Fig 16 Enc. F6, tap cleveram 5025 3220 mm til DP Transmitter DP M12 0 :50 kPa 0 25 % i s TMDI76 Fig 16 inc F6, tap ekvstam 3220 Somm(1) DP Trerumster DP M13 __ 0: 35 kPa 0 25 % f s IMDis t Fig 16 inc. F6, tar ekv eiam 3220 - 1945 mm ti) DP Teansmitter DP Ime 0:10 kPa 0 5 % i s. TM Dl69 Fig 16 Loc. F6, tap ekvatam 1945 1125 mm (1) DP Transmities DP P005 0 :35 kPa 05%fs TMDIE2 bg 16 lue F6. top ekvatam il25 50 mm (5) DP Transmater DP lu)6 t___ _ _ _ _ _ _ __.______ _ _ _
e n 5 fh2 remind Pimis mic Sgun in u Au ura) Sli.T sed Iki l 8* g Cannemcialis ime haene inmumes.s tnw a 18:14E HU.N DI E Molll11 E I F p l DP h anwha en DPOl6 -M:*R kPa 1125 'A f s. 15tM44 m2tnDIN S Upper - kmer header E U2 LOWER HEADFR Malp08.E I W) Near ba k cover Dante. cit. Dos C. sup (*) nemuaouple K 1W 001 0: 200 *C +/ I I T TCK2N) Fig l) Near buk tove nante, esi .pm C.ini(*) Thermmouple K IW OX12 0: 200 *C +/ l .l *C TCK261 Fin l) _ .-{ fnet cover. cenual nutum (*) 1hermmouple K IW OXII 0 : 200 T +1 1 I *C TCK262 Fin il Fluid temperature. poi D.(bak sale) Therm <wouple K T GUI O 21 0 *C */ I I *C KK015 Fia 13 ,, Fluid temocrature. na I,(inme side) Thermornuple K T CtH2 0 : 200 *C +1 I I *C KK016 Fes il ~5 DP Transmitter DP017 0: 50- k Pa 0 25 % i s. TMD364 00209tXWl tmer header deem ime (first lenath) Therm <xouple K TW CR001 0 : 200 *C +/- t I *C TUK 242 Fia 11 - - F cover tvde , pn I (*) y> Thermocouple K TW CB002 0: 200 T +/- 1.1 "C TCK2 5 i Fin 13 Fruns cover tels , pos 2 (*) Frontc m cr h h ip n 3 (*) Thermem.m.:e K TW CB005 0: 200 *C +/- I l *C KK244 Fia lI DX 0711 +105% mm/mm ./ 5 % m v. SGIO) Fia il _ Near bu k Hanse. esi . sup . at. diresinm Sirun ante Near bac k nanae. est , sur . cu direstinn Sirain anse DX GXf2 +/ 05% mm/mm +/. 5 % m v. SGIG8 Fez ll . p
+/- 5 % m v. SG105 Fin Il M DX G10) +/- 0 5 % mm/mm Near hack Hanse. eat . int . an darromm Nc a huk Hanse ent .ini .cu direciam Seeam ante Stra n saae DX C004~ +/ 0 5 % mm/mm +/- 5 % m v. SG106 Fin 13- 5 l >
Front cover, censtal en , ens . X der Sirain anse DX-nu15 +/- 0 5 % mm/mm +/- 5 % m v. SGIO7 Fin I3 3~ 3
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Front cover. s eneral pu , est . Z die Straan asse DX GX1h +/05% mm/mm +/ 5 % m v. SGlos Fin Il DX CR001 +/05% mm/mm +/ 5 % m v. SGl09 Fia 11 Fuma cover h>li l en E Sirun saae DX CR002 +/. 0 5 % mm/mm + /- 5 % m v. 5G110 ha il Front cmcr tulo 1.pis I Slima anae Fnet ever het 2.pm E Siraan anae DX 0900) +/- 0 5 % mm/mm +/ 5 % m v. SGill Fia II ._._ Fome cmcr hdi 2. pn i Siresa anse DX C8004 */05% mm/mm +/. 5 % m v. SGil2 Fia il DX Cson5 +/ 0 5 % mm/mm +/ 5 % m v. SGill Fez 11 Fnes cover hile 3, n.s E Siraan anae a f* 1 OWER HEADER MODUl.E 2 (F) Fluid ternpersture (bank sideL pn. D lhernuruuple K THUI o:200 *C +/ 1I *C TCKoli Fia 14 . Therm <xuuple K - TW M101 0 : 200 *C +1 I .1 *C TCK261 Fia 14 Near buk Hanse.cai, anauter pn I (*) ~~ Neer bath flanne est , anaular pn 5 (*) Thermmouple K TW lui? 0: 200 *C +1.I1 *C TCK2M Fia 14 DP 018 0:50 kPa 0 25 % f a TMD161 tu2090091 ' tower header , desin hne (fint lenath) DP Teanimister
- PCC SUPPORTS (S)
- Themumuuple K TW Sinit 0 : 200 *C +/- 1.1 *C K K265 Fia i1 Supprt St. riahn inte (* )
Suppwt St. left ude (* ) Therm <xouple K TW S0021 0:200 *C +/-1I *C KK266 Fia 13 LVDT 0: 2 mm +/- 0 5 % f s EDTD04 Fia 13 But suppet Y derestion _ PO S008 Prtet -..--;. Y duccine LVDT PD SOf12 0:2 mm +/. 0.5 % f s. LDTUQ5 Fia il Supptwt St.Z dir , kit side Sirman anae DX 5001 +/-0 5 % =J.._-. +/- 5 % m v- SGil4 Fia il ,, 2, S .. ;St.Z du ,nahe side Stram anae DX-5002 +/-0 5 % =Ax +/ 5 % m v. SGil5 Fia Il tj DR AIN LINE (G;5) Thermmouple K TW GUDI O:200 *C +/-1.1 *C TCK267 Fia 85 __ Inlet sectum, est , anauter pc. I (*) inlet sectum. est , anauter on 1 (*) Thermample K TW 0002 0:200 *C */ I I *C TCK268 Fim 15
'? , % , - -.c vi w - s e v
- s e %.- , . - . . . + , . ~ < * . - - -
14 1 nua d mu Au ur a y $11 1 unic W I D* g Inumment type l'Imt u nk Span 4 Gannment in ime km.atum P W P o ol. (P) *C 105 *C TRfM t hg 17 l a atum t)) elev atum 38to mm 0) RTulqlm -Tim 6 0: ISO Fig 17 (A RTU lil(I) T I4117 0 : ISO *C l 05 T TR042 incaske El Incethm F3 elevstum 1810 mm (1) clevstum 1sto mm (5) RTU liian Tims 0:150 *C I 05 *C TRo41 Fer 17 h
.-j RTU lil00 T ITM0 0 : 150 *C 10$ T TR044 Fez 17 Laetion ll) elevatinn 3810 mm (1) 105 *C TR045 Fig 17 Lncathml) elev atkm 3Sl0mm (1) RTU PTIGO TIMMI 0:150 *C
*C 105 T TR046 Feg 17 elevnaam 1880 mm (1) RTU lil00 TitM2 0 :150 ,
Laathm l_) I 05 *C TR047 bg 17 g tmstum A6 e lev at = = 2155 mm (1) RID lil00 TIMM) 0:150 T - T IY44 0:150 *C I 05 *C TRott ha 17 imatkm B6 elevstum 2155 mm (1) RTV ITIOD Feg 17 - - T 1985 0: ISO *C t 05 *C TR049 locatkm C6 clevstum 2155 mm (1) RTD 14100 0:150 *C I 05 *C TRQ50 Fes 17 tecatum D6 elevatum 2155 mm (1) RTU Pfl00 TlYM6 0: ISO *C I 05 *C TROSI Fra 17 Lastke E6 elevatum 2135 mm ($) RID I4100 TIMM7 T 1.05 *C TR052 Fig 17 RTV PTl00 T P(M8 0 : 150 Locatke F6 clevatum 2155 mm (1) T I 05 *C TROS) Feg 17 3 9 RTD Ptiff) TIMM9 0:150 incatkm G6 - clevatum 2155 mm (5) Timo 0:150 *C 105 *C TR054 For 17 3 X incatkm 546 elevaimm 2355 mm (1) RTD PTIOD Fig 17 4 h 0 :150 *C 105 T 1R055 RTU PTitn T ITMI t ecatkm 16 . elevatum 2155 mm (1) T itr52 0 150 *C 105 T TR056 ha 17 3 3 l ocatum 16 elevatum 2155 mm (1) RTD FT100 Fig 17
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T Itri1 0:150 *C I 05 *C TR057 Lcutum DS elevslum 5650 mm (5) R TD I4100 Fig 17 0: ISO T I 05 *C TRoss Incstum D3 elevatum 5025 ram ($) RTD filun T lt)S4 TR059 Fig 17 TItn5 0: ISO *C I 05 *C La aikm Cl elevstum 2765 mm (5) RTV I4800 0:150 *C l 05 *C TR060 For 17 RTD PTICO T ITl56 incethm C2 - elevstum 2765 mm (1) 0 : Iy) *C I 05 *C TR061 Fig 17 Im atkm C 3 - elev eimm 2765 mm (1) RTU PTIGO T.ft157
*C I05*C TR062 Fig 17 RTV PTIOD T-lyt 58 0:150 Incatum DS - eleverum 525mm (1)
L ft101 0:50 kPa 0 25 % i s TMD019 0020DtW) o f Tap clevatum 5025 - 18 25 mm (5) OP - Tr ansmktet TUK N*, 00210DD9) Thenn-Ne K T MODI 0: ISO *C +/- 1 I *C Make-up Ime TMDol5 002100091 GilDo DP F Mn01 0:100 hPa 0.250 % i s -- Make up tee TCK195 - 00210DD9) Thermanuele K T R(UI O : 200 *C +/ 1.1 *C Discherse Ice 0 :10 kPa 0 25 % i s. TMDl?7 002 0DD91 GelHo DP F R001 Discherse ime 00209DD91 s. IC lent inwee umnettma ime ThermanuNe K T N001 0: ISO *C +/- 1.1 *C TOK045 ~ [4 IC P(M)t, (Q) 002fMDtW1 0:50 kPa 0 25 % f s TMD019 Tap elevatum 5l40 - 1440 mm 0) DP Transmitter 1. Qmi 0 :20 kPa 0 25 % fs. TMD009 00209DD9) -- Tap elevatum 3140 - 1420 mm (5) Dr . Transmitter L Q002 CONDENSATE TANK (t.) T +/- l .1 *C TOK046 00209DD93 ,, Thenna ouple K T LD1I 0 : 200 Devatum 4(M0 mm (f) T +/- 1.1 *C TOK047 002090093 lj % Thermmouple K T I312 0:200 Elevstum 3545 mm (() *C +/ 1.1 *C TUK(M8 00209DD9) Thermanuple K T 1I101 0: 200 Devatum 1500 mm (f) *C +/- 1 I *C TOK049 00209DD9) Thermace K T-IIl04 0:200 __ Phv. 388 mm (f) 0:100 kPa 0 5 % i s. TMD003 00209DIMl_ DP Transmkver DP025 Comnensaie tank - Vent tank 0 5 % f s. TMDn02 002MDD91 DP Teansmitter 1 1D01 0 :100 kPa 6* drw harge lme
- . .. . . ~ - , _ - - - - . -
l 1 I ai. 2 C.. unit _ mu Anus ay SllTu nc NelDmg Inmumtut aux 1%a unic Spas , C. ntu wususImcl.uimm S g Pcc Penn. m
- DP Tiensmnie: D6' l407 0: 10 kPa 0 25 % f 5 TMDl ?5 ha lh la ll6. top elevetum S6Hl .1220 mm t%) lhlDl61 ha16 I (/)
DPim8 0 :20 kre 0 25 % f s law H6.sapelevetum 1231 1945 nm t%) la. H6. iep elev ntmas IM5 Il15 mm (5) DP Teensmitier DP Trenimitter DP l41N 0 ;10 kre 0 25 8E f a TMDl72 Fes 16 h ; i DP 1910 0 : 20 kPe 0 25 % ( s. 1M Dl94 ha 16 m-{ Im. H6. ter elevoimm 1125 50mm(1) DP Tiensmieter 1 0: 150 T I 05 *C TR006 ha i7 [ Imetum 81. elevetum 2765 mm (5) RID PT100 Tlint 0:150 T I 05 T TR007 ha I? Y t am etim 81 cIcvesum 2355 mm (%) elevenu tN5 mm (5) R IU PT100 RTD PT100 Tlin2 T Rn1 0 :150 *C I OS T 1R(D8 Fes 17 !
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l_m etim B 1 I 05 T TRfRN ha 17 RTVfTim T Rol 0: 150 T taetum B 1 eleveum 1515 mm (1) 8 05 *C 1R010 Fia 17
--'4 RTD Pil00 Titni 0:150 *C la atim B ) eleveaum il25 mm (5) I 05 T Troll ha 17 RTU 17100 T ltin6 0:150 T ; l au stum D1 elevoimm 2765 mm (1) I 05 T Trol 2 Fit 17 R TD Prim TItn7 0:150 T lastum Di elevoimm 2355 mm (1) 0:150 T I 05 T 17013 ha17 RTDPTim TlYns 1 m otim D 3 elevaism 1945 mm (1) eleveemm 1515 mm (1) RTD ITIOD T1109 0:150 *C 105*C 1ROI4 ha 17 $ p M 1 <x etwm D) 0:150 *C I 05 T TROIS ha 17 3 RTU Pfluo T 1980 1 m etum D) elevetum 1825 mm (1)
T IUll O: 150 *C I 05 *C 1Rol6 ha 17 $ h t oc stum DS - eleveime 2765 mm (1) R TD ITI(n 3 elevoimm 2155 mm (1) R1D PTi(U T rol2 0 :150 T 105 T TRolf ha 17 3 t urnium D5 T I 05 *C TR018 ha 17 RTV PT100 T R18 ) 0: 90 I m eine D5 ele'es== 1945 mm (5) *C I 05 T 1* 089 ha 17 RTD PTIfn T lill4 0: ISO Imetim D5 elevoimm 1515 mm (1) I05*C TR020 ha 17 RfD PT100 T R115 0:150 *C lamine D5 eleveten 1825 mm (1) *C I 05 T 1R028 ha i 7 _._ elevetum 2765 mm (5) RTV PTIGO T Inte 0:150 I su sum F5 0:150 T I 05 T TR022 ha 17 elevetum 2355 mm (1) R fD ITIGO T R)l7 l awsum F 5 0: ISO *C I05 T T102) ha 17 RTV Fil00 T 0018 o f 1 <x sim F 5 - clevetum 1945 mm (1) 0:150 *C I 05 *C TR024 ha 17
- elevwum 1535 mm (1) RTD PT100 T R119 ta mitm F 5 0 :150 T I 05 T TROIS ha 17 eleveaum 1125 mm (1) RTD PT100 T#020 la asian F 5 0 :150 T B OS T TR026 ha 17 elevetum S650 mm (1) RTD ITIOD T M721 ~~
la sim G) 0:150 T I OS *C 11027 ha l? elevetmn 5025 mm (1) RTD FTifU T P022 lu eewm O1 0:150 *C I 05 *C TR028 Fra 17 elevetum 1810 mm ($) RTV PTI(D T P023 l a enum G1 0: ISO T I 05 T 13029 ha i7 g 1 su atum G1 elevstum 1220 mm (1) RTD PT100 T.R724 T1925 0:350 T I 05 *C TRO10 Fia 17 k'
- tu ntum G 3 elevetum 2765 mm (5) RTD ITIOD Fia 17 0:150 *C I OS *C 1R03 elevetum 2355 mm (1) RTDITIOD T-R726 t a neum G1 0:850 *C I 05 *C TRO12 Fia 17 --
elevmunn 1945 mm (1) R TD ITIfD T R127 ta etmn G1 0:150 *C I 05 T TRO)) F a 17 , elevetum 1535 mm ($) RTD PTIOD T F028 ta ntiosi G1 0:150 T I05*C 1R014 Fin 17 ,a T R729 Laesum G) elevetum 1925 mm (1) RTD IT100 T RHO 0 : 150 T I 05 T ~ TR035 Fin 17 ME elevetsnn 670 mm (1) RTD PT100 l_sxetism G1 O:150 T I05 T TR036 ha 17 elevasem 525 mm (1) RTD ITICO T IUII tamiani 03 0 :150 *C 105 T TRO17 Fia 17 elevetum 50 mm (1) RTD Pil00 T-MH2 tweaum n) 0 :150 - T I05*C 1R018 Fra 17 elevetum 5810mm (5) RTU PT100 T P011 tweaum A3 0 : 150 T I 05 T TR019 Fin 17 elevetum 1810 mm (1) RTD PTtte T P014 tuotum 81 T IU15 0:150 *C l oi *C TRfwo fia 17 I m etum C) elevetum 1810 mm (1) RTU PTifn _ _ _ . . _ . . _. - m _ .. _ _ . _ _ _ _ _ . . _ . __ _ . _ . _ _ _- ._.__._.x.__. .a
J G e 1 I.OCATION D d a FI,tilp i tri TAG TYPE (mm) (mm) (m') kd Non condensible inlet ime 102.26 24.2 3.8038 E44 ' AIR F-2001 ORIFICE F-2002 ORIFICE Non condensible inlet line 26 44 7 3.2618 E 05 AIR j Steam inlet Lme 66 65 42.1 1.3053 E-03 51EAM F 1001 ORIFICE ORIFICE Vent Tank Mixtuie Diwharge Line 128.2 94.7 7.2220 E-03 STEAM AIR F-TUDI Vent Tank Mixture Discharge Line 51.5 13.2 1.1579 E 44 511iAM - AIR am g F-1D02 ORIFICE 1_ : _ 24.3 7.8 6.68 E415 WAT1iR F 3001 VENTURI Desupesheating Line GILI10 Condensate Tank Discharge Line 102.26 // M=4.795515E-7(*) ' WAlliR _ F.11101 K=1.494639E-4 i 102.26 // M=4.909911E-7(*) WAlliR , , F-M001 - GILf10 Poots make-up ime I K=9.98417E-6 l
// M=4.916536E-7(*) WA'iliR 7 -R(Xil GILFLO Pools dncharge Ime - 102.26 --
K=3.51008E e I j (*) M (m'!(s'Pa) L K (m h) calibration coats D = tube inside diameter -_ d = thmal diameter ' n = calitwated or calculated llus coelficient l ' Tab.3 - PANTilERS-PCC FLOWMETER DEVICES CHARACTERISTICS v e
+._-.~.-m _ .. . , - --.4 . - - - s -- - = -
s r e i." ,w ,- * *- - .- - - ev e - ---==2a---m-- u =---- -- --
I at, a 'oiit J mu Sill u=k Kt thg g C.uigwwni us lux tim an.m insin> mens i> pe thosu=k Sp.ui As um .m > CONDI Ns AIE I An (I.) 0 25 % i a TMD166 m3NDINI E t/) Tap elevaine 4NO - 1800 mm (1) DP le ansminer 1.11n12 0: 50 k Pa 4* dm harge line Vennin DP F1101 0: 15 kPa 0 25 % i s TMD026 m2mDtW) 00209DLW1 DP Transminer DP 024 0:100 kPa 0 5 % f: TMD010 _ { Ctwalensate tank uppen ht aJer mi=1 1 T105 0 : 2fD T +/ 1 I T K K050 m209DD91 g Dmharge line (nuid temperature) Themurmiple K CT gas spue P Tsanunuter P tIril o:1 MPs 0 25 % i: TMAfRW 002mD(W) ] VENI I A.% (1) ~{ Themumouple K T lin): 0: 2m T +/- 1 I T TCK051 to2mDINI Elevatum 6106 mm (f) TOK052 m2mDtW1 - - -- Themurouple K T l(X72 0: 21s> T +/ II T Elevatum 1228 mm (f) KK05) an2099twl Thermixouple K Timi 0 : 200 T +/ II T Elevatum 570 mm (1) TCKOM (U209DD91 A utwaruw dm hange ime (tank sop) Thermiumple K T TYVI 0:2f0 T +/ 1I T 1 Iml 0: 20 kPa 0 25 4 f s TMD005 m209DINI Tap elevatum 3228 - 570mm (f! DP Transmitter VT aas spate P Transmetser P1001 0:IO MPs 0 25 % is. DtA0li 00209 DIN ) 3 p P T101 0:1 MPa 0 25 % i s TMA012 002090tM1 S M P-Te ansmnter Av / Vapw .h iharge law Onftee - DP F-TIUt 0:100 KPa 0 25 % i s TMD027 00209 DIN I 4 $ Air / Vape dmharge hne (high Gomeate) Onfke ' DP F Tu12 0:to kPa 0 5 % is utDl70 002090lMi 3~ 3
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Aw I Vape Jmharge hne (Io= Dowsnie) CA Kl1 TA M (On kPa 0 25 % i s TMDl67 m3notNi DP 1:ansmitier L 4Mol 0:50 I~ap elevatum 1910 - 610 mm (f) STE AM ElVPASS 11NE (7) m2tNDtN I P7ml O : 20 MPa 0 25 % f s __ _. Swam tmpass Imc P Tearummer 00209DD9) T 7001 0:400 T ,/ I I T Stcam twpass im Therm <rouple K M AIN DL511PERilE A11NG 1INE (N) 0: 25 MPs 0 25 % i a tut 2iNDIN I o f Mam desuperhe aime line P Transminer P8(ol 1 Abbrntanlim dir. = darcation ang = angular (*) Ctengwn.atum dwinusouple los met hann ai nwasuit ment e lett. = cate:nal a / mt. = micrnal smaj = trumlule pin a ymtam y til Licsatom is tcri(J in the t=dioen el ICC us IC p=.1 I sup = supesmir g = gravsty suelerainwa (i) Ejes atawi scismd to alw tank matinallottom mi = inferum f s. = futt uale et. = atial mu = measurement umt } g str. = cmumferential m v. = measured value c str = etia ndan lis = lut atant mu = mir ados cl. = clevatam ____m.._..____..___..______ - . _ _ _ _ _ _ - _ _ ___._m___.-_.____ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ . _ _ _ _ _ - _ _ _ _ _ _ _ - _ _ _ _ _ _ - - _ - _ _ _ _ _ _ _ ._.._____m __.-__.1____._ ___m__.:___ _ _ _ . _ _ _ _ _ _ _ _ . - - _ _ _ _ . _ . _ _ _ . _ _ .....__.__._u_
t Rev Page j of SIET l Doc""' _ _ !i . () 45 225 vznine Heatww1 Innovsirvi ! t r a%.["t91 ! 6.1.4 Condensate tanlL level control loop ne level in the condensate tank is controlled using a digital PID device to which are connected the level measurement signal as process vanable and a pneumatr valve. in.cened in the discharge ime, as actuator i de vice. 6.1.5 Pressure control loop in order to control the pressure inside the PCC plant two different control loop are foresca. One wdl te used in the steam-noncondensibile matrix tests and it consists of a digital PID electrome device with the inlet pressure value as praess vanable and a pneumate valve. insened in the Vent Tank discharge line as xtuator device. i 6.1.6 PCC poollevel controiloop The PCC tank level will be controlled usmg a digtal PID device with the level as process vanable and a pneumatic valve. insened m the pool discharge line, as actuator device. i l l I i 1
Da***** ' R*v Page of SIET l senone Reanon Irmvativi t 00098PPQI i 0 at 225
- 6. TEST PLANT CONTROLS AND SAFETY CONSIDERATIONS 6.1 Control sysican descripuons in order to perform the PCC cupenmental test seven control loops are foreseen. These control loops are provided in order to manage and regulate the key tests parameters. A main control board is foreseen to
.ontain the electronic controllers that will perform the operanons.
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6.1.1 Steam flowrate controlloop 'l The control of the steam flow. rate is performed usmg a digital PID electroruc controller to which are l j connected the steam onfice pressure drop instrument as process vanable and a pneumatac valve. tnserted in I the steam supply Ime, as actuator. The temperatusr and the pressure of the steam are used in order to adjust the engmeenng value of the flow rate.
- 6.1.2 Sieam.noncondensible nas inisture temperature control loup 1
-I The temperature of the steam.noncondensibile gas mixture will be controlled usmg a digital PID electroruc controller with the mixture temperature as process vanable and a pneumauc valve. inserted in the desuperheaung ime, as actuator.
- 6. lJ Air flowrate controlloop The control of the att flow. rate is perf ormed using a digital PID clectronic device to which are connected the air onfice pressure drop as process vanable and a pneumauc valve. insened in the atr supply liae sas as
.ictuator. The temperature and the pressure of the air are used in order to adjust the engineermg value of the air flow rate.
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6.2 %fety cons.derstmas l To assure the structural integnty of the PCC full scme prounvpe and to meet the design requirements of the Panthers PCC Components and prping the following safety valves are installed: ai F016 on steam air mixture supply line, set to high pressure signali1.0 MPa) N F050 on the ime connecting the mam noncondensible hne to the gas spre of the condensate tank, set to high pressure signal (1.0 MPs). a FtMO on the vent tank set to high pressure signal (1.0 MPa). I I I 4 ______.E________________' - _ _ _ _ _ r
Dac=a' R*' Page l or SIET I- l l
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1 0 f a7 225 secone Meanon innovssive n009RPP01 DATA ACQUISITION SYSTEM i I The data acquisioon and elaborauon system is designed to match all the needs to measure and handle { measured signals from the plant.' A supervisor computer provides a protected work area and the access is restncted to the authonzed users only. The large amount (4 the user opersoon are standardazed and f i collect m a set of software procedures to avoid errors and loss ofinformauon ! i j Hardware coefiguration The data acquissuon and elaboracon system consists of some components comp 6csely integrated in orter to maae the user able to perform all the significant acuon connected with the data acquisition and elaborsuon process. The ehematics in tref. 2.2.2) show the artt.ngements of PCC DATA ACQUISTT10N and ELABORATION system. It basically consist of four main central components: l l
- supervisory computer DEC VAX4000-200 graphics wortstation DEC VAXSTATION 2000 remote I/O dnver DEC MICROVAX 11 falc transler DOS device and of Iwo data logger subsystems:
digital data acquisiuon subsystem RTV AX 300 analogical magnetic tape recorder system HONEYWELL model.101 connected with a FFT syssem i HEWLETT PACKARD HPM67A) 9
D c"*"' R" l Pa l o' SIET ' l '
'iOO98PP91 0 i 4R I 225 'erxme Restm Innovarm 1 Se ornals coming from instruments are ended to the two data loggers by means of particular measurement cruins.
Ne -supervisory computer is a DEC V AXan:00 elaborator u nh the following features: CPU $ VUPS I contreuer DSS! 10 MIPS m RISC tecnology l ETHERNET controller 10 MIPS m RISC tecnology
- M Mbyte of RAM memory mass storage: I Gbyte of hard duk RF72 DEC 1.2 Gbyte removible cartndre T1204 DEC penpherals: : consolle 4 color video termtrul I pnnter DEC LA100 6 ommunication : 4 senal ports I intertsce adapter f or data acquisition subsystem CS 85RU 1 ETHERNET port
- he graphic wort.stauon is a DEC V AXSTATION 2000 claborator wnh the followmg features :
1 CPU n Mbyte of RAM memory 1 ETHERNET controller ; l i ll
Doe = ea' Rev Pate j of SIET I i l itoggppol o ao ' P.5 seuane Neanum Innovaim mass storage : 130 Mbyte of hard disk penpheraJs: 14* R floor color video XWINDOW termmal DEC VR290 The remote 1/0 dnver is a DEC MICROV AX 11 claborator with the fouowing features : ICPU
- 5 Mbyte of RAM memory i ETIERNET controller mass storage : 130 Mbyte of hard disk 90 Mbyte of hard disk 70 Mbyte tape streamer removible cartndge penpherajs : 4 wnal port 14" monochrome video (PC based computer + VT240 termmaj emulator softwares ne tile transf er elaborator is a DEC V AXMATE computer AT IBM compauble with the following !catures :
CPU A0286 i Mbyte of RAM memorv i floppy disk dnve high density 5"+1/4
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rad @RPP91 ! O i 50 :23 secone xewum leenvi l 1 4 sinual hard disk for a toul amount of 60 Mbyte ETHERNET contreuer I senal port i pnnter pon monochrome CGA l 8" sideo of " remote
- data logger Imked in a star The digital data acquisiuon subsystem RTVAX 300 es a set configurauon. by usmg a thin Ethernet cable.to the supervisory computer m which as mstalled a virtual central node. Every of this remote units has this main charactenstics:
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6 huffer memory i Mbyte , microprocessor card with 32 bit bus. 20 MHz ciock Ethernet controffer 10 Mbyte/s througput switch mode power hos 100 Hz maximum adjusuble samphng rate set of dau conditioning and amphfier card The analog data acquisition subsystem consists ut a magnetic tape analog recorder and a Fast Founer Transtorm system The HONEYWELL Model.101 Magnets Tape Record / Reproduce Portable System is a mulutrack record / reproduce system for recording and reproducmg data on magnets tape.The system uses FM rxtreproduce ciectronics which may he mixed to suit the requirements of the applicasson. The maan snaractenstics of this device are:
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Dac' R" Page j of SIET I I l l
,enone Resuw1 Innovanvi finoggppg] t 0 i 91 I 225
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1 input channels 24 inputlevel 0.5 + 10 V peat to peak with adjusting 4/. 40 %
-l mmimum mput inpedance !$ LD manmum input capacitance 10 pF operaung temperature 0 + 10 'C ,
l adjustable handwith DC + MO kHz 1 i TAPE SPEED 1 inches per j CES Itm FREQUENCY BANDWITH (kHzl c ond) I ikHis 120 1 432 i DC + 80 60 1 216 DC + 40 to i 108 DC + 20 15 1 54 DC + 10 l 7M i 27 DC + 5 'I 1% i I 3.5 DC + 2.5 Iw ! 6.75 DC + 1.25 15 / 16 i 1375 i DC + 0 625 j TheHP 3567A PC spectrum /networt analvter is a espandable FFT analyzers that characterize signals in hoth time and frequency domams. consists of a set of measurament hardware and signal processing software wich is on an IBM PC compatible computer. The measurarr,ent hardware is connect to the computer usmg an HP.lB (GPIB) mterface. The measurament hardware HP3567 A is of modular type consists of the HP35650A mamframe. HP35651B HP 1B / signal processor module. three HP35652A one channel input module nad the HP35653A source module 1or calibrauon. The signal processmg sof tware controls the measurarnent hardware and computer to make and display measurarnent. Its digitize and stores analog input signal: appbes extensive library of pre programmed an3Jvsts f uncuon to store data and display the signal and/or the processed miormation on the screen. It incorporates all of the features of: at high performance data acquasation and signalconditionmg system be microprocessor-controlled digital storage and analog /dtgatal display system
Document Reo Page or l l l SIET I on@HPP91 8 0 1 42 , 225
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l A non-mtatile siccare of waveform data. control setups and programs is possible with the floppy dask dnve l . ine IB%PC corrpatible computer.. This device is configund with a plug in module with three omebase nomendentJv adjust.able.11 is possible to select the sampling speed uhe number of acquired data points and tent of pre ce post ingger recording ior optimum acquisiuon and analysis of waveterm data). n deta:1 the charactenstic parsmeters are: r CPU 16 bit 68010 1 display trxe modes data records up to 8 K word intertre: HP.!B (GPIB) 1 snput channels input coupling AC.DC.GND Dynarnic input range 50 dB input range trom 1.26 mVpk to 39.8 Vpk.and frequency from 6: uHz to 51 kHz 3w itchable 3 mput modes voltage, charge.4 m A costant current source A D converter resoluuon 16 N with manmum conversion rate 600 kbne/second 3e measurement chain is composed of three mam hard components as shown in t ret. 2.2.2): instrument ugnal conditioner card l l l CD converter card ifor digital measurements only)
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' O i 53 ! 223 woone demian innovsiivi The digital measurements need additionalinformauons that are contained m live logcal software archmes:
transdia:er desenptor bktt physical xquisioon channel measurtment channel alarm condition acuon code monitor page The instrumentation fcr f'CC test to be recorded is divided in two group referred as digitally acquired and analogically acquired. The digital intruments are intended to determine the thermodynamic performances of the PCC component. In addition these mstruments are used where high frequency resolutaon is not necessarv. Sampling frequency for exh measurements is adjustable; prettmanary sampimg frequency is
<tted to I Hz. but this value may be changed in funcuon of the expenmental test.
Analogically recorded instruments are used in location where there is an important frequercy content. The instrument ugnal designed as analog transducers taccelerometers) are recorded on magnetc tape in FM mode. De prelarninary record bandwith for these instruments is seued to 0 - 625 Hz but this value may be
. hanged in function of expenmental test..
*2 Softw are The sof tware used to perform the data acquisition process is based on VGVMS (DEC) operauve sysrem and on VAXRDB (DEC) relational data base. All applied sof tware use the properties and the titraries of this tw1D main wort erivironments. The applied software perform the operauon to drive the data logger 3. to
.j rxord the instruments values to reduce tconverts them in crigineenng units ta c. LPs for ddlerenual pressures. MPs for absolute pressares. etca, to pnnt and plot the results and to store the data into
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SIET l- l n0098PPol t 0 1 3.s i 225 secone Newian innmtm -) d into a similar approonste mannene media. The applied software consist m a set of program mtegrate Oper:uive Svstem Utility that only allows standard and tested operauon. Inside these programs there are se subroutines o e. the calculatsenal subrouune that elaborates flow rates or water levels. etc frorn real nme saluest that are treated as venfied engineenng calculanon. The sottware that dnves the digital data leggers RTVAX300 is transparent to the users and wdl run in - 3 hxkgruond dunng the expenmental operauuns. In partscular this_ data acquisitaon system is based on ' networt architecture m which there is one control and elaboracon unit and same remote unit with data l f hM 3 sampi.ng funcuon. Every remote uruts is Imked to each other m a star logica con iguranon wu ( inforTnauon flowmg from the central control unst to the remote unit and viceversa. Any commurucauon heetwen the remote units is not allowed. The entire xuvity of control. acquisuion and elaboracon is divided in wah=1 task. Inside the remote units the commurucanon task dialog usmg MailBoses and shared area memory. This Mailboxes are FIFO type communicating channels. When a task want get informauon starts an own input MadBox.Two specialized task iNET IN and NET.OlJT) rouung the commurucanon beetwen tasks resident on dJferent remote umts , A task that send mformauon to another task on a different remote unit wnte this message to put the message and the address of the target into the NET.OUT MailBos that VET !N task on target remote unit. ' The data acquisioon process is performed usmg same tasks resu%ni on different remote units.- The vntihcrals units sample the physical signals and convert they m ntierber. This number are sended to the ' sontrol unit where goes on the first elaborsuon and the data are permanently stored on disk. The kemel of f the process of acquisition and elaboruuon is cosutusted of a shared area memory that contains the image o same
- ne earlier acquired data of all the xuve measurements channels. Around this kernel runs ,
specialized tavks. m parucular there te three tasks: read data from networt. convert it into engmeenng umts and put them m the ELAB.PHIS.D ATA Jata structure resident m mernory; when reads data of channels involved m the determmanon of logical results that must be computed on.ime starts the ELAB LOG. DATA task ELAB _ LOG.D ATA calculates the valuc of all ioFical measurements 1 parses the shared arta memory and save on disk every complete D ATA. BLOCK j 5 AQON. DIS K -
<tung a slag ot 'save ' nn the relauve block m memory.
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D cummit Rev Page of SIET I l l scuane Newen innovativi n0WAPP91 i 0 55 l 25 'e .urav of xuve taska on the central node have available shared area memory in = hach are same Ltferents type of mformataans : svstem configuration image loaded dunng the start up of all network process up1mrt acquissuon's parameters image talarm.sampimg frequency.ecc...) "Dus serta;ture reflects all the changes m the system parumesers modified by the user during data acquassoon process. one unage (temgiral shift windowl of data. This area is a buffer for build the data sinactun: on disk. The data orgaruaauon has the same logical structure in memory and on dzsk store urut. T?us structure is a bidirectional linked list. The data acquisioon process measure the trend of a phenomena dursng a penod .md a til handje a sequency of value for each rneasurements channets . The condsuon in whsch the vajue will be costant Icr an amount of sampimg is foreseen to allow a best use of mass storage space. The elementary urut of acquassoon is the D ATA that represents the measure make or calculaaed for one ume and f or one acquisioon channel. To handle a very large amount of data and allocate memory the pocess use a structure denved from the DATA: the DATA. BLOCK. This is a fised long structure that contams : sequenually sampled data array
.iusiliary mformauons forward and backward DATA _ BLOCK pomter This DATA _ BLOCK stnacture is contained mio another high level structure named ENTRY. BLOCK a ith the links to Srst and last DATA. BLOCK structure.too. Starung from ENTRY. BLOCK and track 2ng the forward imk cham ts possible ktw.wn the history of acquired data, or backsteppmg it usmg die hxkward link (for esample see the last 50 pomtsi. When the sampled data 611 a DATA. BLOCK ks tored into a disk's file and is allocated another DATA.BIDCK in which put new data. Befoic DATA BLOCK saturates the memory the process discarge the oldest DATA. BLOCK to free space for ne* data. The d2mension of this temporal wmdow is furiccon of channels number and their sampimg treguency. There's one ENTRY. BLOCK structure for each measurement channel.
Inside the recorded data Gle will be
- Tite an header contammg the expenmenta3 test idenuficanon code , the used archivies configuranon idenuncanon code, the starung daic of recordmgand further internal system 1 informatiori. i i
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D (""' Rn Page of SIET I i l { semane dennon innovainvi on09EPPol 0 i % ' m i I Ta somplete the measurement chain for the digitally recorded signals the system needs addauortal
- nlormation contained into sis logical sof tware archisies:
i transducer desenptor block pnysical acquisition channel musurement channel l
.ilarm condition accon code monitor page The first functional bos in the measurement chain is the transducer desenpoon block. It has in input a p.'.fsical signal (pressure. temperature. ecc.J and give in output another physical signal telectncal or ciectncally measurable) proporuonaj to the input. The input and output parame'ers are ntnply desenbed by ,
uung a ubel and a measurement unit. If the input / output relation is linear is sufficent define the stralitth line parameter in this formula: OUTNT = PARAM_Q + INPUT
- PARAM.M t
it ts also possible to use an esternally defined convession table Every acquisition channel capture m input the transducers output, elaborates it (conditioning. ; j snplification. A/D conversioni and presents in output a numencal value with n bit of resoluuon. The inpuvoutput transter f unction is linearly defined by using the operators OFFSET and GAIN: , OUTPUT = OFFSET + INPUT ' GAIN l This channel make avas' a ble the measittement of the pnmitiv physical value to the Measurement enannel because in general the physical channel may or must te linked with other to obtain the ngth saiculauon of a salue I i i i
nocumeest Rev Page of
'1098PP91 i 0 l 57 225 r the user to Worm the acquassuon data process: display.
s block contain the referew;c to the algontm. to the Itst of all nputauon of the engineering value. the value that may be shown in tables or plot, the pnna format xk. ied one or more alarm condsoon control funcuans.This means ,easured value to venty the overtahng of a treeshold. When an start the foreseen acuons.Dunng the data acquisioon pmcess abled or enabled by the user.The image of this informauon is of the data acquisioon process, out the action to be performed in relauon with the alarm an alarm condsoon is reached. Generally this accon may be
>nstst to send a message to a physical control channel. The 2nd correct format parameter in funcuon of :he tyTe of nbty to record an event udenuficauon channel code. time, alarm process) is foreseen.
momtor pages organizauon. In this archive are stored the ay limits. These informauon are orgaruzed for exh monstar
i l Doc ==a' Reo Pase j of SIET t l 00098PP91 i 0 58 1 225 semane Remum innovative J Nofware qualifiestme Be data xqutstuen system sof tware wtil be quaufsed performing the follo'<ing acuons: !i end cabbrated voltage srfnais to the data xquisiuon svr.cm input channels and venfy that the ugnals are correcdy xquired and recorded be 'JAS;
- ) , heck that the instrument conversion corbonts are correctly input and allocated m the DAS:
1i check that the conversson formulas are perfectly mserted m the DAS: .i senfy the corticmess of the conversion calculanons performed by DAS. sending cabbrated voltage urnals to the DAS input channels and companng the DAS convenion results with the same signal conversions carryed out by means of hand calculauons. These venficauons will be carned out only once before starung the tests both for directly measured quanuties and for denved quanuoes. The results of the venficauons will be archived in the DRF. tf some insuuments is replaced as consequence of instrument failure or tf some instnament spans is changed the s enficauons conce mng the instruments in object wdi be repeated. Be instrument zero will be venfted every day before test starting. l 1 l l
-)
5 Da***a' R" Page j at l i SIET 1 I 59- i 225
'l 00098PP91 ! O scrame wemuri innovwvi M. DAT A ANALYSIS AND RECORDING M.! Data redsetmas t
M.I.1 Dignally acquired quaantnes Dunng testmg all the mstrumentauon signals (compensauon thermocouples incluued) are recorded and stored in real ume. The samplmg frequency is normally fixed at 1.0 Hz and can be adjumed in the range 0.1 + 100 , Hz. The recuoed data are convened in engincenng units (S.I.) and pioned versus time for the entire test pened '. or selected time mterval. The mean value, the standard devianon. the manmum and mirumum value of the , acquired quanunes are also calculated. , 8.1.1.1 Directly measured quantities 8.1.1.1.1 Ahsahmte and differential pressure Absolute and differential pressures are measured by means of transmitters and transducers. The electncal kPa) as follows: signals coming from mstrument imV) are converted in engmeenng units ( l
~l Y = M * (mV - Q) + K a nere:
M. Q = cabbration constants . K = instrument hydraulic head The mstruments are calibrated in laboratory to venfy if they meet the required xcuracy. After installauon a measurement chain check is performed to control the cwww.dsce between the data acquisioon sysem recordmg charmels and the pnmary instrument. The instrument zero are also venfied every day before test starung. l
i l Doc == == i Rev Pane j or SIET I 00098 PP91 . O t 60 225 setxww Nemum Innmusvi 4.1.1.1.2 Temperatures The temperature of the fluid. piping. components anil pool water are measwed by using: sheated therinocouples type K Cmmel Alumel0.5 l.5 mm OD RTD thermoresistances type PT 100 A matru E imV). T(*C).for "k" tvpe thermocouple is generated by the following formula: (UN17938 specificanoru) E =I d, T' - 125 esp f-l/ 2* tT 127 /65/) ) / 1000
..o where :
E = electric signal imV) T = temperature a*C) do = 1.853306
- 103 JJ
= 3.891834
- 103 J3
= IW515
- 1(r2 di = 7.70237 8
- Ify5 4 = 2.283579
- 107 ds = 1570023
- Ifrio J6 = :.991291
- 10*I3
-b = - 1.2849R5
- 10-16 4 = 2.223997
- 10 20 The *alue of temperature T(*Clis obtained from the segr.ajs commg from thermocouples ElmV). performing a linear interpotauore of the matna E. T.
Doc =a' Reo Page of SIET l l 4ccone gemari Inrumini ' 00098PP91 # 0 ' 61 1 225 !n the ume ww the tigruls coming from thermoreststance (Q) are converted in engtneerung auuts (*O pertorming the linear interpolanon of the FT100 tyTe thennoresistance data chara;tensues generted by the leuo*mg formula : 2 iUNIU Ti specificanons) R3 100 * ( l + .1.90802E 3
- T 0 5802E-6
- T )
4 here: T = temperature (T) (D) R= measured RTD resistance Thermoresistances and thermoccupies are calibrated m laboratory to venfy tf they meet the requutd accuracy Before tesung a check to control the correspondence between the data acquisioon sysicm reco@g channeh and the instruments is also performed. R.I.I.I.3 Displacements Displacements and posiuons are measured by means of high ic.nerature, waterproof transducers type LVDT
.hnear vanable differential transformeri. The signals coming from the instrument (mV) are convened in entmeenng units (mm) as follows:
Y = mV /( 5
- V )
a here : t mV) mV = clectne signal coming from insuument
#mV/(V /mm) )
S = esiuvity coefficient (V) V = feeding voltage The instruments are calibrated in laboratory to venfy if they meet the required xcuracy. After installatrwt a measurement chain check is performed to control the correspondence between the data acquistuon ryseem recording channels and the instrument.
Doc""' Rev Pete l of SIET i I l 00098PP91 0 i 62 225 cuane Mesion innoveuvi i < l.1.2 Denved quaatrties < l.1.2.1 Flowrstes 3e flowrate of singk phase Guid (steam, air, water) is measured by means of dJferent pnmary elements: .in6ce plates. noz2ks. ventun tubes and Gilno. Except fcr the Gdflo flowmeters. the reference formula. in .a cordance with L'N! !0023 spectfications. are: ikg/s) F=a c
*t* 8*5 for compressibk fluid (kg/s)
F=a,*8* 5 for incompressible fluid
*ith:
APc = AP 2 p
- g
- h iPs) f or onfice plate 4
t= I iO 41 + 0.35*$ )
- ape / la
- PI)
- or Ventun tubes and nozzles M
. t b) I () *
/Pl G. , a ,
P/i , ,o3 c s i: a1 P, = P2) I 1 P) ! Q*
- j P. la i i Pi j! ,
a ncre-
-i . - im-)
- 1. = 2
- d -
- v 2
- ri calibrated or calculated Out coefficient aJ
Dac="'"' l Rn Page of SIET I xmane gum innamm i 00098PP91 i 0 l 63 225 W <i = Das coefficient c = compressibehty coefficient (c = 1 for hquid ) (m) J = throat diarneter
= Ouid density upstream the measurement device (kg /m3) 0 AP = measured pressure drop (h)
= local pressurt drops across the nozzle (Pa) 1P c
= absolute pressure upstream the measurement device (Pa)
Pi
= pressure taps height difference (m) n
= downstream / upstream pressure rauo P:/P Cp/ C, = iscentropic exponent asteam supply line = 1.27 : air = 1.4) o =
0 = diameter rauo (d / D) (m) D = tube mside diameter (kg / s) F = Do* Tate The a, Oux coefficient value is corTected taking account of the Guid temperature upstream the measurement device by means of the following formula: rz, = ac * ( 1 + A * ( T - T c.i )) im2) w here:
= woriang temperature s'C)
T
= cabbration temperature (*C)
Tcal A = imcar thermal esparision coefficient = 1.2E.5 (1/'C) With the GILFLO vanable area ortfices the water flowrate is measured as: i j I l I i
k""' Reo Page of SIET I i l { OOO98PP91 0 1 64 i 225 scume McWtn Irmovstave F = p
- i M * .1P + K 6 ik g/s) w hert:
Im' / (s Pa)) M = calibrauon constant (see table 31 (m*/s) K = cabbrauon constant (see table 3) ipa)
;P = GILFLO pressure drops 4 kg/rn')
p = water density The neam / au mixture flowTate discharged from vent tank. is measured by means of two onfice plates. The reference formula is : ik g/s)
'9 mix * .
1Pe ) 03 F = rx ,
- tmis A sin .
I * 'O.41 + 0.3 5
- D ) * .iPe /4e mix *Pp d
t nis = mtxture iscentropic esponent
- Cp, C, = Nueam
- Cucam
- X3 g
- c 3g ,
Cmin
= I/!!+ti = air quahty N 3g i/fl+s) = steam quahty Xueam =
iKg/m 3) Jmix = 4:
- H5+II/ sl A hef e ;
im 2) rr,= EI*d2*d*a J/ cahbrated or calculated flus coetficient a = flus coefficient iPal AP e : ontice pressure drop
D" *" '* t Rev Page of SIET l woone Meson inncwsim l 00098PP91 i 0 65 ' 225
= sent tank discharge line steam an density (Kg/m3) pmaa sent tank d2scharge line saturated steam density at the measured temperature tKg/m 3) put =
P* t = M steam / M 3 , = specific / absolute humidity = 0.622
- P P.
i (kg) sicam mass Mnearn = (kg) ; M air = an mass
,ent tarsk discharged steam iscentropic exponent = 1.31 cueam =
og = aa isoentropic exponent = 1.40 3
= absolute pressurt upstream the measurement dence (Pa)
P; l 0 = diameter ratio (d / D) l
= saturated steam partial pressure at the measured temperanne (Pa)
P sat l 4.1.1.2.2 Levels Liquid level in single priase or level in two phase tsteam and water, att and water) are measurtd by means d differenual trasmitters. The reference formula is: a h ) / { g * (pg . pg a ) ) (m) L = 1.iP g
- p gas
- hert; (kg/m3 )
p g33 = gas density p g33 =0 in single phase for steam and water (kg/m3 ) p g33 = pucam (kg/m3 ) p gas
- Pay = P/(R
- D for atr and water
= as pressure (Pa)
P
Doemme Reo Page of SIET I l i 'KX)98PP91 i 0 66 225 secone Memm timverive
= air temperature (K)
T
= 287.037 (J / kg K)
R = air gas constant (kg/m3 ) pi = hqwd density (Ps) iP = static pressure difference (m) M = pressure taps height difference (m / s2) g = gravity accelerauon Liquid level m presence of steam / sir mixture is calculated as :
- h I / I E * ( Pi 9 mix ; I (m)
L = { AP - g
- pmix a ith, r
(kg/m3) Pmis Put
- l(t+1)/ )
x = 0 622
- l Peg / iP - Pug) J 4 nere:
(kg / m3) pmit = mtxture density ikg / m3) peg = saturated steam density at the measured temperature (kg / m3) 0; = liquid density s = specific / absolute humidity saturated steam parnal pressure at the measured temperature (Pa) P,y
=
(Pa) P = gas spect absolute pressure (Pa) AP = differential pressure im) h a pressure taps height difference
D c="' Rev Page l of SIET i l l secone kemum lem ' 00098PP91 1 0 1 67 1 225
= gravity acceleration im /s2) 4.1.1.2J Pooldensary i
Ne pool s ater density is measured by means of differennal pressure trasmmm. as foUows : p = .iP / ( g
- h ) ikg / m3)
- nere:
differentla) pressure Pa) $ s h a pressure taps height difference (m) g = gravity accelerauon (m / s2 ) 2.1.1.2.4 Strse
~
The IC 1 PCC local struins are measured by means of capsulated high temperature strain gages. The reference .ajculation formula for the specific strasn is: t = tm +J
*ith:
_1R c' = S- K a here: (Q)
.iR = strain gage xuve resistance change
= strain gage active resistance (O)
R I I 1 l l 1
i i j l Dac = ='* 5 Res Paaa j of SIET ! l l 00098PP91 0 1 68 27.5 zwe wwim Innovaim ! I x GF*k ntrument gage tactor at operating temperature ] s imm/mm)
, = measured stt:un GF = instrument gage factor at room temperature
= = temperature correction factor = 1001 5f48E 5
- T 2.499E 7
- T2
?
j = pressure correction fxtor = 4 677E4
- P
;*C)
T = lemperature of measurement point t MPa) P = pressure on the straan gage The k and ; factors are calculated followmg the reference docurnent 2.3.1). 4.1.1.2.5 Condensatson iberTnal power ne PCC thermaj power is calculated by means of a global energy balance. The adopted formula is: Lout ik M W = F mn *h mit Fcond *h ennd F out *hout - Fentr<ond
- hen N 4 -
a nere : PCC ini.e mixture flowrate ( Fmix = F team
- F, + Ftig j ikg/s)
F,a = 4 ikg/s) supply superheated steam flowrate F ream = ikg/s)
.r * 'upply air flowrate s kg/s)
F;,4 = Jesuperficating water flowrate PCC inlet mixture enthalpy =
'y g =
WLini / F mix id / k8)
= iFym
- hucam.in
- F ,33* hair.in + F ,q t
- hlig.in uperheated steam enthalpy upstream supply line mitmg point iu / kg) h =
ues.in ikj / kg)
= .ur enthalpy upstream supply line mixing point 5.ur.in ikJ/kg) %g.in = desuphealine water enthalpy
Doe ="' Rev Paare of SIET ! I secone Ncuen innoveniv' 0009f!PP91 0 69 i 225
'A t,n = power Amt m the mixture supply line retween mixing pomt and PCC uuet (kW)
PCC ouuet condensate tiowrate (kg / s) F,ono = i
= PCC outlet condensate er'thalpy (U / kg)
'cond
= sent tank steam /sar mtature discharge hne tiowrate (kg / s) 3 F nut I
h = sent tank discharge line mittare enthalpy = l nut 1 X ueam (U / kg)
= h air.out *Xait
- ut.out h
= 1/(1+t) = air quality
\w s/(l+st = steam quahty Nueam =
P s = specific / sbsolute humidaty = 0.622 *
? - P, P eg = saturated steam parual pressure at the vent tant discharge line measured temperature (MPa)
= vent tank discharge line absolute pressure (MPa)
P h air.out = vent tank a2r enthalpy at the measured temperature and air parual pressure (P Put) (U / kg) 5 = s ent tank discharge line saturated steam enthalpy at the measured ut.out temperature (U / kg)
= sent line entrained condensate flowTate (kg /s)
Fentr cond
= vent hne entrained condensate enthalpy (u / kg) hentr-cond
= sent ime and vent tank power lost (kW)
'A' Lout De entrained liquid in the vent hne Dow is collected in the vent tank. The hqtud nowrase is measured taking xcount the sent tank level increase I AL). during a measured time interval (At) with the Squad dsscharge ime l shut of f. as : !
ikg / s) Fentr cond = sal / at>
- pentr cond
- A l
i I
- l Dac=S Reo Paste l of ;
SIET > l I coone elemum irwativi 00098PP91 0 ' 70 225 4 here: 1 4 k g/m i z entr:nned condensate denniv Jentr cond A = sent tarik cylsndrical crou section = 2.27 $-3 ~N instruments used to measure the above mentioned quanuties for the PANTIERS-PCC are reponed in the 1 allowing table: 1 QUANTTTY l USED INSTRUMENT TAG F.,,,,,, lF1001: F 1002: F-1003: T 1001: P 1001 F,,, lF2001: F-2002: T-2001: P-2001 f Ft.n f F 3001:T 3001 he,,,,o ,n l T-1001: P 1001 h ,,, ,n lT 2001: P 200I hi ,n ,n l T-3001 t i Wt in T 1001: P 4001: T-1002: P 1002 l F,..,,,a l F L001: T-LOO 5 l i h,nnd T 5001: P 5001 F,,, ,, l F T001: F T002; P.T001: T-T001
! h , ,, n,,, l T TD01: P-T001
%, n,.. T TD01: P T001 j
P ,, T.TT101 t j P l P T001
; F,o,, ,nna l L 1001: T-1001:T 1002: T 1003: P-1001 Pentr cond l T 1001: T 1002: T 1003: P 1001 i h.n,, ,nna l T.1001: T 1002; T 1003: P 1001
- W,,,,, ! F,,,,, T 6001: TWX)2: T 1001: T.1002:
f
' T in01: P 1001 l
1 l l l i
k=a' Rev Page or SIET l l 60098PP91 1 0 71 225 coone kemon innmeim (1.1.2.6 Heat flus coefreient 3e local hess Oux cocificient is measured as :
= Q* , i T e T pool 1 (W / Km 2) h5 a eih.
Te) / In ( R, / R, ) ( W / m2 ) Q* = k / Re * ( T,
- here :
= local thermal Out (W / m2)
Q*
= AISI 304L or INCONEl. 600 thermal conductivity ( W / m K)
L
= external TC hot junction rad 2us (m)
Re internal TC hot junction radius (m) R, = csternal tube wall temperature (K) Te =
= internal tube wall temperature (K)
T, pool temperature (K) T gj = 4.1.2 Analogically acquired questities Dunng testing the signals coming from accelerometers are recorded anajogically using a magneuc tape recorder and later analized by a FFT. The data recording is periormed only dunng certain time penods with tape speed set during the shakerinwn t est, ne signals will be later reproduced at the same tape speed and sent to the FFT to obuun Power Spectral Densities iPSD) for resesn:h of the main frequencies. 1
kune j Rec Page j of l SIET i 0 ' 72 i 225 enone Henium iwan ' j M 8PP91 t
- 2 Errirs esatuatsoo
'e ar% lute maximum error aan and the statu12rd deviaton ici of the dacctiv measured physical quanuues m69tc and dif ferential perssures, temperature. etc. are defined as: 133 + Sgy + ag,;# mammum ermt 3= standard devauon a=: 31 + 4 + 4 )o s 4 here: 3; = assigned accuracy raung of the instrurnent for absolute and ddTerenual pressure: ANS! specsal error for thermocouples or calibration maximum error. UNI 7937 spec Scauon accuracy or calibration maumum e: Tor for thermoresistance; manufacturer accuracy or cabbrauon maximum error for LVDT crmr m acquisituv; trd A/D converter bit value 3BV= ag = maximum error of the cold Juncuon tonly for thermocouples) The absolute manmum ermr and the standard devianon of the denved quanuues tilowrase. levels, etcJ will v calculated using the following error propagation tormulas: t 3x, 3r = - ,,ri 'x, s
- . ~0$
cY = : 'f eX,) Y = i i X, # s = 1. 2. .n 4
- j. Docuiust Rev Paee of SIET . l l 00098PP91 - ' 0 l 73 ! 225 scoone Reston innovem l
4 here it and cXi are the manmum error and the standard devtauon of the X iquanones. The error .alculations will be carned out usmg,in a conservar *e wsy, the upper value range of the iruarumeest. , t 8.3 Data prv>cessiost and analysis The data analysis will he performed in order to evaluate the goodnes of the experimental test. Dunng the . expenmental phase the operators will perfonn a momtonng of the measurement values m order to venfy the mos important test' paran.ners and to check the congruency of the values. If necessary an on-Itne intrument , - heck is foreseen m order to recover the error. The data processing and analysis adi be performed m three steps which are desenbes as
- quack look*.
" preview" and full processing and analysis.
A " quick look" phase will be performed in order to provide the mformauon needed to proced with the . preparauon for the next test. This will consist pnmanly of indentification of the matrument which have tailed or performed incorrectly danng the test. venficauon that the objecuves of the nest were aclueved, and
- he control of the structural data to insure the integ.nry of the condenser. More decaded informataan will be e
performed in the " preview
- phase that has the purposes of providmg representauve results from the most .
ognificant measurements to be used m the " Apparent Test Results* report, and to and an defining the remainder of the analysis. The time history plots and digital data tables of key parameters will be performed and examined to determine time penods of significant mterest for more detatied analyns. The plots and tables for the Fmal Test Repon wdl be generated m the " full processmg and analysis" phase which has the purpose to organtze the data in a form that provides an integrated mterpretapon of the test results to show the perf ormance of the condenser and demonstrate that the objectives have been achieved. c 4.4 Data records i The digitally xquired data values wdl be directly wnte on magnete disk in real time (cr the enure duranon .l of the expenmenud test. Immediately after the end of the expenmental test will be done a copy of the dass file on a magnets streamer tape m order to have a saved image of the data file. More wd1 be copied into the magnetic streamer tape the compiementary mformauon about the expenmental test the transducers, the t i
Ne = Rev Pate j of I } SIET ' 00098PP91 ' 0 71 225 wcone keancri inno*sim pnMical input channel, the measurement channels. the alarm the action archivies and the monitor page rchmes The miormation about d:ulv instrument check, about the happened alarm condtuons. the change operated tw the user inside the data *ase will te logged in relative file and saved on magnetic streamer tape im l Be analogically recorded data will be accutred on analog tapes at fixed tape speed. The recortiang of these data will be pertormed only dunng mteresting transtent. In xcortimg with the tape speed chosen the life of a WF analog magnetic tape will be about 3500 s. The analog tapes will be replayed through the FFT Jcvice and the resulting information copied and stored on magnetic disk for future interpretauon and .mabsys. De distance betw een gnbe marks will be measured pnor testing and at the end of the tests. the measured distances will be recorded in wnung on suitable data sheets. All the test records analysis and venficauon record will be stoird into a Design Record File iDRF)
#5 Data sheets De follow ma data sheets will be prepared for exh espenmental test:
)
i I ii rnnt table containing the list of the mec -ments with their main characteristics indentification. pan, calibration constantsassociated ermr. location on the facility, measurement channel number and umpime Ireuuency ) l L pnnt table containing the daziv mstrumentation check h rnni tables of digital s alues ni the recorded signals m engineenna units for selected time penods L rnnt tables of mean, standard deviation, minimum and mastmum value of all the measurements in ensmeerme units dunng a specified time penod (i plot graps of any selected test varable as a funcuon of time stame history)1or any wiected test time
- indow The single plos graphs will show troup of I to M test vanables
i I 1 l Doe = Rev Page of 1 SIET I I 4 00098PP91 ' O 75 225 secone kemm innovum , 1 ne uNes conuing the results of spectrall analysts for determuuuon of the pnmary frequettes present in the accelerometers. The eapenmenal test identification code *til be printed on all pnnt ubles and plot graphs Tante containtng the measure of the distances between scnbe marts performed pnor of tesung and at the end of tests wdl be prepared too. i
i I Dac = Rn Page of SIET l 1 l l n0098PP91 - 0 1 76 i 225 1
-econe kcumn innovenivi ,
i l 9 SHAKEDOWN AND PLANT CH ARACTERilATION J 9i PL ANT CHAR ACTERIZATION ne plant *ill be characterued by two bnds of pre-operauonal tests; cold and hot tests. Be purposes of cold pre-operational tests are: senty the pml suppon structure atest n. C-01 t s enfy the adequacy of pool make up and level control system, determane the adequacy of the pool connecuon line and venfy flowmeter cabbestion (test n.C 02k determine the hvdrauhc resistance of the mJecuon hne. nser, condenser vent line and discharge i
!ine. senfy the air compressor capability and the adequacy of the vent tank pressure control wstem tiest n. C-03t
-!ctermine the hvdraulic resistance of drain line. Senfy the ade vy of condensate tank level ontrol svstems and of the pressunzauon systems atest n.C-04 3e purposes of hot pre-opersuonal tests are:
Jetermine the heat losses ni the injection line. sent hne and the vent tank, venly the tube 1 bundle wall thermocouple calibrauons and veniv the vent tank proget itest n. H 01t l 1 Jetermine the heat loues of the dratn hne and the condensate tank and venly the condensate i tank project itest n. H-021: Jetermtne the heat losses of pool connection hne to catch tank and venfy the stack discharge
..ipabthtv stest n. H-03 t 4
Document Rev Page l or SIET j l 00098PP91 0 77 l 225 c:2 cme dearr:1 Irmveim 22
.ontirm plant stabdity (i.e. to rexh steady state condicons6 to perform matna test number 4 41(test n. H& and H.05) 9 1.1 Geoeral description of test C-01 The test wdi be performed by filhng with water IC and PCC pools at seven different levels frorn I m m 4 5 m and by messunng the pool support structure defoimation in order to vertfy tf the custmg -upport structure is able to withstand the maaimum load without exceedmg the maumum allowable Jeformation.
The test detailed procedure with its check itsts are reponed in part 11 of this TP&P document 9.1.2 General descripnoe of test C-02 The test will be performed feeding with four different flowrates, the IC pool with level set pomt LIC-Q001 tixed to .t.2 m. and drammg the PCC pool m order to venfy the adequacies of the pool make.up, level-The test detaaled procedure with its checkhsts are reponed in sontrol systems and flowmeter calb i rations. part 11 of this TP&P document 9.1.3 General description of test C.03 The test will be rerformed with complete closed PANTHERS.PCC facility. The condensate tank wdl be t'dled bv water to reach level L LOO 2 = l.75 m teorrespondmg to 2.5 m above the condensate tank inlet nozzles and pressunzed witt a2r at the same PCC mlet pressure: the steam supply hne will be closed. the PCC inlet pressure will be c ontrolled using vent tank discharge valve R)20 and PIC.4002 conceller. The test will be carned out sendang aar flow through the nser to vent tank at four different air Dowrases and two pressure levels, in order to determine the pressure drops of anyecuon line, nser condenser, vent hne and to venfy the air compressor capabibty and the adequacy of the pressure control system. The test detailed procedure with its check hsts are reponed in part !! of this TP&P document. Enclosure 2 is a schematic view of the plant configuration for test C43.
Doc = R*o Paae of l SIET I I 00098PP91 > 0 i 78 1 225 enone dcamri innowm + 1. 4 ;eneral decripnoe of test C-04 3e test wid be per1ormed with compicte closed PANTFfERS PCC fx htv. The vent line and vent tank wdl y enduded closing spectable 11ange SF002; the steam supply hne ud! be closed; condensate tank wdl be leed water hne wdl be connected to .onnetted to infecuon line opening spectable flange SF001; a temporary module i upper header and water flow will be sent through module 1 Rx and drain line to the condensate tan t The condensate tank *dt be filled by mater to reach level L-LOO 2 = 1.75 m teorresponding to 2 5 m above
'he condensate tank inlet nozZiel and the level will be Controlled by means of pneumatic control valve F019 ed LIC-LOG 1 controller.
Be estem will be pressunzed sending air to the nser and to the condensate tank and the pressure wdl be regulated by means of pneumauc controu valve F021 and PIC-LOO! controuer. The test wdl be carned out feeding the module i upper header with four different water flowrates and tw hfferent pressure in order to determine the pressure drops of drain inne and to venfy the adequry of the
!* o condensate tank level control systems Id scharge from overtlow line or from bottom of condensate tank) tnd of pressuruauon system.
De test detaded procedure with its check lists are reported in part 11 of this TP&P document. Enclosure 3 is a schematic view of the plant configuranon for test Col. 9.1.5 General desenpron of test H.01 Ne test wdi be per1ormed with complete closed PANTHERS.PCC fxibty. with pools P. Q and condensate tant empty and the condensate tank liquid discharge line connected to bottom. ne condensate tank wdl not be connected to irijecuon ime closing spectable flange SF001 and the air feed Sne w all be excluded. The condensate tank mixture discharse kne will be excluded closing F015 valve. De system *d be pressunzed at tour differnt pressure levels sending a small flowrate labout 0.2 kg/s or em of superheated steam (superheating level less or equal to 10*C) through the nser and PCC to the vent
. ink; the preuure wdl be regulated by means of control valve F020 and PIC 1002 controller on vent tank I
misture discharge line. ne superheatmg degree on the nser mlet steam will be adjusted in order to have saturated steam m PCC whe bundle vent ime and went tank. The heat losus os the went ime and vent tank will be determmed by means of thermal balance measunng and plotting the condensated s ster level of vent tank versus time. l
~
D"= "' Rev Page of SIET ! ) i secone Wesun intestwa 00098PP91 1 0 79 225 The test will be camed out with four different temperatures of steam in the range 130*C .170*C. The sexam .ondensated by PCC heat exchangers wiu be dramed to the concuate tartt. The heat losses of the injecoon hne will be calculated performmg the thermal halance between the injeccon ime steam air mtung point and the nser inlet. The calibrations of the PCC bundle wall thermocouples will be vertSed and ewntually .ahusted compartng the steam saturanon tempratures wim the temperature values given by wau
- hermocouples.
The test decaded procedure with its check itsts art reported in part II of this TP&P document. Enclosure 4 is a schemaue view of the plant contigurauon for the test H41. 9,1.6 General description of test H 02 The test adi be performed with complete closed PAfGEERS-PCC facdsry with pools P and Q ernpry. The PCCs heat exchangers wdl be tsotated by closing the vent and drain imes ustrig the spectacle flanges S!002 and SF003. The PCCs heat exchangers wdl be filled with water by connectmg a temperurwy feed water Itne to the module I upper header. The condensate tank will be connected to injection ime opentng the spectacle flange SF001 and the condensate tank liquid and steam discharge imes will be excluded closing the manual valves 1017,1918 and F015 respecuvely. The drain line and condensate tank wdl be pressurtzed at four different petsswe levels bv feedmg with a very small steam flowrate the PCC nser (superheatmg degree less or equal to 10
'CL The steam temperature wtli be adjusted m order to have saturated steam in the drazn ime and condensate tank.
The test will be camed out startmg with condensate tank empty at four differerit satursuon temperatures d steam in the range 130*C 170*C. The stearn pressure =di be controued dischargmg steam to the atmosphere through the manual valve F503.The heat losses of the common drain line and the condenssee 1 tank will be determmed bv means of thermal balance measunng and plotting the condensated water level d l
.ondensated tank versus time.The test datailed procedure with its check lists are reported m part 11 of this ,
i TP & P document. Enclosure 5 is a schemauc view of the plant contigurauon for the H42. i I i l i I
D*cta' Rev Page of - .; SIET I l 00098PP91 0 40 225 senone Remiari Inteauvi i 9.1.7 (;eneral description of test H-03 ne test will be performed with complete close PAS ~!HERS PCC facibry, with pools P and Q filled at a ' level lower than 0.5 m respect to the normal water level (l.26 m m IC pooll m order to avoid the overGow os the PCC water to the catch tank dunng boil of f. De test wdl be performed heating the PCC pool water s l till to reach steady equdsbnum bulk (steady states average remperature. e De PCC pool water heanng will be carned out feeding the FCC wuh saturated steam and allowmg the pool to reach steady state bulk average temperature. When the PCC pool is m boding condsuons the steam do* Tate will be reduced at the mmimum value capable to mantain the pool bothig in order to mmtmtze the qeam velocity and so reducing the carry over effect. The steam generated by PCC pool mdi be sent to the stact through th.: pool steam connecuon hne. the
,ondensated hyuad generated by the heat losses of the pool connectaon hne to the catch tank wdl be measured m the loop seal of the catch tank Ime.
'The heat losses wd be measured performing thermal balance plotung the loop seal water level versus time.~
De detailed procedure of test H-03 with its check lists are reponed m part !! of this TP&P document. 9.1.8 (;eneraldescription of test H 64
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The expenmental .o..,1:tions and procedures of this test are the same of test type A.I.3 i8-u.uodules, steady state - steam only - no att m PCC tubes) test condsuon n.43 and therefore the general desenpuon of this test a reponed in paragraph 10.$ while the detailed procedure of test H44 with its check Insts are reponed in - h ran 11 of this TP&P document. > 1 9.1.9 (;eneral description of test H 05 r i The expenmental conditions and procedures of this test att the same of test type A.l.1 (two modules, steady - state saturated steam /atri test condition n.22 and therefore the general desertptson of this test is reported in paragraph 10.3 while the detailed procedure of test H-05 with its check lists are reponed m part 11 of this ! TP&P document. a L 4
-eV e - e - - - .
D cument Rev Page at SIET I 00098PP91 1 0 81 225 scoone keancn innovatm 9.2 %hakedown matru ne cold preoperauonal test mains is shown in tab.4; the hot preeperauonal test mmu ss shown in tab.5. The pre opersuonal test detailed procedure check bsts are reported in part 11 of this TP&P document. I i 1 l l l l 1
1 Do " ' Ro Paste l of l SIET I I j 00098PP91 0 I B2 1 225 ct mc Mession intownim
- 10. P 6SIVE CONTAINMENT CONDENSER TE.STS i Se PCC tests *di te a senes of steady state tesu at specified steam now rate. non condensible Dow rate.
niet gas temperature and inlet pressure lequivalent to drvsell). The condensate tank pressure wdl be equal u miei .ressure and the vent tank pressure will be ad.iusted to obtain the specified PCC inlet pressure. De PCC pool will be maintained at a costant level tfull) and equilibrium bulk average temperature dunng mosa ests. The PCC will be brought to the specified conditions and allowed to stabtisze. i.e. reach a condamon d
. tem!v - state heat transfer and allowed to operate for apprettmately 15 minutes at these condamons. Data siti be recorded dunng pool heatup and for the penod of steady operauon.
Initial nesting wdl be performed usmg a complete PCC unit (two module). The perfomance of this unit will v tested over the expected range to SBWR condiuons. Following the perfomance tests addauonal tesung 4 ill be performed to complete the required structural tesung. Alter successful compicuon of these tests. one PCC module wdi be removed from the factlaty and the pool hal0cd to reduce the effecuve size. The sinsie moduie PCC will be iested at cond200ns eqtuvalent to some of the f ull PCC tests. The purpose of these tests is to xcomplish the objecuve of IC test modeling desenbed in chapter 2. Tests usmg hellunvair mixtures will also be done with the single module. 10.1 Types of tests required for the PCC The tspes of tests to be pertormed with the PCC have been defined as follows: A Tests with two modules: A 1.1. Steady state perf ormance-saturated steam /azi mixtures. A.I.2. Steady state pertormance superheated steam / air mtxtures. A 1.2 Steady state pertormance steam oniv. A 2.1. Effect of pool water level.saturaged steam. I A.2.2 Effect of pool water level-saturared steam / sir mixtures. I i
. one - i an Pas.
SIET [ l
.f 00098PP91- i 'O 83 225 woone Reanon innovum i 4
A.3.1. Addiuonal Structural Tests simulated LOCA pressurumwwi A.3.2. Addauonal $tructural Tests. simulated leak tesung. A.4 Steady state. air only pressure loss measurement. B. Tests with one module: B.I. Steady state performance. steam only. B .2. Effect of low density noncondensibles. 10.2 FIRST PRIORTTY TESTS The first pnonry tests are a senes of steady state tests that wdl be performed usms a complete PCC unit immediately af ter the compleuon of the shakedown tests.These tests will be performed just with saturased - steam / air and just with saturased steam only (no air in PCC tubes). The general desenpoon and pmcedure of these tests are equal to those of tests tyTe A.l.1 and test type A.I.3 reported in paragraph 10.3 and 10.5 respectively. Four of these tests will be camed out at inlet condsuons correspondmg to same of the Toshiba Giraffe phase I tests.
10.3 DESCRIPTION
OF TEST TYPE A.I.1 Two Modules, Steady State-Saturated Steasi/ Air. O-neral Test ortredure The selected constant values of air and steam flow rates (m3 and m grespecovely) are set up accordmg to procedures determmed dunng shardnwn testmg. The PCC inlet pressure is adjusted to manmum value. Pi
< max i using vent tank discharge valve. Inlet mixture temperature is set to saturated condinon. The PCC E
1 1
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a R" Pase of , SIET i Dac5""' I I. 00098PP91 1 0 > M 225 i se.aone wcmari innovum - I pool water n allowed to heat up to sieady state bulk average temperature. Valve settings are trimmed to
.ahusi inlet temperature and pressure to presenhed 5alues. '
Data are recorded at approstrnatelv 5 inlet preisure values between Pi (mast and Pt imint or unul a '
<pecified PCC detta P limit is reached. The delta P limit will be apprustmately 14 LPs C psal, but will be The test wdl be repeated for each selected value. f specified by the Responsible Test Engineer pnor to the test. ';
of ma and ms. For what concerns indeperkient vanables the pool level is maintamed constarit at normal level (full). The inlet gas temperature is set at saturation value corresponding to the inlet pressure and gas mixture or the '
'!he detaded procedures of test type A.I.1 with its specilied depees of superneated above saturauon.
eneklists are reponed in Part 11 of this TP&P document. , 10.4 DESCRWTION OF TEST TYPE A.I.2 ,
.i Two Modules. Steady State-Supertested Stessi/ Air.
r'ener11 Test Prncedure Procedure is the same as Test A.I l. Some of the murated test condst2cns will be repeated from A.1,l.. cach
.. two salues of superheat. i.e. six test condiuons teach with 5 inlet pressure valuesI. The superheated values are io be determined (TBD) by analysis pnor to testing.
4s A.I.l. The detaded procedures of test t) Tie A.I.2 with its ; Independent vanables are the same as I: e hektists are reported m Part 11 of this TP&P document. 10.5 UESCRIPTION OFTESTTYPE A.lJ Two Modules.hteady State 5 team Only. when the PCC is tested with steam flow only, the pertormance .an be affected by the presence of noncondensible gas trapped m the PCC tubes. Two conditions will be considered for Tests Al.3.; l) No ast in PCC tubes. and 21 Air m PCC tubes. I
1 i of Dac '*"* ' Roy Paqre SIET l l rXXF38PP91 ( 0 85 225 senone Re. arum insunarm 1, CeerM Tea Pmeedure No Er m PCC rubes The spectacle flange in the vent ime may or may not be closed for these tests. Thas will be decuted on the hasts of the shnednwn tests. All air is purged from the system pnor to start of tesung. The condenser is row similar so the IC, i.e. with steam flow rate as the mdependent vanabic, the tnlet pressure wtll be adjusaed o masch the capssary of the FCC. The PCC is opermed at different stearn flow rates and data are recorded. Inlet pressure shottid nrt te allowed to increase above 690 kPag (100 psig). For what concerns independent vanubles the pool lewi is maintained cartstant at normal level. The inlet gas temperature is adjusted accortiing to the measured PCC inlet pressure. Values of superheat are to be determmed (TBD) by analysis pnor to testing. No condauons are prtmded for mlet air flow for these tests. The detailed prrrwimes of test type A.1.3 (no 22r m PCC tubes) with its cheklists are reported in Pan !! of this TP&P document. L GenerM Test Pmeedun .Atr m PCC tubes Smetacle flange is closed on vent line. The air is purged from systern with steam pnor to start of test. The speci6ed saturated steam flow rate is x1 up and operauon (inlet pressure) =Wihad Air is bled slowly into eniet ime to PCC at a metered rate and data are recorded as mlet pressure increases. Test is ceased when pressure stops meressing or appinaches 690 kPag (100 psig). For mdependent vanables, the pool level is maintamed constant at normal level (full). The inlet gas temperature is adjusted to the saturated temperature tor the specif~ sed superheat) of the stearn at the mittal ipurged) pressure and mamtamed constant throughout the test. The inlet air flow rate is adjusted to a rate
- hich will fi!) the condertser in appronunately 15 to 30 minutes at the stabilued mlet presure. The detailed procedures of test type A.I.3 (asr in PCC tubest with its chekjists are reported in Part 11 of titis TP&P document i
Doc = a' Rev Page of SIET I 1 l 00098PP91 , 0 ,
% 8 225 scocme Mcanm Inno. im 10.6 DESCRIFTION OF TEST TYPE A.2 Two %1oduks. Effect of Pood Water Level O nent Test Pmcedure Dese tests wdi demonstrate. for a timited set of condicons, the effect of pool water level decrease on the pertormance of the PCC. It is proposed to do this by recording data while slowly lowering pool water level aiher nv allowing the water to boil away without refilling or by slowly draming. When the low level ts rexhed m the pool. amou:nt water will be slo *ly added to refill the pool, while contanumg to record the data. Two test condiuons are forescen: saturated steam and saturated steam / air mixture respecuvely.
A 2.1 Samted sinm: all air will be purged from the system and test condscon n. 81 will be repeated. about 50% of nonnal level or until the inlet pressure allowing the pool water lesel to decrease to reaches apprextmately 100 psig (690 kPag). The detailed procedures of test type A.2.1 with its , beklists .tre reported m Part 11 of this TP&P document. A 2.2 Saturated simm!nr mnture: the test conditions n.15 and 30 will be repeated allowing the pool level or unul the inlet pressure reaches a ater level to decrease to about 50% of nortnal approximately 100 psig. Test is started with the minimum values of inlet pressure and the vent sank discharge valve postuon as mamtained throughout the test. For w hat concerns independent varubles. test is begun with normal pool level a full) and this as allowed to decrease to 50% of normal. Slowly it is relilled and test as ended with pool again at the nonnat level. The inlet gas temperature is adjusted to saturanon value correspondsrig to the mlet chekhsts are pressure and gas mixture. The detailed procedures of test tpe A 2.2 with its reported m Part 11 of this TP&P document.
Doe =' Rev Page of SIET l l 1 l waane Henrri tenam 1 00098PP91 1 0 87 225 ! I l
10.7 DESCRIPTION
OFTEST TYPE A.3 T mo Modules, Additional Structural Tests. To confirm the PCC structural design adequacy for the SBWR desgn hicame, the est program most include tesung the PCC for at least five times the number of design bans pressureAemperunre cycles. De perf ormance test tncludes most of these condiuons. except for the LOCA ard the pneumane leak tesang. 10.7.1 Test type A.3.1 : simulated LOCA presuritanoas The design basis is two LOCAs dunng the sixty year design life of the PCC. For the test.10 sirnulased LOCA cycles must be performed. Ceneral Test Pmcedtrre ne PCC is to be rapidly pressurued with saturated steam to 379 kPaf g)(55 psig) and 151 *C (303 'F). The s ent tank discharge valve must be partly open dunng pressunzanon to purge air from the PCC tubes and permit hesung. The total time penod for the pressunzaoon and data recordmg is appraumaaely 30 mmutes. The flow rate of steam required to achieve these condiuons can be determmed either by shakewn testmg or from previously run two-module tests. If the steam supply is not large enough to mamtran the requzred pressure with a steamotly inlet flow to the PCC, as flow can be nort Pre adpstment of the vent tank discharge valve posioon by "tnal and error" may be necessary. The pool level is mamtamed constant at normal level (fulli. The pool temperncure as trunalired with pool as ambient temperature and allowed to heat up in response to PCC performance. The inlet gas tempereture is adjusted to saturated temperature at 379 LPs g (55 psig). No mlet au flow rate is provided for these tests unless it is requzred to achieve the final teqused pressure This procedtut will be performed a total of 10 umes. The pressunzauon transient for PCC will be about the following: 1 I l l l 9
M Dac=="' Rev Page of SIET l l 00098PP91 1 0 l s8 225 coone kwinn Innovaim 4 PCC mlet pressure Required ume to reach pressure , kPar epsial 'wel l istani 0 (0) l l75 (25.41 2.3 249 (36.1) 32 i 261 (37.8) 67 379 (55) 1800 The deta4Ied procedures of test type A.3.1 with its chekhsts are reported in Part 11 of thts TP&P document. , 10.7.2 Test type A.3.2 : Simulated Pneumatic Leak Test Pressuraations. The PCC design basis assumes that the unit will be pneumaccally pressunzed for leak testing 60 times Junng its design life. Each leak test will consist of closmg the vent and condensate lines and pressunzmg , the PCC with a to 758 kPat g)(l10 psig). The pressure will be masntamed long enough to demonstrane that [ the PCC does not leak. For the structural test,it is required to simulate five times the number of load cycles - produced by these leak tests and theretore a total of 300 tests will be performed. ! Cener11 Test Pmcedure 7he sent and condensate lines are closed of f as necessary to permit pressurtzation with str to 758 kPa(g)
' i 10 psig). The system is pressunted with air to the required pressure. pressure is held for approximately l-2 minutes and then released. The unit may be partially filled wnh water to reduce the time required for pressuruing. The PCC should be checked for leaks by venfying the absence of aar bubbles in the pool approximately once for each fihy cycles.
1 l i
Document j Rev Page of SIET l l rC098PP91 O I 89 I 225 ) semm Memon innovum I I Pmi les et n maintained constant at normal level t f uth. w htle pool temperature is ambient temperature. Inlet cas temperature is less than 60 'C t140 'R. Inlet air now rate is sufficient to perform approumately 8 a ctes per nour. The detailed procedures of test tyTe A.J.: with its chekhsts art reponed in Part 11 of this j TP&P documenL 1
10.8 DESCRIPTION
OF TEST TYPE A.4 l 5teady State Pressure imes. Air.Only. Cenerni Test Procedure The PCC is operated with air only at several selected flow rates. At exh flow rate, the vent tank discharge s ahe is adjusted to give 8.3 kPag (l.2 psig1 pressure at the PCC vent pipe connecuan. Condensate drain line should be submerged. PCC inlet pressure, vent connection pressure and the ddierenual pressure are recorded. The Foi level is maintained constant at normal level (full). Pool temperature. is ambient temperature. Ittles air temperature is maintained constant for all air flow rates at a convement value between 20 *C (68 'F) and 29 'C 1120 'n Vent tank pressure discharge valve is adjusted at exh air flow rate to mamuun PCC vent .onnection pressure to 8.3 LPag i1.2 psig). The PCC will be operated with 6 ddferent azr flowranes covenng the r3nte from 23 4 of the maalmum available up to the maaimum availabie. The detailed procedures of test type A 4 *ith it.5 chekltsts are reported in Part 11 of this TP&P document. 10.9 DESCRIlilON OF TEST TYPE H.! Sinale Module. Steady State-Steam Only. These tests repeat some of the test conditions from the two module test A.I.3 as followit
Doc = =8 Reo Page of SIET I l l 0 ' 90 225
<enone Meanon innman,' 00098PP91 '
ii Generu Test Pmcedure - No nr in PCC tubes The mectacle tlanne m the vent line will te as it was for Tests A.I.3 Part 1. All air is purged m from the system pnot to start of testing. As m A.I.3, the steam flow rate is set and the inlet pressure is aUowed to .4just to match the capacity of the PCC. The PCC is operated at one-half the steam flow rates used m A.I.3 and data are recorded. Inlet pressure should not be allowed to increase above 100 psig.. The pool level is mamtained constant at normal level. Inlet gas temperature is adjusted to the saturated salue at the measured PCC mlet pressure. The detailed procedures of test tyTe B.I (no air in PCC tubest with its chektisu are reported in Part !! of this TP&P document.
) Cener_tl Test Pmcedure . Att m PCC tubes Perform tests similar to the two modules tests. A.I.3. part 2. Spectacle flange is closed on the vent line. All .ur is purged from system with steam pnor to start of test. The specified saturated steam flow rate is set up and operauon onlet pressure) stabihred. Air is bled slowly mio inlet line to PCC at a metered rate and data are recorded as mlet pressure increases. Testmg is ceased when pressure levels out or approaches 100 pssg.
Pml level is maintained constant at normal level (full). Inlet gas temperature is adjusted to the saturated iemperature for the specified superneati of the steam at the ...iual (purgedi pressure and maintamed s onstant throulthout the test mlet air flow rate is adjusted to a rate which will liU the condenser in
.ipproximately 15 to 30 minuies. The detailed procedures of test type B.I 1:ur m PCC tubes) with its ,hckhsts arc reported m Part !! on this TP&P document.
10.10 I)F.SCRifilON OF TEST TYPE H.2 single Module: Effect oflow density noncondensables. Genen! Test Pmeedure Tats are pertormed umilar to the imo module tests. A.I.3. Part 2. except usina helium arid helium / air I l
'nitturet in place et air.
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' Da** * "' ! l SIET -
00098PP91
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91 ! 225 wraone dennon innovanvi 4 I 1 spectac'le llange is closed on PCC sent line. All air is purged from system with steam prior to start of test. Saturated steam llow rate is set up and operauon innlet pressurel stabihzed. The noncondensable gas is bled dowly into inlet line to PCC at a metered rute and data are recorded as inlet pressure increases.. Test is
, cased a hen pressure levels out or approaches 100 psig 1690 kPa gl.
-)
Pool levet is maintained constant at normal level. Inlet gas temperature is adjussed to' the saturated .! iemperature of the steam at_the initial (purged) pressure and maintained constant throughout the test. Inlet helium flow rate is adjusted to a rate which will fill the condenser in approssmately 15 to 30 minutes. The detailed procedures of test type B.2 with its cheklists are reported in Part 11 of this TP&P document. t, b
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D*c= "' Rev Page of SIET l I l l 00098PP91 0 t 92 225 emme Neuen treum
- 11. TEST %t ATRICES j
l Te ref erence expenmental test conditions foreseen for exh PCC test type group or sub group arth TWO MODULES are reponed m : Tab o: PCC FIRST PRIORITY TEST MATRIX Tab. ? - PART A TESTS WITH TWO MODULES - TT.ST TYPE A.l.1 Steady State Performance - Saturated Steam / Air Mixtun: Tab. 8 : PART A - TESTS WITH TWO MODULES -TEST TYPE A.I.2 j Steady State Performance - Superheated Steam / Air Mtzture ! I J Tab.9- PART A TESTS Wi1H TWO MODULES - TYST TYPE A.I.3 Steady State Perfonnance Steam Only No Air m PCC tubes l Tab.10 : PART A - TESTS WITH TWO MODULES TEST TYPE A.J.3 Steady State Performance Sicam Only - Airin PCC rubes i Tab.II: PART A - TESTS WITH TWO MODULES TEST TYPE A.2.1 Effect of Pool Water Level Saturated Steam TEST 1YPE A.2.2 Effect of Pool Water Level Saturated Steam / Air Mtxture Ch.10.7.1 : Addstional Structural Tests Test type A.J.1: Simulated LOCA Pressurualmns L'h 10.7 2 . Addstonal Structural Tests Test tvpe A.3.15 mulated Pneumauc eaktest Pmssunzauons j Ch 10 M . Test tvpe A.J. Steady State Pressure Losses. Air only
SIET : Da' " '"' l Rev. l Page ]; (4 none desim innowmvi 000%PP91 0 93 ) 225 Te ref erence expenmental test conditions fcreseen (cv exh PCC test nTe group with ONE MODLLE are eponed in : T.ab.12 : PART B - TESTS WITH ONE MODLLE TEST TYPE B.1 Steady State Performance - Steam Only - No Air in PCC tutes Tab.13 : PART B TESTS WITH ONE MODULE TEST TYPE B.! Steady State Performance - Steam Only - Air in PCC tubes Tab.14 : PART B TESTS WITH ONE MODULE - TEST TYPE B.2 Flfect of Low Density Noncondensibles 11.1 Acceptsace criteria The expenmental conditions will be xcepted if they meet the following acceptance condstsons (*): I> PCC inlet pressure iP 4002) = reterence matnx value +/ 50 kPa
- ) PCC inlet temperature iT 4002) = reference matrix value +/- 5 'C (")
. PCC air inlet flowrate IF 2001/ F 2002) = ref erence matnx value +/- 10 %
o PCC >tearn inlet flowrate iF.1001) = ref erence matrix value +/- 10 %
. *) These acceptance entena can be changed af ter the shakedown tests i"1 Appbcable only to tests : 31 + 36. 44 + 49. 52. 53
D '"*est l Rev Page of SIET l scoone genion immim 00098PP91 i O I 94 i 225 I: REPORTS A hnel Apparent Test Result i ATR) report will be prepared for exh test. as desenbed in CH.7.3. within mproximativ one week followine pertomance of the test. The ATR report, approved by the Responsible Test Engineer, w all be transmined to the Test Requestor iGEl. A Final Test Report tFTR) contauung the data analysis and results of all tests wiu be prepared, as descnbed in CH.7.3. within approximatly wo months after the end of the tests. The FTR. approved by the Responsible Test Engineer. will be transmined :o the Test Requestor. l l 1 l j 1
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- 13. Q A REQUIREMENTS The tests in the PANThcRS fribues are pertormed by SIET under a researth contract with ENEA. in the tramewort of the four party Agreement (General Electnc. Ansaldo. Enel and Encal on the Design Development. Procurement. Fabncauon and Tesung of ICS and PCCS Components.
The QA procedures apphcable to the tests are in comphance with GE's Test Requaremerits and with Enes's i Advanced Reactors Departrnents Quahry Manual, and an: xtuated xconhng to Siet's Quahry Plan ummanzed in Part !!! of this document. - In panicular. Siet: . will provide copies of their Q A documents to GE. upon request, for review and approval xknowledges GE's nght to pertorm an audit to venfy the appleauon of the Test Quahty Plan .; 4ill umely noufy Enea's Responsible Test Engmeer tRTE) with documentauon of the actual test ) calendar and of any ugnificant changes in the test contigurauons or test procedures.
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A Design Record File iDRF IC & PCC) has been opened for QA record storage of documents relatmg to - the design phase. A separate DRF will be opened for the test phase, j o
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Dac = "a ' Rev l Pase l of SIET I I scuone Memun inno,sim 00098PP91 0 I 96 - 225
- 14. TEST HOLD / DECISION POINTS Enes s RTT. muss nave renewed and approved the Test Plan and Pmcedures Docurnent hefore the test program can start.
Furiner hold'decmon points. which require Enes s RTE to revies and approve the test setup. configuranon and conditiorts.are estabitshed as follows:
.it the end of the shakedown tests; rnor to starting the performance of eacn PCC test group or sub group as defined m cn.10 and 11 of this document.
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s Tali. 4 - SilWit-l' ANTilEllS: I?ull - Scale l'rototypes l'CC Test ! m Colti pre-operational Test Matrix (Notes I,2) a - __ _ . __. _._ _ j M d il.hI HilN R ESI I)EM'ltil'litlN l'liHl'OSE OF I F.Si ('OMMEN i $ f I a Vceily the P.= I's Suppist Strut turc 7 lescis to te ecsied C-01 Penets Filhng *
- 4 flow rates to be tested C-01 Ptml P Drain down Venty fewl omtiot system adeqis a'y
' lAitemme the ic>ntante of the twl,Cosmetium
{s i inc m Vestl) llom ilicht (Jlsbadisual
- Deicimme the sesne.inte of the inysium 1.me. Rnce,
- Inget enm hne umnct scd w sih C I C 03 Air Fluw theough the Hiser to the Vent Tank
- 4 llowrates to be tessed _.
Condenwr, Vent .md Dot harge i.mes 2 gwessures to be tested
- Verdy Picssure umisol system adequxy 0
- Inyt-teim i.mc connetled with CT C.04 Water Flow through the lin
- th:tcomme the resnt.ince of Diam Lenc ._
of snodule I to the
- Temsnias y lecd wates hue unmu ted in Condensate Tank; 4ic Iiow - Vcuty level umtiol system adequ.a y molute I uppen header to the Riser med tu the 0 {3 Condensate Tsak
- 2 pressure > and 4 mater llomsaics to be
- Venly gwessuruainm sysicm .__. _ _
tested ee O Notes:1) Pse-operautuut test, ase all umdutted w ith adapted open or t losed plant umhguratum. l
- 2) Test performant e implies that irgmrvd m>trumentation is cahbrated. DAS is operstmg and valves . ire upcsaisonal __
.h___ __.__._____._im__ _ . _ . -____u_-_.m_a_____. _____m _hA 2.%
E il I ab. 5 - Sil% R.I' AN IIIERS: l'ull - Scale l'rotoly pes l'W l est ; m llot pre-operational Test Matris (Notes I,21 g Q
*-l IiSi j HilN 15.S1 DEST HIPiloN PilH POSE (W I ESI' CONIMEN I S 3
s 11 01 Steam ihm through the Howr to the
- th:tcomme the heat knws of the Vent
- 4 Temperatures to be tesied _ _ .
VentTank I me. Intettion I ine and the Vent TanL Verity the tube bundle wall therrmnimple t abbrainins Venly Vent Tank protec __ ll 02 Steam Ilow through the Riwr to the ' Deten one the heat hnses ed the Dr.un
- 41cmperatures to be tested , ,
T 8 Condenute Tank l ine ar.d the Condensate 1 anL
- Vcoly Camdenwie Tank prureti 3 $
11 01 Steam ihm through the Pont
- Deteimme the twas kisses of the hail
- Ste.un flow at the minunum wiue tagubic Connection I ine to the Stark Cimnection ime to the Catch TanL to maniam the pi=>l bmhng umdonna Venly the Stas k Discharge t arabihty _ . . _ _
~
1504 St ady State Pesfuemame Steam . Cimform the Ste.aly State heat removal
- ti 6 kgh steam flow rate to be tested Only less n. 43 capahihty in the espected camdations
- Maumum Prenure value : 690 LPa g Omfirm the stability of Plant Parameters s
(
- Confirm the propised test procedure __ _. _
11 05 Steady State l'erformante Saturated Meawre the decrease of the Steady
- 5 Pressures to be tested Stease / Air hlisturesTed n.22 State heat removal calubehty .a Camlism the stabihty of Pbut $ {
PJeameless Cimfirm the prusuned test proceduse _ NutesIl l'ac opesatamat seus are all umdatseJ mith adapted open or tkned pbns cimfigurauon u U ,' 26 Test perfoam.uwe emphes that required instrumentainien is cabbrated. DAS is operating and valves are operatumal
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s t. ~ X Tah.7 - PART A. TESTS WITil TWO MODUI.ES Test 13 pe A.I.l .Sicatly State l'erformance - Llurated Steaml Air Mistures Te5t Cunilitions [ 22 M 5
-4
~
Iml P euu.. 5 r.se Supe *hout Steum isow Au Ilow kPo h Condenon 5 Pl P2 P3 Pd PS *C CF) Numbes bg/s Ob/s) __
. _ . _ tors Ob/s) r 194 33 418 83 542 33 666 33. 190 M < 10(18) 045(10) 0 064 tu tthh 2
1 14430) 0 014 (01W)) 30833 428 U 549 33 669 M 190 M < l0 Q8L _ 308 33 428 83 549 33 669 83 190 33 < 40 (18) 3 25(553 0 021(0 (W)) 0021 (00mi 31833 428 &3 549 33 . 669 &) 190 33 a la(l83 4 5 3 6 (8 D) 5 (68 0) 0 021(0 0614 0021 (0(WD 318 33 42883 549 U 669 83 190 33 308 33 42883 549 33 669 43 190 33
< 10(18)
< 10(18) h
{ , 6 51(125) < 10 (18) -o ,3 1 66(145) 0 021 (0 0m) 308 33 428 83 540 33 669 &3 190 33 _ 8 1 44(30) 001J t016) 294 33 418 33 542 33 666 83 190 33 < 10(18) 3 $
~
308 33 428 83 549 33 669&3 190 33 < 10(18) 9 50(150) 0 016(0 11) 0013(01') 308 33 428 83 549 33 669 &3 190 33 < 10(18) e to 5 / f t2 5) 66(145) 0013(01.) 308 33 428 83 549 33 669 83 15"3 33 < 10ils) _ Il 239 33 313 3 381 33 461 33 535 33 < 10 ( 4 8) I? 045(10) 014(036) ' ~ ~ 0 14(O 31) 294 33 384 33 413 83 563 33 653 33 < 10(18) 13 25(55) < 80(18) 14 36(80) 0 la (0 31) 294 33 418 13 542 33 666 33 190 33 294 33 all33 542 33 666 33 190 33 < 10 (18) m l i 45 50(1103 016(035) C
- 014(031) 301 33 421 33 542 33 666 33 190 33 < 10(18) 16 6 o tta 5) < 10(l8) 11 25(55) 036(019) 213 33 356 33 438 33 521 33 604 33
- 281 33 315 33 463 33 551 33 639 33 < 10(18) 18 5 d 618 0) 0 4 t (090) ~
j 036(019) < 10(18) 19 51(125) _. 294 33 384 33 413 83 563 33 653 33 ' 280 33 363 33' 445 83 528 33 oll 33 < 10(18) 20 5:38 0) .059(129) - N ! 281 33 315 33 463 33 551 33 639 33 < 10(18) 059(129) 21 6 6Jt4 *d 0 86 (l 9) 198 33 262 33 325 E3 389 33 453 33 < 10(18) 8 l , 22 34(307 < 10(18) Sillo) 086(19) 260 33 341 33 422 33 503 33 584 33 23 < 10(f 8) 24 51(125) 086(19) 266 33 349 33 438 83 . 514 33 591 33 _ _ 280 33 363 33 445&3 528 33 611 33 < 10(18) 25 66(845) _ ._ 086(19) 225 33 294 33 363 33 432 33 Sol 33 < 10 ( t 81 26 25(55) 10B(2 31) N 239 33 3l3 33 381 33 461 33 53533 < 10(18) 21 3 N80) 108(231) 253 33 .329 33 40483 480 33 556 13 < 10 (18) O , 28 50(11 Os 106(231) ., 260 33 341 33 42233 M3 33 584 33 < 10(f 83 ' ' 29 51(I25) 108(231) l 08f 2 31) 266 33 349 33 431 &3 514 33 591 33 < to(18) _ l I [ 30 66(l45)
-m n - m,,., ..e.- ,,,,.g., ,.,a__,.n-o_,w,,,,. .-n,. ,,,..,,w--..n..,-- ,,e,.,---v s y-,., .,,,,,w.,,,.,,,., , , . . - - , , , ,.,,.-.n.,..,,,,,a~,,-6.+,n , u. .. _ . , , , _ _ _ _ _ _ _ __ ,
i' 1 i $ 9 Tali. 8 - PAltT A - TESTS WITil TWO MODUl.ES Q t est I)5w A.I.I. Steady Staic l're f.,emance . Superheated Steam t Air Mistuces Test Condituens g i 3 Test Range of Inlet Pressure _. Steam I/ low Air Flow kPa Superheat Conditism Number kg/s (th/s) kg/s ilh/s) Pi P2 P3 P4 PS *C (*F) _ 428 5 669 5 790 20 (36) 31 2.5 (5.55) 0.027 (0.060) 308 5 19 z g 32 2.5 (5.55) 0.027 (0.060) 308 428.5 549 669.5 790 30 (54) g 3, 790 20(36) 549 669.5 308 428.5 33 66(l4.5) 0.027 (0.060) 790 34 f 6 (l4.5) 0.027 (0.060) 308 428.5 549 669.5 30 (54) 5 5 I l .0) 0.83 (l.83) 260 341 422 503 584 20 (36) 35 36 5 (l 1.0) 0.83 (l.83) 260 341 422 503 584 30 (54) g g.
._ w l
l
5 1 w Tab. 9 - PART A . TESTS WITil TWO MODUllS i E6 Test Type A.I.3. Steady State l'erformance - Sicam Only. No air in ITC tubes Test runditions Test Steam I< low Air I' low Supca heat _ Cundition kg/s Ohls) kg/s Ob/s) *C (*F) Nuenher ___ 37 0.45 (l.0) 0 (0) < 10 (l8) - 38 1.4 (3.0) 0 (0) 0 (0)
< 10 (18)
< 10 (18) l [j 39 2.5 (5.5) g -
40 3.6 (8.0) 0 (0) < 10 (18) - 41 5 (11.0) 0 (0) < 10 (18) 42 5.7 (12.5) 0 (0) < 10 (18) _ 43 6.6 (14.5) , 0 (0) < 10 (18) 44 1.4 (3.0) 0 (0) 15 (27) ,
=
45 1.4 (3.0) 0 (0) 20 (36) 46 1.4 (3.0) 0 (0) 30 (54) _. 47 5 (11.0) 0 (0) 15 (27) 48 5 (11.0) 0 (0) 20 (36) @[ 49 5 (11.0) 0 (0) 30 (54) n-- , -- y w w W e--* m y e _ - - ' - - - _ -- - - _ _ _ .
8
^
Tab.10 - PAltT A. TESTS WITil TWO MOI)UI.ES x m Test T 3pe A.I.3. Sicady State Performance-Steam Only. Air in PCC tubes Test Conditions j ._ Q H Test I Steam Flow Air Flow Superheat i Condition kg/s (th/s) kg/s (th/s) *C (* F) ___. Number 50 14(30) very low < 10 (IF.) 51 5 (11.0) very low < 10 (18)
, f.
3 52 1.4 (30) very low 20 (36) . 53 5 (11.0) very low 30 (54) _ j e a ! t m_m--_mu -_m- _ _ _ m____ __-_T- __ _ _ _ -m _m._m__.-+-m v -
-.-are6 4 e% .. . _ a --.me-m-w_-ree- ri--s.i-.-s,v-1 a w . , . . .w-_-+ a-br ..-ev -- _m=a.-_ ___m_____. --__ __u____..-- _m --
Tab. 11 - 1%ItT A. TESTS WITil TWO MOI)UI.ES Test Type A.2.I . Effect of Pool Water I.evel-Saturated Steam k $ Test Type A.Z.2. Effect of Pool Water I.esel- Saturated Steam / Air Misture 5 Test Conditions {s Supes heat 3 Test Steam Flow Air Flow Range of Inlet Pressure i Condition kg/s tib/s) kg/s (th/s) kPa
- C (* F) ~-
Number 54 (41) 5 (11.01 11 ( 0 ) (dependent vanable) < 790 < 10 (18) g _ ___ q g 3 a i 55 t15) 5 tiI II) 0.14 (0 31) (stasi at 294 stop at 790) < 10 (18)
~
56 (301 b 6 (14.5) 1.08 (2.37) (stant at 266 stop ai 790) < l0 (l8) ; d m sm. M hE _-mm_ m__._.__-. . _ ____-_-_ _ -__ =-t,-w u.e,,,,u ,+..e,,,w[. 4 ,. a, ~ -s . .y e, m.i-,w~,- , a- e w ,,w .. . . - . . , ...%...,
5
- w I E4 I
Tab.12 - PART 11. TESTS WITII ONE MOI)UI.E -- Test Type 11.1. Steady State l'erformance-Steam Only Test Conditions No air in I'CC tubes Test Condition Steam Flow Air Flow Superheat 5 f 8 Number kg/s (th/s) kg/s (th/s) *C (*F) 0 (0) < 10 (l8) 3 E 66 (37) 0.23 (0.5) 67 (38) 0 6M (1.5) 0 (0) < 10 (18) 6M(39) 1.3 (2.8) 0 (0) < 10 (18) _ _ 69(40) I.8 (4.0) 0 (0) < 10 (l8) . 70(41) 2.3 (5 0) 0 (0) < 10 (18) 0 y* 7l(42) 2.8 (6.3) 0 (0) < 10 (l8) 72(43) 35 (7.7) 0 (0) < 10 (l8)
- m
e i I $"1 H 4 5 Tah.13 - PART 11. TESTS WITil ONE MODUl.E - Test Type ll.l. Steady State Performance-Steam ()nly Test Cunditions. Air in PCC tulics S S 5 Uest 3 3 Cundition Steam Flow Air Flow Superheat - Number kg/s (th/s) kg/s (th/s) *C (*F) 73(50) 0.7 (1.5) very low < 10 (18) -- 7-1(51) 2.5 (5.5) very low < 10 (18) o y w< -- N ,.,2- g_ - _ __m- _ ___2-___ ___-__am
i i I E! M I _ -4 I ! Tab.14 - PART 15. TFST WITil ONE MODUIE Test Type B.2. Effect of 1.nw Density Noncondensibles Test Conditions 5 .
% 5 Steam Flow Air Flow liclium Flow Superheat ! I Test _
kg/s (Ib/s) kg/s (Ib/s) kg/s (Ib/s)
- C (* F)
Condition Number - - 0.7 (1.5) 0- (0) very low . < 10 (18) 75 76 2.5 (5.5) 0 (0) very low < 10 (18) 77 0.7 (1.5) 3.4 x lie flow very low < 10 (18) o { 78 2.5 ($ 5) 3.4 x lie now very low < 10 (18) 55
% m:
__._.__..___..______n__._________. __a'. _ . . _ _ . . _ . . _ _ _ _ . . . . __ . . . . , ... ..1,... .,-#,,. , , . ~ ...--,........,,-..._......e_ . . _...,,, .~.___ _ .._.__, _
I
~
j Documet -l. Rev. Page of SIET senone demian innovaim ' is109RPP91 - 0 108 + 225 i i PART II: TEST PROCEDURES TABLE OF CONTENTS
- 1. INTRODUCTION 111
- 2. VERIFICATION OF STRUCTURAL CAPABILITY OF POOL SUPPORT STRUCTURES TEST C-01: PRE. TEST CHECK LIST 112- 3 2,1 Venficauon of structural capabdity of pool support sovetures test C-01:
TEST PROCEDURE !!4-121
- 3. POOL MAKE.LP SYSTEM VERIFICATION TEST C-02: PRE TEST CHECK LIST 3.1 Pool make-up system venfication test C 02: TEST PROCEDURE 123
- 4. AIR FLOW TEST C-03: PRE TEST CHECK LIST 125 41 Air flow lest C-03: TEST PROCEDURE 127
- 5. WATER DRAIN TEST C-64: PRE TEST CHECK LIST 130 5 i Water dr:un test C-04: TEST PROCEDURE 132 ,
m
~
- 6. HEAT LOSSES IN INJECTION LINE. VENT LINE AND VENT TANK TEST H 01:
PRE TEST CHECK LLa ( 135 a 5.1 Heat losses in insecuon line. vent line and vent tank test H-01: ' TEST PROCEDURE 137 HEAT LOSSES IN DRAIN LINE AND CONDENSATE TANK TEST H-02: ' PRE TEST CHECK LIST 140
- 1 Heat losses m drain line and condensate tank test H 02:
142 TEST PROCEDURE i 4 HEAT LOSSES OF POOL CONNECTION LINE TO THE CATCH TANK TEST H 03: PRE TEST CHECK LIST 145 ! 41 Heat losses of pool connecten line to the catch tank test H-03: )' 147 TEST PROCEDURE l J 149 9 STEAM ONLY TEST H 64: PRE TEST CHECK LIST 0i Stearn only test Hot: TEST PROCEDL%E 151-I i i
Doc ==*
- Rev Page of SIET l l
' 00098PP91 i 0 109 225 senone Nennon innm' arm i
153
- 10. S ATURATED STEAM / AIR MIXTURES TEST H.45: PRLTEST CHECK LIST 155 10.1 Saturated steam / a.r mtstures test H.05: TEST PROCEDURE 159
- 11. TEST TYPE A.t.1 -S ATURATED STEAM / AIR MIXTURES: PRLTEST CHECK LIST 161 11.1 Tes type A.I.! - Saturated steam / .ur mistures: TEST PROCEDURE
- 12. TEST TYPE A.I.2 SUPERHEATED STEAM / AIR MIXTURES: PRE TEST CHECK LIST 166 168 12.1 Tes: type A.I.2 - Superheated steam / air mixtures TEST PROCEDURE 172
- 13. TEST TYPE A.13 - STEAM ONLY (NO AIR IN PCC TUBE): PRE TEST CHECK LIST l
174 13.1 Test type A.I.3 - Steam only iNO AIR IN PCC TUBE): TEST PROCEDURE 176
- 14. TEST TYPE A.1J STEAM ONLY ( AIR IN PCC TUBE): PRE TEST CHECK LIST 178 .
14.1 Test type A.I.3 Steam only ( AIR IN PCC TUBE): TEST PROCEDURE
- 15. TEST TYPE A.2.1 EFFECT OF POOL WATER LEVEL- SATURATED STEAM: 180 PRE TEST CHECK LIST !
15.1 Test type A.2.1 Effect of pool water level Saturnied steam: 182 TEST PROCEDURE
- 16. TEST TYPE A.2.2 EFFECT OF POOL WATER LEVEL - 184 SATURATED STEAM / AIR MIXTURES: PRE TEST CHECK LIST 16.1 Test type A.2.2. Effect of pool water level Saturnied sicam / air mixtures:
186 TEST PROCEDURE 189
- 17. TEST TYPE A.3.1 SIMULATED LOCA PRESSURIZATION: PRE-TEST CHECK LIST 191 17.1 Test type A.3.1 - Simulated LOCA pressuruauon: TEST PROCEDURE 193
- 18. TEST TYPE AJ.2 SIMULATED LEAK TESTING: PRE TEST CHECK LIST 194 18.1 Test type A.3.2 Simulated leak testmg: TEST PROCEDURE 1%'
- 19. TEST TYPE A.4 PRESSURE LOSSES AIR ONLY: PRE TEST CHECK LIST 198 19.1 Test tp A.4 - Pressure losses air only: lEST PROCEDURE
- i
N ="' Reo Page of SIET ! l (WYNRPP0 f > 0 110 l 225
-coone Newton freum 200
- 20. TEST TYPE B.1 STEAM ONLY INO AIR IN PCC TUBEShPRE. TEST CHECK LIST 202 20.1 Test type B.1 Steam only iNO AIR IN PCC TUBEL TEST PROCEDURE 204
- 21. TEST TYPE B.1 STEAM ONLY ( AIR IN PCC TUBEShPRE. TEST CHECK LIST 206 21.1 Test type B.! Steam only i AIR IN PCC TUBEt TEST PROCEDURE
- 22. TEST TYPE B.2. EFTT.CT OF LOW DENSITY SON CONDENSIBLES: 208 PRE. TEST CHECK LIST 210 22.1 Test type B.2 EfTect of low Density Non Condensibles: TEST PROCEDURE t
e
D ( * *' Reo Page of SIET I i l l enone desion twaim 'VK98PRI i o til i m
- 1. INTRODUCTION L
Dns part of the TP&P document reports on the pre test check itsts and detailed procedures of cold and hot nakedown tests. and on the pre tests check hst and detailed procedure of experimental tests foreseen for P OTHERS PCC fxdity. For similar test. belonging to the sarne group or subgroup only one per test check list and one test prtredurt n repried for exh group or sub-group; exh test of the sarne group or sub-group has different PCC inlet
.onditions. but all the tests are performed in the same way.
t I
Rn Page j of SIET i D ' "
- I l
~
8 009MPPol
' 0 ll: 225 u mme xemian innovoim P ANTHERS PCC PRE. TEST CifECK LIST Pap _.Lof_2_.,
Tsale Verttiration of Structural capability of cool succort structures Test n Q-Q), Descriptco Note Status Oper. Phase s i - - Signat. I 10 i Venfy that the plant configurauon is complete and suitable I t'or the scope of test C 01 Venty the correcteness of installauon of sinsctural Instruments 20 instrumentation. LDT 011. 012. 013. -014. -015,4)l6. 017 supplied and installed tw 4 EMME company i 30 Venfy that the following instrumentauon has been calibrated, mstalled, filled vented and is in operation : F M001. F.R001. L-Q001. L-Q002. L P001. LDT.Oll. - 012. 013. 014. 015. 016.-017 40 Venfy that the Data Aquisition System is operational and
, the conversion costants and formulas have been correctly 1 inened in the D AS I F035 and 50 ! Venly that the followine valves :.re closed F036 are not
.FO:7 installed
! F028
.F029 F030
.F031
*FO':
.Fnta F035 F036 I
60 l Ventv that the tollowing salves are open
.F033
.Fnd%
70 Venfy that the Iollowing tanks are f ull i MIOl. A002. A003 40 Ventv that the pump C004 n available
.. i m
Doc "= Rev Pate l of
) l SIET !
f(yNRpp4] O l ll3 4 3
-caone M estari intmeirvi PANTHERS PCC PRE. TEST CHECK LIST Pqe,l_of_2 rune t'erracorron of structural cavability of cool sunoort structures Test a C.-QL Newe Date Espenment Mannaer Sigasture e
Doc "' ' Reo j Page l of l SIET i 225
*(XMPPol O + 114 senone demian innovsovs PANTHERS PCC TEST PROCEDURE Pnse Lof_2 Title VmHcation of structural canability of 0001 suDoort structures Test s Q Descriptu>o l Note Status l Oper.
Phaw i I I Signat. s 10 I Start the w ater suppiv pump C004 20 li Open salve FD26 till to reach the maximum flow I 25 Measure water flow rate F.M001 30 f When level L-Q001 s I m. stop pump C-0CM and close valve F026 T1us durauon can be changed 40 Measurt dtsplacements dursna the test
- LDT 011. -012. 013. -014. 015. -016. 017 everv 30 s for 30 minutes Table witn suowable 50 Compare the measured values with allowable deformauon dtspiacement shown in table should be i attached to stus
! Check List i
i 60 j If any measured deformation is a the correspondent i allowable value then stop the test and drain the pools P. Q c!se continue "O Venfv the leakare from the pnot P Q K0 ! If leaiste is > l g/s then stop the test and drain the pools P. O else conunue I f 90 i Stan the water suppiv rump C004 t 100 f0 pen salve F006 0 11 to rexh the maximum flow i t 110 ! when level LQ001 a 2 m. stop pump C0(M and close valve FO:6 ! l l l 1 l
Docua R" Page j of j { SIET 1 W W PP91 0 !!5 5 22.5 i seuene Nearmn inno*sim PASTHERS PCC TEST PROCEDURE Psse lof I , i Tisse \~er16 cation of structural caDability of Dool suonort structures Test a C .Q.L Desmptmo j Note j Status j Oper. , Phee i ; I I I Signat. l s I
! l 120 ' Repeat phase 40 I I I l I I I IM ! Reveat phase 50 l Repeat phase 60 l f f 140 i l l l .
150 ! Repeat phase 70 160 Repeat phase 80 170 Stan the water suppiv pump C004 180 Open valve F026 till to reach the maximum flow 190 when level L-Q001 a 2.5 m. seco pump C004 and close
- s alve F026 l f 200 i Repear phase 40 210 Repeat phase 50 '
l l l l I I i 2:0 Repeat phase 60 230 Repeat phase 70 l I I l ; 240 i Repeat phase m0 l
?.!0 ' Stan the water surpiv pump C004 i
r ) 260 Open sahe F026 till to reach the maumum flow
\
270 when level LVOI a 3 m. stop pump CON and close valve i
! FT126 2A0 Repeat phase 40 J
*=a' Reo l Page j of l SIsT i I I
trKmlPP91 0 > 116 i 22.5 secone Remian Innovaim 1 I P ANTilERS PCC TEST PROCEDURE Page lof_2 Title Veri 6 cation of structural caDabilttY of Dool suDoort structures Test c M Desenptu>n Note Status Oper. Phaw s %,. 290 Repeat phase 50 l l l
. I 300 i Rcpese phase 60 310 Repeat phase 70 320 Repeat phase h0 330 . Start the water supply pump C004 340 Open valve F026 till to reach the maumum flow 350 When level L-Q001 a 3.5 m. Stop pump C008 and close valve F026 I l I I I 360 ' Repeat phase 40 I l l l i f f 370 ! Renest phase 50 380 Repeat phase 60 i l l l 30 Renesi chase 70 I
4a0 Repeat phase MO i 410 Stan the w aier suppiv pump CON [ 420 Open salve FT)26 till to reach the maximum flow i ! 430 l Fn26 when level L.0001 s 4 m. stop pump C001 and close valve l l l u0 l Rencai enase 40 i Revesi pnase <0 I i l 450
D" = ' ' Rev l Paae of SIET I I secone gention inrealm htXNRPP91 - 0 !!7 i m PANTHERS PCC TEST PROCEDURE l l Pase i of_2 l l
\
Title L'erttiration of structural CODabiliti of D001 SUDDort structures Test c M Descripuos Sote j Status Oper. Phee ; l f Signat.
' l_
8 460 Repeat phne to 470 Repeat phase 70 4A0 Repeat phase 50 490 St.vt the water supptv pump C004 500 Open valve F026 till to reach the maximum now $10 When lewt L.Q001 24.5 m. stop pump COLM and cime valwe F026 5:0 Close hand valve F033 This dursuon can Measure displacements a be changed 530 LDT-011. -012. 013, .014, .015, .016. 017 dunng the test everv 10 s for 10 minutes f40 Repeat phase $10 after 16 h Open i or both the
- d ves.
550 ll Open hand valves F029. F028 acccraing to the I manunum l flow i disc harge
! raie achievable 560 Measure and record now rate F.R001 570 When level L.0001 a 4 m. close valves F028.
I. I: FO 9 lhe ourauon can i he changed 580 Repeat phase 40 ac cording to the results td the l loadtnt phase i I
haa' Rev Paste of SIET l I l rOO98PPol o ' l18 i 225 senone Wesuri inrioveuvi PANTTIERS PCC TEST PROCEDURE Page _1.of 2 Tisse Verincotton of structural cavability of cool succort structures Tess n GQL Desenptu>o l Note 5tatus l Oper, Phaw }' ' i Signat. s Open i or tuxh the v alves. 590 l Open hand valves F029. F028 accanang to the matunurn dacharge flow l rate achievable i i i 600 i Nicasure and record now rate F.R001 1 610 t When level L-Q001 s 3.5 m. close valves F028. F029 The duranon can
.he changed 620 Repeat phase 40 Ecorthng to the results of the loadma phase Open I of tun j the valves.
630 ! Open hand valves F029. F028 according to the i rnasunum t dacharge Cow rate achievable I M0 Nicasure and record Unw rate F.R001 i 650 I when level L-Q001 a 3 m.close valves F028. I I Fn29 The oursuon can be thanged 660 { Repeat phase 40 accading to the results of the J
. Ioading phase Open 1 or hotn the v alve5.
I Open hand valves F029. F028 670 acccadarig to the I matunurn docharge now f fate arruevable I 6go I Nicasure and record now rate F.R001
- - ~. .,
D**"* Rec- Page i of SET ! I _ 0009 APP 91 8 0 l 119 225 scraone Hemun innovssrvi PhNTHERS PCC TEST PROCEDURE Page.jLaf.2 Tosse Vertfication of structural canability of cool suonort structures Test a C-Q.1, Descripuoe Note Status Oper. l Phee l ' I Sisant. i 690 When level L-Q001 a 2.5 m.close valves F028. F029 The durauari can
- Sh*^8*d 700 Repeat phase 40 accarthng to the resuku of the loadma phase Open I or txan th* * *1"*-
710 Open hand valves F029. F028 accehng . to the mansnurn decharge now rste achievable - 720 Measure and record now rate F.R001 l 730 When level L.Q001 a 2 m.close valves F028. F029 The duranon can be changed 740 Repe:t phase 40 accordmg to the resulu of the loading phase Open i or botn th* * *1"5 - 750 Open hand valves F029. F028 accmdarig to the matarnum discharge Dow rate schwvable I l . 760 1. Measure and record flow rate F.R001 770 When level L.QODI a i m, close valves F028. F029
~ h"a' Rev Pate of SIET I l l l iu rNRPP91 0 l 120 i 225 c wne demum twum PASTHERS PCC TEST PROCEDURE Psse 2_ofd risse Veriticanon of structural cavabihty ot'vool sanoort structures Tess n GQL Descriptsaa Sote Oper. Phaw # lI Status lI Signas a The aurauon can w cnangect 750 Repeat pnase 40 readtng to the results ci the loadinr phase I l l i Drain the pools P O l I '00 The curauon can
- chan8888 R00 ; Repean phase 40 accadmg to the results of the loadtng phase N <d e Date Experiment Manager Signature ,
e4 l e r--
D ''' R" Page l of SIET I I ! I M RPP91 1 0 i 121 1 225 sc.uine demian innovaim P ANTHERS PCC PRE. TEST CHECK LIST Page_L.,of 7. f.tle Pool Make un System Veritication Test n C-Q1 Descriptma Note Status Oper. Phaw s l SittaL I 10 Venfy that the pel suppon structure is suitable to perform test C-02 i 20 I'InrVenfy that the scope the of tes plant conngurauon is complete and suitable C-02 30 f Venfy that the following instrumentauon has been
' cabbrated, installed filled. vented and is in operation:
F M001 F.R001
. L Q001 L-Q002
- L P001 T M001 T.R001 i
40 I Venfy that the Data AQuasillon System is operatonal and j the conversion costants and formulas have been correctly I nsened i in the D AS F035 and 50 Venfy that the following valves are closed: F036 are not
.F028 installed
! F029 ,
! F031 1 i.F032 l l FOM l
, FU35
{ F016 60 l Venfv that the following valves arc open l*F027
, F030 l F033 i . Fn.1 %
I 1 l l
. i d
I i
~'
D """* ' R Pass l of
! l SIET i trXN8PP91 0 122 1 225 _j cuane Meanon innovoim P ANTHERS PCC PRE. TEST CHECK LIST Pase_1 ofL Torne Pnni Sfake-im Synem VertRcanon Test s C&2 Dexnpreon . Note States Oper, ihw a l Signet.
1 6 'O I Venfy that the fo!!owing tanks art full l
- A001 A002
'*A001 i Venly that the touowuist control system is available:
80 1 LIC-0001 90 Venfv that the pump C004 is available Note lbte Espenment Mausser hignature
R= "' R Pat of SIET I I l l coone Neanon innovauvi tr @ 8PP91 1 0 1:3 i m P ANTHERS PCC TEST PROCEDURE i PageJ_ofj Tisle Pool Make.un System Vertncation Tess a C-Q2 Note Status Oper. Descripesoe Phase l . Signet. 8 I Dus value can be l Set up the pool Q level control LIC 0001 to 4.2 m chanted dunas 10 f he itst i l l f 20 I Start the water supptv rump CON Dus value can be changed dunns 25 Fill the pools P. Q to levet L.Q001. L P001 = 4.2 m the test Open 1 or txsh th' *alves 30 Open and regulate the pool P drain valves F031 F032 to *c"*"8 to th' obtain a docharge now rate F R001 = 1.0 kg/s dacharge ac= rate achsevable i 40 Yensure and record: ) 4
- F M001. F-R001 4 L-Q001. L-Q002. L MK)I 4 for 600 s 4
50 Ad. rust the parameter of controller LIC-Q001 to optimate the level controi l 60 Regulate the pool P drain valves F031 F032 to obtain a i discharse now rate F.R001 = 10 kg/s ! It could he l necessary to 70 ; Repeat phase 40 adpust agaut the j conociner l l parameters as in l phase 50 I M0 Regula!c the pool P drain valves F031 F032 to obtain a discharte flow rate F.R001 = A 0 kefs l it mund he l ne:casary to 90 Repeat pnase 40 adjust agagt the cmue16er I parameters as in j phase 50 100 Regulate the pool P drain valves F031 F032 :o obtain a
; discharge now rate F.R001 = 9 0 kys or the maximum ic hievable.
w-
1 l I Doc " = = Reg l Page l of SIET i ! i *3
*( W PF91 . 0 13 econe xeanan inno mv' P ANT 11ERS PCC TEST PROCEDURE Page _] Lor
- Tinne Pool Make-ton System VertReation Test s @
. Note O per.
Descriptsoo Status fl Signat. Ptutw { 8 3 it cou6d he nercuary io !10 f Repeat phase 40 adf usi agam the controtkr l palecten as in phase 50 Nrwe Dale . Experiment Manager signature I l l i
Dwumem l Rev Pate of SIET , l } eacne vemum Innovanvi rin008PP01 i n 13 4 23 P ANTHERS PCC PRE-TEST CHECK LIST Page-.Lof_2 T,tse Air Flow Test Tess s .C-Q1 Desenption Note { Status Oper. Phase s i l I I I Sisant. 10 Venfy that the plant configursuon is complete and suitable for the scope of test C-03 20 Venfy that the fouowing instrumentauon has teen calibrated, installed. filled. vented and is in operauon: I F-2001. P-2001. T. 2001 F-TD01. P.TD01. T.T001 P 4001. P 1002 L-LOGl. L LOO 2. P.L001 DP-001. DP402. DP-003.DP 0GS. DP-005 DP406. DP-007. DP 008. DP 009. DP-010
- DP411. DP-012. DP 013 DP-014. DP-015. DP-016. DP Ol7. DP-018.
DP.019. DP420. DP-021. DP422. DP-023. li DP DP-024. 030. DP-026. DP-027. DP-028. DP-029. P A001 I P-C001 I 30 , Venfy that the Data Aquisition System is operatonal and the conversion costants and formulas have been coritctly inserted m the D AS All the purse
, I
* * *nt * *
- 40 ! Venfy that the tollowing valves are closed: must be sk:nc i
4 F001. F002, F003. F011. F013. F015. F017. F018 I F023. F025. F017. F01R. F41. F047. F0aR i 50 I Venfv that the following valves are open I
! F009.F020.F039.FGad.F089 I 5Fn01 SF002 i {
60 ; Venfy that the following safety valves are set at i MPs: F016.F050.FOa0 < 1
! and the valve F441 is set at 4 MPs 'O l' Venf v that the air compressors C002. C003 are available
l i i
~
Rev j Page of Da' "* 1 l SIET > itKNRPP91 0 126 225
-c z.one w eston inno sis" P ANTilERS PCC PRE.TFST CHECK LIST Pagelofj Test a C-Q}
Tisie Air Flow Test Dewrapex>o Note ()per. Pnase s l l StatusI l Signat. RO Venfy that the following control systems are available:
' PIC-#02 I i* FIC 2001
%we i Date . Esperiment Manater Signature 4 I
Rn Pau j d SIET l Dac =""' I l (WINRPP91 1 0 i 127 1 225 semne demon Irwaim , PANTHERS PCC TEST PROCEDURE PEEt L.d 1 Tess a C.:D.). Title Air Flow Tests Sme l Staans Oper. Descripuoe Phaw { f Signat. ,
)
8 f 10 Open the valve F0it and fill the Condensate Tank to rexh level L LB02 = 175 m f 20 I Start air compressors C002 C003 l l
! i 25 i Set P!C 1002 at 281.3 kPa M Set FlC.2001 at 0.10 k rjs j Wait to stabtitze the inlet pres we P4002 arid Gow F 2002 10 I f steadv staten I 50 Measure and record all instruments for 1000 s It changes the-onfia measunns 60 Close valve F-039 and open valve F438 the utlet flow rate 70 Set FIC.2001 at 0 3 kt/s R0 Wait to stabilize the inlet pressure P4002 and flow F-2001 I 15teady %tatel 90 Rereat phase 50 i
I. 100 i Set F1C 2001 at 0 6 k r/s 110 Repeat phase 80 120 Repeat phase 5n About i kg/s IM l Set F1C.2001 at the manimum now rate available 140 Repeat phase MO 150 Repeat phase 50 160 Set PIC 1002 at 701.3 kPa i t i I i 170 I Repeat phase in
Da( = = Rev Page j of SIET ! 1 l 0009ftPP91 0 8 128 , 225
<none wearson inno nov' PANTTIERS PCC TEST PROCEDURE Paze lofj iess a C-03 Tit!r Atr Flow Tests Dextiption Note Oper7 Phase , I I ! Statusstr t.
l 11 shanges the g I m6ce measunns 180 , Open valve F439 and close valve F-038
' I the inlet Oow rate 190 Repeat phase 40 200 , Repeat phase 50 lt Changts the m6ce measunns 210 Close valve F039 and open valve F438 the irdes Co= rete _
2:0 Set FIC.2001 at 0.3 kgjs l
} I 230 I Repeat phase M0 240 Repeat phase 50
! l i e0 i set FiC 2001 at 0 6 Ws l
260 Repeat phase m0
!?0 Repeat phase 40 m i s e, Fic.:00i a,ine mamum n-ie avesie l^""** l l i i i i f I i
290 ' Repeat phase =0 i I l I 40 1 Repeat phase 50 l l f i10 I Tom oif the air compressors c002 cn01i l l i l I 1 3:0 ' Deprestunte the svuem 4
*****' Rev Page of SIET i l scoone weation tesem n009MPP91
+
0 f 129 23 PANTilERS PCC TEST PROCEDURE Page lofj Titu Ag , !aw Tests Tess o @ %ote Date Espenment Manater Sirmature
i 1 D* * * " ' Reo Pase j of SIET ! I i 215 er;onc demai Inrealm GNPPI O 1.10 1 I l l l i P ANTHERS PCC PRE TEST CHECK LIST 1 Page ,Lill Tess a C-M Tisle Water Drain Test Sote Status j Oper. Descriptare Pbaw a l I I 9 tant-bec ause Itus 3** d 10 Venfy that the plant configurauon is complete and suitable * *5" " Y ior the scope of test C-04. in parucular inat the temporary 2* ""'8 'h*" "
; wh 40 feed water ime connects line M mefore the valve F- ,g ,
0.14) and the Upper Header A. nozzje A i enu. it is new shown in the I PAID I 20 l Venly th:1 the f ollowing mstrumentation has been j calibrated. installed. filled. vented and is m operauon: l l P 2001. F 2001. F 2002.T 2001 i P 4002. P A001. DP 026. P.C001 DP-017. DP4)l9. P 5001. DP-029 P-L001.L LOO 2.L LOGI.F LOGl T LOO 5 DP-024. F M001. T-M001. DP020. DP-Ol 8 i DP-- 016 1 30 ; Venfv that the Data Aquisition System is operational and
' the conversion costants and lormulas have been correctly inwned in the O AS .
40 [ Venfv that the following valves are closed:
} F001. RJ25. F011. F037. F018 l' SF002. F033. F034. F013. F021 sTru t . Fn46 F01R. F026 f I
f0 ! Veniv that the f ollowine valves are open l 1 Fn44 F039.F009 SF001.Foli F015.SF001 l e.0 , Ventv that the followine safety valves are set at i MPs: l
; F016.F050 l j and the valve Ru3 is we at 4 0 MPs i
70 l Veniv that the followine control svstems are swastable: j LIC-LOGl. PIC.LOGI
.. i 1
1 i l l l
~~ Document Rev Page of SIET i rOO9MPP91 0 131 2 15
<oww Memen innovum i P4NTilERS PCC PRE TEST Cl{E.CK LIST Page_2.of_2 rutse Water Drain Lt,u Tess s .C-Q4_
Desenpaos Note Status Oper. Phase # l Situat. l M) Venfy that the pump C0f>4 and the air compressors C002 C003 arr svulable Nene 1 Date Espenment Manager Sigasture l l J I l l 1
9
. Doeinmet j Rev Page of SIET i i 0 132 l 225 cocne kcanon innoveuve - M RPP91 t
PANTHERS PCC TEST PROCEDURE i Pap l orj ; Teen e C-Qf. , riae Water Dram Test ! I Description Note Semes Oper. Phase l Sisset. s 1 10 ' Set LIC-LODI m manual mode and fuuy open pneumauc i I valve F019 Discharp of CT l l is fan the 20 { 5 tart pump C-ON and fil! Condensate Tank to reach level Pipe. 1 L-LOO 2=1.75 m awhen this level is rexhed. the water starts
' to drain m line L through F-LOGI
**h ',' '
Pressure is u
*M888 W ,
30 Set P!C L001 m automaue mode and ses pressure set point and ts cans PIC-LOGI = 281.3 kPa hv RT2I welve I 40 l Start air compressor C-002 50 Open F008 and ptessurue the sysicm till to reach steady state pressure condition P '_00l=281.3 LPs UC-L401 is an 1 manual e 60 { Adjust water tiow rate F M001 = F LOGI = 1.0 kg/s. acting i on valve F-026 70 i Wait to reach steady-state llow rate F-M00l=F- , I LOO 1=1 Okius and pressure P LOOL =2RI.3 LPs i 40 Measure and record all instruments tor 1000 s ', 90 Adjust water flow rate F-M001 = F-LODI = 1.0 kg/s. acting l
. on valve F 026 I
100 Wait to reach steady-state slow rate F M00l=F-LO0l=3.0 ; k r/s and pressure P-LO0l=2R13 kPa l 110 i Measure and record all snstruments for 10n0 s 1 120 Adjust water flow rate F M001 = F L001 = 6.0 kb/s, acting on valve F 026 , 130 Wait to reach steadv-state tiow rate F M00l=F LOOlmo.0 k gjs and pressure P LOOL =2Rl3 LPs
.4 i
i
' ~ - ~ - - , . . , . _ , _ _
l l l Dac"* "" Page of MET l I l er;one desim innovaim (OO9RPP91 1 0 133 i "1 , I l. P ANT 11ERS PCC TEST PROCEDURE Pt n . of 1 Test a f,.-Q:S Title Water Dram Test Description Sote Status Oper. Phase Signet. 8
! l l i i 140 ' Measure and record all instruments for 1000 s 150 f Adjust water Dow rate F M001 = F-LOGI = 9 0 kys. xtmg I nn valve F 026 160 Wait to rexh steady-state flow rate F M00l=F L00l=9.0 kvs and pressure P Loot =281.3 kPa 170 Measure and record all mstruments for 1000 s Dacitarse of CT is from the 180 Open valve F 018 and close valve F-017 trMtom of CT I
190 ' Switch level controller LIC LODI to automaue mode and set level set point = 1.75 m 200 Set PIC-LD01 pressure set pomt = 701.3 kPa 210 Adiust water flow rate F-M001 = F LOG 1 = 9.0 kys. xtmg on valve F 026 l 220 Wat to reach steziv-state now rate F M00l=F-LO0l=9.0 l aes and pressure P LU0l=7013 kPa 230 Measure and record all instruments f or 1000 s 240 Adiust water now rate F-M001 = F LOG 1 = 6.0 kr./s. xtmg i i on vwve F426 l 250 l Wait to rexh steady-state flow rate F M00l=F LO0l=6.0
! k vs and pressure P LO0l=701.3 kPa 260 Measure and record all instruments f or 1000 s 270 Adjust water flow rate F M001 = F LOO! = 3.0 kg/s. xtmg nn valve F-026 280 Was to texh steady state 11ow rate F M00l=F-LO0l=3.0 I
L es and pressure P LO0l=7013 kPa F
D** "" ' R" Pase j of ; SIET - ' I l l riOO9RPP01 1 0 134
- 225 sencme demrin lesuvi l
PANTHERS PCC TEST PR(X'EDURE Page,,1 of 2 ; r Tess a C-Q4_ Title Water Drain Test . Desenptmo l Nase Status l Oper. Phase l i' I Sisant. 8 I 290 Measure and record all instnaments for 1000 s , 300 Adjust water flow rate F-M001 = F-LO0i = 1.0 kg/s. actrig on valve F 026 , 310 Wait to rexh steady-state flow rate F.M00l=F.LO0lst.0 kr/s and pressure P L00l=701.3 kPa , j 320 Measure and record all instruments for 1000 s I l l I Turn off air compressor C 002 I i 330 ' i I l l l I. 340 I Turn off ptmp C-int l_
% nte _
9 l
)
?
l Date Espenment Manaaer Signature f
. . . , , . - - . . ~ . . . . . . - . , . . _ - - . . . . . . . - -.
' Docu=a' Rev Paste l of SIET I l
-aone deuirn innosum f ormPPol 0 135 225 PA NTHERS PCC PRE TEST CHECK LIST Pate_. loc Title Heat Losses in Inrection line. t'ent Line and Vent Tank Tess a lt-QL Descripoon Ncte Oper.
Phase a I l Status t i O traat. 10 Venfy that the plant configurauon is complete and suitable i for the scope of test H-01: pool P Q and CT empty steam I suppdy line 1. desuperheating lines, in;ccuon line 4. PCC. l sent line 6. vent tank. line T. drain ime 5. Condensate tank. C CT Jtscharee line L are available 20 Venfy that the following instrumentation has been cahbrated. installed, filled. vented and is in operauon: P 1001. T 1001. T4001 P4001. T4002. T4003. P 8002. T 5001. P. A001 l T 5002. T-LOGl.T LOO 2.T LOO 3.T-LOO 4 P 5001. P L001. L L001. L-LOO 2.T-LOOS L-LOO 3
. DP-001. DP 002. DP 003. DP-004. DP-024
! DP.026. DP 017. DP-019. DP-021. DP 029 I P A001. DP 016. DP 018.DP-020 I DP-022. T-6001. T-6002. T-1001. T 1002 f TP1003. T001. T L 1001.
T001. PCCLfluid 1002. P 1001. and tube DP-023 wall thermocouples 30 : Venfy that the Data Aquisition System is operational and
. the t.onversion costants and formulas have been cofftctly insened in ine D AS I
40 } Veniv that the lollowmg vajves are closed:
)
F001.F002.FD03.F011.F009.F013.F017.F015.F023. l FNQ SFMs F059. FON . SF001. FN6 l
!O ' Veniv that the to!!owine valves are open: ;
j F025. FT107. F018. SF002. FD58. F04R. SFOOT 60 . Venfy that the following safety valves are set at 1.0 MPa- l F016.F050.Fmo l
; \ enf y that the touo'. wing control systems are avaltable: l
*0 PIC4002.11C 5002. LIC L001
! l l RO Venfv ihat the pump C001 is available
}
l l 90 : Venfv that the condensen are cooied CFluviale pump is in l !
"teration i
i l Rev Pate of SIET I D ' *" ' I l l
< sVFJMPP91 ' o '
116 1 225 coone Neurwi truw sim PANTHERS PCC PRE. TEST CHECK LIST Pue_1.of_; Title Heat Losses in Injection line Vent Line and Vent Tank Test a lt-Di % te __. E 1 Date Expenseat Manaaer .N irnature
Dac"* "" .Page j of SIET I L l
' 0 137 i 225 sesone Neanum Innovairvi i 4109ftPP41 i PANTHERS PCC TEST PROCEDURE Page _,,Lof_2
. Test a t{:QL Tine Hear Losses in iniection line Vent Line and Vent Tank Desertptme Note j Steau j Oper, 1 I sinnet-Phaw!
s Discharge of the l U fmm the 10 j Open the valve F019 at its mmimum value won Pressure m atmolute value 20 f Set PIC 1002 pressure set pomt = 2813 kP3 Atxmat10'C of superhea as PCC 30 i Set T1C4002 temperature set pomt =141 *C tfdel I The seam flow rate sheiuw be 40 Open valves F003. F002, f001. FD04 and open steam Dow about 0.2 ks/s. If control valve F-005 at its mmimum value compaubte with i' ddII'"3' the possibilaty to control the pressure P4002 discharging some uncondensed steam from PCV F020 "[' '" close valve F019 50 Stan pump C001. oyn valves. F059 / F0li and begm to desuperhear steam 60 Adjust steam temperator till to reach the req.ured temperature of T 1002 (fr.ut 10*C of superheat) The sicam must be superheated in 70 Decrease furtherly strarn temperature till yo have saturated the inrection line steam m the PCC u,iper headers The sicam m the PCCand upper 80 l' Wait to reach steady state condicon in pressure P 1002 2"d '" hd"' l temperature T-(COI. T-6002. T T001. T-t002. T-t003.T.
- A001.T A002.T D001.T-D002 I;Ondit DDRs 90 l Measure and record all instruments and plot water level in I vent tank versus time for 1200 s 100 Set PIC4002 pressure set pomt = 501 t kPa AboutIU"C of superheat at PCC 110 Set T1C4002 temperature set pomt = 162*C nn}et 120 Repeat phases 60 and 70 1
1l
.. )
Page j of l R a m'cua' I l i
! .ui 4 23 a SIET _ _ 0 4 irryappol omne xcuinn inno um j
P WTilERS PCC TEST PRm*EDL.'RE Page 1.,o(J Tess n H-D1 i d Vent Tank t,tse l{ eat Lorses in internon line Vent I ne an Note Status Oper. '
%gnst.
Descripten Phaw f The sicam in vent ( f E ime must tie ai
/
wait to reach steady state condsuon 002 m pressure
"d CTshdifInris P4002 and 130 temperature TWol. TWC2.T.TT01.T4 J
Measure and record all instnaments and plot water level in 140
' sent tant venus time (nr 12(U s Set PIC4002 rressure wt pomt a 7011 kPa About ioT as '-
!!O supertwu at ICC
, 'nlet 160 l Set T1C4002 temperature set pomt = 175 *C l l I
- f. .
I I
. Repeat phases 60 and 70 The aisam in the l '
IJD PCC upper i ""d
- 1R0
! %'xt to reach ueady state condicon m"'*pressure ,
P4002. l l TP4003.T. AOOl and temperature TW)01. A001. T. A002, T.D001. T.D002
,n ,,,,,,g
. crmonions TWC2 ! T.T001. T4002.
Measurt and rvord :J) mstruments and plot water level in 190 sent tant versus time tot i200 5 Ret Picam2 pressure set pomt a M25 3 LPa About 10*C rg f 200 Superness at Pcc __ iruct Set TIC 4002 iemperature set pomt = 18l*C 210 l l l _ 1 i The ueam m veni j l 220 Reneat rehases 60 and 70 Ime must N in ! state condsuon in pressure P4002.**'""8 l
% st to reach steady "d"' "'
i 230 P Anal and temperature T401. T.6002. T.T001. T4002. ' i i T.Wm T. Ar02. T.D001. T.D002 l I - I..240 .! Measure and record all instruments and plot water level m , t sent tank versus time fnt I:00 s f. i { O l 0 ' ' Clow steam flow control valves FJol . FJoi FJO2. FJI 3 . 1 I Turn ntI pump C001 and cime valves FOII / F049 I a a, . . _ l
~ cepreuunze and dram ihe svuem I
i
tuxuancei Rev Page j of T , l l
.e tacme N e w ton t rvov s evi > :rmR PP91 0 i 1'9 '
D I P ANT 1tERS PCC TEST PROCEDL'RE Pa ge _1,.of.,2 risse Heat Losses in intection line Vent Line and Vent Tank Tese a ti-QL wwe l l I I I l l 1 l Date Esperiment Manater Signature l
i Dac=*ai R"- Pane of-SIET I l On09MPP91 i 0 1 138 23 f-- enone Hennon innovativi . PANTHERS PCC TEST PROCEDURE 1 1 Page W Q l l
.- Tess a l{-Ql.
rotse Hear Losses in iniection line Vent Line and Vent Tank Description j Note F' haw i l Strans l Oper, :, s
! I Siraat-
~ N swam m went '!
ime must be in 130 Wait to stach steady state condiuon in pressure P4002 and
'***'*d temperature T4)01.T 6002.T.T001.T4002 ennonums .
140 l Measure and record all instruments and plot water level tn ; I sent tasik sersus time for 1200 < 1 j
; }
! Set PIC-4002 pressure wt pomt = 701.3 kPa i I.
!!O About IU*C a superheat at PCC 160 Set TIC 4002 temperature set pomt = 17$ *C ,
m1c 170 Repeat phates 60 and 70 ! The steam m the i 180 Wait to reach steady state condiuon in pressure P 4002. P. A001 and temperature T-6001. T-6002. T T001. T 4002. [PCC upper'jj'" l T 4003. T. A001. T. A002. T D001. T-D002 m inwnied i ccmdasons 190 ! Measure and record all instruments and plot water level in i I sent tank versus time f or 1200 s i l f i 200 ' Set PIC tm2 pressure et pomt = N25.3 kPa Abou .10*C d Superheet at KC 210 ; Set TIC 4002 temperature set point = IMI'C mje -) 220 Reneat phases 60 and 70 The swam m vent i 3m' mu N
- 230 ) Wait to reach steady state condiuon m pressure P 4002, * *8 "'d l P A001 and temperature T-6001. TW102. T T001. T 4002. ' "dd"**
' T H001 T. A002. T.D001. T.D002 240 ! Measure and record all instruments and plot water level in
' sent tank versus time for l200 t l
I l.
- !O ! Close stearn now control valves F 001. F.00$. F 002. FJ103 i
l l 260 } Tom nef pump C001 and clow valves F01I / F059 l 1 { ! 270 - Depretturne and drain the tvstem 4
~
h u""' R" Paste j of SIET 1 l l secone weston inno um f(09RPPQt 0 i 139 1 2:3 Pun {ERS PCC TEST PROCEDURE Page l ofj Title Heat Losses in iniection line. Vent Line and Vent Tank Tess s WD1 N ote Date Experiment Manaster Sintasture
D**"" "' Paste j of MET I I ! scanne Nemicn truwwaim i m09RPPol i 0 1 140 4 225 PASTHERS PCC PRE. TEST CHECK LIST Pastelofj Titse Hear Losses in Drain Line and Condensare Tank Test a it-Q2 Desenptme Nase l Status Oper. Phase s l I l_ Signet. 10 Venfy that H plant configurauon is complete and suitable for the scope of test H.02 Pool P and Q empty and the folowmg imes are avasble: steam supply line 1. l condensale desuperheating tank. temporary ime 3. inyecuon feedwater ime line to module ! 4. drain line 5. I upper header Venly that the fouowing valves are closed: F038. W39, 20 F009. M13. SF003. SF002. Mi7. F018. F015. F001. R02. FD03. F025. F011. F059. F033. F034. F005 F058. F007. l Venfy that the fouowing valves are open: 30 SF001.F506 40 Vertfy that the following instrumentauon has been calibrated, installed, filled. vented and is in operauon : P 1001. F.1001. T 10CI. T 4001. P 4001. T 4002. T4003. P 4002. P.L001.T. LOOT.T.LD02.T LD03.T. LOO 4.T 5002. OP 029. L LOGl. L LOO 2 1 50 Venfv that the tollowmg safety valves are set at 1.0 MPa;
- F016
*F050
!- ~
e 1 60 ! Venfy that the steam desuperheatmg control system TIC. l 4002 is avaible
} I 70 ! Venly that the Data Aquisition System n operatonal and i Ihe converson costants and formulas have been coffectiv l inwned m the D AS
- NO Venly that the condensers are cooled t Fluviale pump is operauonall -!
t,.-y e.,,,,,.,,m,-'-*-*g'r*r- -t'*+4ea-*
- w "e-N g e ~- w' v 's
i
**""' "" l P*** '
SIET I I I (WXNRPP91
' O IJi 225 s< ma wcuum tr.novsuvi PANTHERS PCC PRE-TEST CHECK LIST Page l o(j Test e &D2 T<ae Hear Losses in Drain Line and Condensate Tank
%de e
a f Date F.speriment \tanater Maasture I - l t f 1
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Doc u'"*' Rev Pete j of SIET I l l ei0oggppgi i o { la: 3 :3
-enone Neanon inno suvi PANTHERS PCC TEST PROCEDURE Page lofj Test n &Q2 rase Hear Losses in Drain line and Condensate Tank Description Note Status Oper.
f%ase Signet-8 10 Open the valve F037 :ind close F506 i 20 ! Start pump C004 and fill fully FCC with water 30 When the water comes out from F037 valve stop C004 and close valve F037 40 Open fully valve F503, and drasn iniection ime Mamaan valves Foot and Foo2 50 Open valves F025. F003. F004, and open F005 at its '#"~ minimum value and begm to Iced the nser, the drain line *A*8 and tha condensate tank with steam shoukt be sufGcient to perform ttw tes 60 Start pump C001. open valves FC*o / F0li and begm to Jesupertiested sicam If required men
fY l'"l* M1 70 Throitle valve F503 till to have a absolute pressure P 4002 and F002 valves a 251.3 kPa AboutiffC of j supi-wi ai PCC x0 ! Set TIC 4002 temperature set pomt = 14l*C inlet 90 l Adiust steam temperature it!! to reach required ternperature na T4002 (10~C of supertiest or lessi The team .n l con *"$8"
- 100 Wan to reach steady state condiuon in pressure P4002. P- """ *
- LOO! and temperature T-LOGl. T LOO 2. T LOO 3. T-LOO 4. T. satursied 6002 .rnditions 110 Measure and record all mstruments and plo'. water level in condensate tank versus ume for 1200 s l I
l l
I*ea: Rev Page of SIET i ! l l
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PAN 111ERS PCC TEST PROCEDURE l Pane 'cQ Test a li-D2 Tine flear Losses in Drain line and Condensate Tank Deeptioe Note Status Oper. lh* l .
. %t.
120 ' Trtotde valve F0531:0 to have a absolute preuure P4002 a 501.3 LPs About 10*C cv I supernes si PCC IM j Set TIC 4002 temperature set point al62*C enjet 140 . Repeat phase 90 l l l 1 1 150 i RepeafI00 160 l Repeat i10 170 Throttle valve F503 till to have a absolute pressure P4(02 m
*01 3 k Pa About 10*C d l Superneu at ICC Ino j Set tlc 4002 temperature set pomi 17$'C miei 190 Repeat phase W)
[ i
' Repeal 100 l 1 200 210 R m atilo 220 Thruide valve F503 till to have a absolute pressure P4002 m d?$ 1 kPa About 10T is l $upernesi ai 6C C 230 ' Set TIC 4002 temperature wt pomt lH1*C
.nics i
i 240 ' Repeat phase 90 250 Repeat 100 260 Repeat 110 270 Close valves F005. F0(M. F003. FU25 and if opened clow I s Svet Ftrl2 and F001
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D"5" - I Ro l Page of , SIET l f e(mMPWI i O l lM 223
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.i PANTHERS PCC TEST PROCEDURE - ,
Page lof,,2 Tinse Heat Losses in Drain line and Condensate Tank Tenait-Q1 .
.i Descriptme Nase Staeus Oper, i Phase l Signet. .
a i 280 ' Stop pump C001 arid clow valves F059 / F011 290 Depretsur12e the tvstem 400 Close valve F011 Note i 6
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Date Esperiment Maneser Sissature l I [ f l i i - - - - - m m. .w- g-,s--y ,, c- -, , - w . - - e,-.--, - ~ , - , ,n,- , , - - -- , - - . . . , . ,.-
o ; I i Da(=' Rev Paste of SIET i l '} { er.icoe kemian innovniivi n00ggProl - 0 i 145 I m I l l PANTHERS PCC PRE TEST CHECK LIST
-Page_Jo(1 _
j Title Hear f arses & rhr Pact ranneerson Iinr and I:nr to rarch Tank Test # M Descriptaos Sose Status Oper. Phase # l Sirast. 7 10 Vertfy that the plant configuranon is complete and suitable ~ far the scope of test H-03: complete closed PANTHERS. PCC test loop ' The ICC metrumentau 20 Venfy that all the instrumentauon (with the excepuon of n as meluded instrumentauon of air injecnon ime 21 has been calibrated, installed. filled. sented and is in operation i 30 Venfy that the Data Acquissuon System is in operanon and the conversion constants and formulas have been correctly inserted in D AS 40 Venfy that the following valves are closed:
- F%8. F038. F039. F009. FDl3. F037. F047. F023. F048.
F015. F018. F036. F031. F032. F030. F034. F028. F029. F035. RM2. Fm l . F002. F003. F025. F059. F0ll F019 and i F007 2re 50 Venfy that the fouowing valves are open: P'"'eny open F058. F007. SF001. FDl7 F019. SF003. SF002. F049. i FtM6. PM S. F033. F027. F055. F020. F022. F060 3 60 ! Venfy that the following safety valves are set at 1.0 MPa; ' I.F016.F050.FfMO l *Venty that the loUowing control systems are avaslable:
"O LIC-0002. T1C.1001. FIC-1001 l
. l i
40 I Venfv that the pump C001 and C004 are available If pools P and Q are full the 90 - venfy that the tanks A001. A002. A003 are full tana.s can be parually full 100 f senfv that the condensers art cooled !"Fluviale' pump is in ,
' nnerations >
i 44
N " **
- Rev Page of SIET I ! ,
#GNMPP91 0 146 23 vnone Hesian innovatm ,
POTilERS PCC PRE TFST CllECK LIST Pagelofj Tale item L nes ..? rhe P+ I C nneer:en t .nr a d L.nr rc r neh T. ink Test n & %nte
- 1) ate Experirinent 4.1anager Signature
l 1 ~ Doe = ="" Rev Page j or SIET I i l 0 1 147 ; n$ l woone Healtori inncnativi 40098PP91 l PANTHERS PCC TEST PROCEDURE Pate 1 of_2__ Title H.. ea! L.rtes ofihr Pont Cmerrinn f :nr and Iine rn tinch Tmtk Test t & Note Stanas Oper. Descriptum Phase i Signat. n 5m t, chow the nmnal w ater 10 I Set LIC@l level set point = 3.75 m level, to reduce the carry cPwee l durma the tmtl off i 20 Stan pump C004 and fill the pools till the required level The levelis 2.5 m arm the CT 40 Open valve F041 and fill the condensate tank up to level L. **' a d' LD02 =1.75 m IWhen this levelis reached. the water start to
- drain il line L. through F. LOG 1 40 Operi vajves:
F002.f003.F025.F059.F01I and purge the PCC bv steam 50 Stan pump C001 . 60 Open valve F006 and v21ve F012 beginning to desuperheat the steam 70 Throttle valve F019 On manual mode) in order to keep level L L0nl higher thario 5 m and L. LOO 2 =l 75 m 40 Open valves F005 and F006, to reach the maximum steam flow rate. controlling that temperature T 4002 shall be less
' ? ben 180*C and pressure P 4002 less than 700 kPA 90 lNicasure the PCC inlet pressure P 4002 and adjust
' temperature T 4002 acting on valve F006 in order to have l superheated steevn at PCC inlet with less than 10*C of ,
; superhearsne 100 Heat up the PCC pool water till to reach the equdibnum butk average temperature tste.My state condsuons) repeaung penodcally phase 90 in order to have superheateA steam at
> FCC inlet with less than 10*C of superheatine Th4s nowraie shouw w 110 Decrease steam flowrate to about 0.5 kg/s tF-100l+F 300ll. *II"' '*
adjusting the desuperheating in order to have superheated rnaamn the C steam at PCC inlet woth less than 10*C of superheating CTmdet ecns
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f Daccaa' Reg Page of SIET l I
- rm9xPP41 1 0 l 148 22.5 tranne demum innesim PANTriERS PCC TEST PROCEDURE ,
Page lof_2.,_ , Title llent 1.nsrs eithe Pact Connrerwn f :nr an.11:nr in C nrh rank Test a W. , Descripton Note Status Oper. Phaw { ~ Siamat. 8 I 120 ' Close valve R160 ; If regwed ou
- Measure and record all instruments and plot water level in mmes and 1.M) "'*'8*
l catch tank hne loop seal iL OOO2) for 1200 s can ce chanmed 140 Stop the test Nde i i
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h r Date Experiment Manager Signature . I Of 1 I
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1 l l SIET l ***** l Rev Page l-of l I iOD9MPP91 1 0 149 ; 22.5 scraone Meassan innowsuv' -; PANTHERS PCC PRE. TEST CHECK LIST 1 Page Lot ; I Title Steam Only Test Ten a M 1 Description l Nase l Status Oper. ! Phase # l I I Signet. ; l 10 Venfy that the plant configuranon is complete and smtable for the scope of test H44: compleic closed PANTHERS. PCC test loop The Kr , insimmensau 20 Venfy that all the mstrumentauon (with the excepuon d " " *
- i instrumentauon of aar injeccon ime 2) has teen cahbrated.
installed. filled. vented and is in operation 30 Venfy that the Data Acamstuon System is in opersoon and ' the conversion constants and formulas have been corttstly j inserted in DAS 40 Venfy that the following valves are closed:
- F044. F038. F039. F009. F013. F037. F047. R23. F049.
F015. F018. F036. F031. F032. F030. F034. F028. R29. F035. F042. FDel. F002. F003. F025. F059. F0ll. F060. F022.F503 I F019 and l F007 are 50 Venfy that the following valves are open: P'"'*UY 'P"" '
- F058. F007. SF001. F017. F019. SF003. SF002. F048.
m16. PMS. F033. F027. F055. F020 i l 60 l Venfy that the toUowing safety valves are set at 1.0 MPa: ' I.F016.F050.FS10
-I i
70 I Venfy that the following control systems are avaslable: 1
!
- LICQol. TIC 1001. FIC 1001 40 Venfv that the pump C001 and C004 are available j if poois P and o are tvil, the 90 venfy that the tariks A001. A002, A003 are full tAruts ean be
! rarnauv fuu I
I 100 l{ Venfy that the conderuers are cooled FFluviale" pump is in
.J
! operanon
D""" " ' Rev Pate of SIET l ! on098PPol 0 150 225 seraone Wemon traveuve PANTHERS PCC PRE. TEST CHECK LIST Page_2_of_2 Tes: s li-Q4 Title Steam On/v Test Nrde Date Experiment Manager Manature l
1 I D " "' R'o Pa** l - of- l SIET i l i i iOO9RPP91 i 0 t 151 l 2;j
'e mme Neannn inno ainvi 1
PANTHERS PCC TEST PROCEDURE i Page_Lo(j Tase Steam Only Test Tess a M 4 Description Note Staams Oper. Pha.w l Sirast. 8 i nonnaa = aser , WI , Set LIC-Q001 le een ses poet = 4.26 m i 10 Start pump C004 feed the ponts and control level L-Q001 = 20 4 26 m The levet is 2.5 m > aanve me CT Open valve F041 and fiU the condensate tank up to level L. d****** ' 30 LD02 = 1.75 m aWhen this levelis reached. the water start to dr:un hne L. through F.L001 At the operung of valve RJ03 steam 40 Open valves: 5'*n8toflo" i F002.F003.F004.F025.F059.F011-and puree the PCC by steam iF003 must be fuuv opens 50 Start pump C001 and begin to desuperheat the steam ' openmg valve F012. F006 5 Acceleromener:
=di be recorood 60 Measure and record all instrument signals meluding for 10 rrunutes accelerometers eviev 30 rrunuies l 70 l Open valve F001 and increase the steam flowrate f .
M0 Throttle valve F019 tin manua! medet in order to keep levei '
. L-LOO) hieher than 0 5 m and L-LOO 2 = 1.75 m 4 10*C of susernest w less at PCC 90 Open valves F005. F001 and F006, to reach steam flow rate * * ' '
F 1001 + F-3001 = 6 6 kg/s. controlhng that temperature T. 4002 shall be less then 180*C and pressure P 4002 less than ,
?90 kP3 !
100 Measure the PCC mlet pressure P 4002 and adjust temperature T a002 actmg on valve F006 in order to have j superheated steam at PCC Inlet with less than 10*C of
%UDerheattMf 110 Heat up the PCC pool water till to reach the equilibrium j bulk average temperature tsteady state condiuonsi repeatmg penodically phase 90 in order to have superheated steam at l PCC inlet with less than 10*C of supementine I
D*c = Rev Page of SIET l l
.< t.,au Newrm inreverm cryngppol 0 152 22.5 PANTHERS PCC TEST PROCEDURE Psse _lar.J, Test a H-04 Tstse Steam Only Test Note status oper.
Desenptmo } Phaw i i Signet s 10 Adjust steam (kw rate to the required value F.1001 + F-3001 = 6.6 kg/s. controlling that the steam at the PCC inlet shall be supetheated with less than 10*C of superteaung nemperature T-8002) 130 When Steady state condstsons are reached. Leep measunng and recortiang all instrument signals for 15 minutes 140 Stop the test Note Date Esperiment Manater Signature
D * * *' "" Page of SIET ! l l l n0094PP91 1 0 f !$3 1 225 secane Newnn innovanvi , P ANTHERS PCC PRE-TEST CHECK LIST Page L _,of_;,,,_ ) Test a H-05 l Title Saturated steQmlalf mixtures test } Descripuoe Note 1 States Oper. l Phaw al I I Signat. I 10 Venfy that the plant configuracon is complete and suitable for the scope of test H 05: complete closed PANTHERS-PCC test i loop The PCC 20 Venfy that all instrumentanon has been cabbrated. mstalled. filled, vented and is in operauon instrumentau on is included Venfy that the Data Acquisiuon Systems is in operacon and the l 30 conversion constants and formulas have been correctly inserted in
.DAS I
40 l Venfy that the tollowing valves are closed: F039. F009. F013, F037. F047. F023. F048. F015. F018. F036. F031. R)32. F030. F028 . F029. F035. F042. F041. F001. F002. Fn03.F004.F059.F011.F060.F022.F503.F034 I F055.F007 50 J Venfy that the following valves are open: and F025 are 5 F001. 5F002. 5 F003. F007. F038. F025. F044 partially open
'!F05RF049F017F027.FGs5.F033.F055 4
Venfy that the following salety valves are set at 10 MPa; 60 I F016.F050.F040 l l 70 ; Venfy that the following ccmtrol systems are avas!able: )
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! P!C 4002 . FIC.1001. FlC.2001. TIC-1001. LIC-0001 80 Venfy that pumps C001. C004 and compressors C002. C003 an:
av allable I I if pools P.O. 90 , Venty that the tanaes A001. A002. A003 are full t are full. the taries can be
. partially full 100 Venfy that the condensers are cooled i "Fluviale" pump is in l
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i am98PP41 ' O i 154
,cuane gemm Ir.novatm P ANTHERS PCC PRE TEST CHECK LIST Page 1.,,,of,,1,_
Test a 6-Q5R Tine Saturated steam! air mixtures test Note Date Espenment Manager Signature I
Doe = ai Rev Paste of SIET l l l l woone Neancri Lvemivi j 00098PP91 , O i 155 j 225 PASTHERS PCC TEST PROCEDLIE Page 1 of _4 Tithe Saturated steam! air mixtures test Test c &Q$, Desaipoos Note l Status l Oper. Phase 8 I l I i l Sirast. 10 Set LIC Q001 level ses poin = 4.26 m normal wita level i Start pump C004 feed the pools and control level 20 ! L-0001 = 4 26 m Open v;uve F041 and fill the condensate tard up to level L. 30 LOO 2 = 1.75 m (wben this level is reached. the water starts The level is
; to drain m line L.through F-L001 2.5 m above j the CT truet l nonle 40 Open valves: F002. F003. F004. F059. F011 and purge At the operting of the PCC by steam. (Valve F003 must be fully open) valve f003 steam starts l
I to flow
! Start pump C001 and begm to desuperheat the steam 50 l openina valves F012. F006
[ Measure and record all instrument signals including 60 1 accelerometers Accelemrriet m wd k i recorded for 10 mmutes l ewry 30 minutes
- Open valves F001. F005. F006 to rexh a steam flow rate F.
70 l 1061 + F-3001 > 5 Kg/s controllmg that temperature j' T.4002 shall be less than 180* C and pressure P-4002
' less than 700 kPa 30 , Heat up the PCC pool mater td) to texh the equilibrium
' hui averste temperature isteadv state condstas) 90 . Start compressors C002 and C003. open partially valve i
i FOOR and w as till to have pressure P-2001 s 2.5 MP3 1 100 ! Open partially valve F009 and berin to ingt air
!!0 Set PIC t002 pressure set pomt = 453 kPa and control pressurt is m absolute
' the pres.sure in automatic mode . value w_ _ _ _ _
- t. n Daa=a' Reo l Pagte of SIET - } l
-er;onc dwinn truwveuve 00098PP91 ! O i 156 225 P ANTHERS PCC TEST PROCEDURE Page l of __4 ,
Title _ Saturated Kleam! air mixtures fest Tess all-QN. . Descripeme Nase Status Oper. Ph ase s1 Signet. i -i l Open valve R108 tdl to have a sir now F.200l=0.83 kg/s if it is not . ' 120 poemble to ' l senfving that the air pressure P-2001 must be higher than rexh the 2.0 MPs required aar
! Oow i
mere se the openmg of the valve I RX)9 130 Operate valves F001. F005. F006,lif required adjust i valves F025 and '/007) to rexh steam Dowrate F 1001 + F 3001 = l.4 Kg/s. controlling that tanperature T. W 2 thall be less than 180* C i 10' C of 140 l Measure the PCC inlet pressure P 4002 and adjust PCC i f inlet conditions an order to have the required followmg test tuperheat or less at PCC ; tnnditions: ,
. i,.:ci f F-1001 + F-3001 = 1.4 Kg/s
! F-2001 = 0.83 LG/S l
l PJD02 = 453 KPs tmaximum mlet test valuel
! T 4002 5 158' C I !!0 < When steadv state conditions are texhed measure DP-025.
l if DP4)5 is higher than 14 KPs stop the test else keep i messunng and recordmg allinstrument signals for 15 , I minutes 160 Decrease the pressure set pomt et PIC 4002 of about a quaner of the PCC inlet pressure vanation range: the set 1 point oiPIC Af102 is = 390 KPa Measure the PCC mlet pressure P 4002 and adiust PCC mlet 10' C of 170 ! condstKms m order to have the required steam (F 1001 + superhest or F30011 and air t F-2001) nowrates cor. trolling that the mlet less at PCC ]
, temperature T t002 shall have a superheatins degree less inlet l 4 than 10 *C I
1
Doc = ** R" P=* i of
! l SIET l r iOO98PPol 0 1 157 ' 215 ennne Neancn imm i PANTHERS PCC TEST PROCEDURE PgeLot__4, Teu a }{-Q1 Tase Saturated steamlair mixtures test Dewription Note i Status Oper.
fmaseai I Signat. - IRO ' Repeat phase 150 l 190 ; Decrease the pressure set point of PIC4002 of about a i quarter of the PCC inlet pressure varuuon range; the set l point of PIC4002 is = M5 KPa i f 200 Repeat phase 170 210 Repeat phase 150 220 Decrease the pressure set point of P!C4002 of a quaner of the PCC inlet pressure vanauon range; the set point of PIC-4002 is = 260 KP 230 f, Repeat phase 170 240 Repeat phase 150 1 250 l Decrease the pressure set potnt of PIC4002 of atout a l quaner of the PCC inlet pressure vanauon range; the set
' point of PIC4002 ts = 104 KPs 260 ' Repeat phase 170 1
270 i Repeatl'O h Stop the test 230 1 l f
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k':" Reo j Page l of SIET I i rin098PPCI O 158 i r_$ cuonc n eumri innovenvi P ANTHERS PCC TEST PROCEDURE Pate 4 d_4_ Tess a H-05 Tiae Saturated steam! air mixtures rest Newe Esperiment Manager Signaturt Date
1 D ( * ** Rev Pate l of i l SIET I er;one demian inno an*' f @ 8PP91 o 159 , 225 P ANTHERS PCC PRE. TEST CHECK LIST TESTS %TTH TWO MODULE.S Page L uf L 3 Test a l+30 l rule Test nve A 1.1 - Saturated steamtarr mixtures rest j Description Note l Status j Oper, Phase s i 8 f Sirmat. 10 Venfy that the plant configursoon is complete and smtable l PCC for the scope of test A.I.I.. complete closed PANTHERS - test loop l l Venfy that allinstrumentauon has been cahbrated. installed. The PCC 20 mstromentat
- filled, vented and ts m operauon ion is included Venfy that the Data Acquisition Systems is m opersuon and 30 the conversion constants and formulas have been correctly mserted in D AS 40 Venfy that the following valves are closed :
! FO38. F039. F009. F013. F037. FN7. F023. F048. F015.
F018. F036. F031. F032. F030. F028 . F029. F035. FN2. FN I . F001. F002. F003. FON. F059. F011. F060. F022. IF503.F014 F055.F007 50 ! Venfy that the followmg valves are open: and F025
- SF001. SF002. 5 F003. F007. F025. F044. F058. FN9.
are partially
;F017.F027.FN5 F033.F055 open Ventv that the tollowing salety valves are set at 1.0 MPs: l
! I F016. Fn50. FNO 60 P!C-70 l Venfv that the followmg control systems are available:
4h02 . FIC.1001. FlC.2001. TIC.1001. LtC-0001 l l KO Venty that pumps C001. CON and compressors C002. C003 - are available If pools P. 90 ! Venfv that the tankes A001. A002. A003 are tul! Q. are f ull, the tanaes can be partia!!v full 100 i Venf v ihat the condensers are eccled a 'Fluvsale" pump is m operanoni l I
N""' Rev Page j of l SIET : i (109RPPo t n i 160 ! 225
'econe d emicri Iresim POTHERS PCC PRE TEST CHECK LIST TESTS %TTH TW'O MODULFS Paat i of i Tat a 1+30 Tisse Test nne - A I I Saturated steam! air mixtures test Neve Date Expenment Mansaer Signature I
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Documt Ro Pete j of l l SIET l 68PP91 0 1 161 225
.ne weanon fressive i PANTHERS PCC TEST PROCEDURE TESTS WTTH TWO MODULES f%e_L_.or.5._
Tess a l+30 Tine Test noe . A I 1 Saturated steam! air mLrtures test Nnte Oper. Descriptson Status l Phase si - 1 Signat. normal 10 ; Set LIC-Q001 level set potnt = 426 m water level i Start pump C0(M feed the pools and control level L-Q001 = I 20 J 26 m l Open valve F041 and fill the condensate tant up to level L. The level as 30 ' LD02 = 1.75 m (when this level is reached, the water starts 2.5 m above f to dram in ime L. through F LOO! 1 the CT inlet no nle 1 At the 40 Open valves: F002. F003. F004. F059. F0li and purge the openmg of PCC by steam. t Valve F003 must be fully open) valve F003 steam starts i to flow l Start pump C001 and begm to desupertical the steam I
!0 . orenme valves FO!2. F006 I Measure and record all instrument signals meludmg Accelerornet 60 f xcelerometers ers will be recorded for l
10 minutes every 30 I mmutes j 0;rn valves F001. F005. F006 o rexh a steam now rate F-
*0 i 1001 + F 1001 > 5 Kg/s controllmg that temperature T4002 i shall be less than 180* C and pressure P 4002 less than 790
!kPa
' l l M0 !
Heat up the PCC pool water till to rexh the equitabrium !
' bulk average temperature itteadv state condinonst l
90 Start compressors C002 and C003.open parually valve F008 l and w ait ull to have pressure F.2001 a 2.5 MPs i From i Kg/s 100 Open valve F038 or F039 to msert the adequate onfice for 10 0.1 Kg/s
, the test open valve F038 below
' open valve j' F039 i10 I Open parually valve F009 and herm to iniect air ;
Dac ==a' Rn- Page of SIET i ! l
'10098PP01 0 i 162 1 22.5 cuane deuvri treenvi -
PANTHERS PCC TEST PROCEDURE TESTS MTTH TWO MODULES Pamelof_5 Test a 1+30 Tine Test twe - A I I Saturated steamiair mixtures rest Descriptme Note j Status l Oper. . { Phawal' I I f- Sismat.
)
i Set the PIC4002 pressure set point equal to the PCC pressure m ' 120 maximum mlet absolute pressure value requtred for the test; absolute we table n.7 for the required pressure valuel value I if it is not 130 : Open valve F008 till to have a air flow F 2001 or F 2002= see table n.7 for the required air now valuet vertfymg that possible to l the air pressure P 2001 must be higher reach i thanthe2,0 MPs l required air
!' flow ,
increase the openmg of , the valve F009 e 140 Operale valves F001, F005. F006. (if required ad lust valves F025 and F007) to reach steam now F.1001 + F .1001 at see table n.7 for the required stearn tiow value) controllmg that ' temperature T4002 shall he less than IMO* C (*) See table l 150 Measure the PCC mlet pressure P 002 and edsust PCC t sniet conditions in order to have the required followmg test N.7 for steam flow,
' conditions:
' air How and t
1 PCC mlet F 1001 + F.1001 = t') kr/s f .j pressure values
'. F 2001 = i') k g/s 1i
- PJn02 = i') LPs (maximum PCC iniet pressurei j temperature T4002 must be superhesied with a j suprnestine degree less than 10 *C J i
1 I ' i I 160 : When neady state condmons are reached measure DP-025. '
! if DP-05 is higher than 14 K.Pa stop the test else keep
.l measunne and recordmg allinstrument signals for 15 l
! mmutes
.l l }
170 ' Decrease the pressure set pomt of PICan02 of about a j l Quaner of the PCC inlet pressure vartation range;isee table
' N 7i t 6
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Documet j . Rn Page of l l SIET I n0098PP91 0 8 163 1 225 secone weuum Innovum PANTHERS PCC TEST PROCEDURE ! TESTS %TTH TMO MODULES
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Page_J_,_of,$ __ l T,sse Test troe A I I Saturated steamtair mixtures rest _ Test a l+30 . . Description Nase Status j Oper. ' Phase s l l ' Siisant. 180 Measure the PCC tniet pressure P4002 and adjust PCC inlet 10' C of F condatons m order to have the required sicam (F 1001 + superhest or ' F3001) and air flow 4F.200 lor F 2002)as specified in table less at PCC N.7 controllmg that the inlet temperature T4002 must be mlet superheated with a supertieaune degree less than 10 'C 190 Repeat phase 1N) 200 Decrease the pressure ses point of PIC4002 of about a t quarter of the PCC inlet pressure vanauon range (see table N.7) 210 Repeat phase IRO 2:0 . Repeat phase 160 [ 230 Decrease the pressure set point of PIC4002 of about a quaner of the PCC mlet pressure vanation range asee table I N 7)
-i i
l 240 : Repeat phase 180 I ; 250 ' Repeat phase IM) i 260 l Decrease the pressure set point of PIC4002 of about a , l quaner of hie PCC mlet pressure vanation rante till to reach - j the PCC mmimum mlet absolute pressure value required for , t the test 4see table N 7) 270 i Repeat phase 140 180 I Repeat phase 160 I Stop the test l I } 290 I l i
Rev j Pane or Da* * * ** ' I l
. SIET I i
m09MPP91 0 1 1M i 225 ser;one Hem uni inr e enivi , PANTHERS PCC TEST PROCEDURE TESTS WTTH TWO MODULES Page 4 of_5__ l Test a l+30 Titse Test troe - A I 1 Saturated steamiair mrxtures rest + Descriptioa Nne Status Oper. Pba3e s l Siamet. , 1 l 200 i Repeat phase 170 210 Remat phase 150 220 Decrease the pressure set pomt of PIC4002 of a quarter of the PCC inlet pressure vansuon range; the et point of P!C. an02 is = 260 KP 230 Repeat phase 170 240 Repeat phase 150 t 250 Decrease the pressure set point of PIC4002 of about a quarter of the PCC inlet pressure vanation range; the set _ point of PIC4002 is = 108 KPs 260 Repeat phase 170 270 Repeat 170 i 9 top ihe test l 1 180 . i i t 4 l . -, - _ ~ . _ - , _ . , _ _ . , _ _ _ . , _ _ _. __ .._z_
t w ume.t ge, j e.se or SIET , l l
-cuane gemun lealm e tXJ9MPPo t n '
165 1 23 P ANTHERS PCC TEST PROCEDURE TESTS WTTH TMO MODULES Pnne 5 of.5 rase Test nve - A I ! Saturated steamiair mixtures test Test a l+30
%we 1
Date Espenment Mansaer Signature
r-D***mt ~ l Rev Page of SIET l sennne Meation innowevi . (WX)98PP91 0 t 166 3 225 PANTHERS PCC PRE TEST CHECK LIST. TESTS %1TH TWO MODULES Page i ol i Tisle Test tyve A 11 Suverheated steamiair minures . Test a 3 l+36 Description ! Nat 5tasias . Opes . Phaw sJ ' Signet. 10 . Venfy that the plant con 0gurstson is compicte and suitable j fcr the scope of test A.I.2.: complete closed PASTHERS - i PCC test loop 20 f Venfy that allinstrumentauon has been cabbrated mstalled. The PCC
' Gued. vented and as in operauon instrumentat sonis
' meluded !
j Venly that the Data Acquisition Systems is in operauon and 30 l the conversion constants and formulas have been correctly I insened m DAS 40 Venfy that the following valves are closed : F038. F039. F009. F013. F037. F047. F023. F048. F015. F018. F036. F031. F032. F030. F028 . F029. F035. F042. F041. F001. F002. F003. F004. F059. F011. F060. F022. F503.F0ts 50 Venfy that the fouowmg valves are open: F055.F007 SF001. 5 F002, 5 F003. F007. F025. F044. F058. F049, ano l"025 I F017.FU27.F045.F033.F055 are pw ally
' open -
i Venty that the following salcty valves are set at 1.0 MPa: l i 60 ' F016.F050.F040 i 70 P!C.
; Vcafy that the followine control systems are available:
M02 . F1C.1001. FlC.2001. T1C 1001. LIC-0001 80 Venf y that pumps C001. C004 and compressors C002. C003 are available i 90 ' Venfy that the tantes A001. AUO2. A003 are tull if pools P. i Q. are full. the tankes can be pantally full I 100 ; Venfy that the condensers are cooled i "Fluviale" pump is m operationi
N = =' R Pase I or I l SIET i er;one Neanan Ir.novarm M RPPol 0 167 } 23 P ANTHERS PCC PRE. TEST CHECK LIST TESTS MTTH TWO MODULES Page ' of '
.Tess a 31+36 Tisse Test troe A 1 T Suoerheated steam! air mixtures
%rne Date Esperiment Manager Signature 1
l Da* *'"' R" Page of ! SIET I i i
, nnne desuri inwom - t n0008PP91
- O I 168 i 225 PAVTHERS PCC PRE. TEST CHECK LIST TESTS WITH TWO MODULES Pay 1 of 4_
r,ar Test troe A 1 T Suverheated steam! air mLrtures .Tess a 31+36 , Desenption Note Status Oper. fue a Sisant.
' Set LIC@l level set point = 4 26 m normal 10 I water level Stan pump C004 feed the pools and control level L-Q001 =
20 l 4 26 m i Open valve FGsI and I'ill the condensaie tatt up to level L-LOO 2 = 1.75 m tahen this levelis reached, the water starts The level as 30 , to dr:un in line L. through F.LD0ll 2.5 m above the CT inlet nozzle , Open valves: f002. F003. F004. F059. F01I and purse the At the 44 PCC by steam. IValve F003 must be fully opent opening of valve f003 steam starts , to flow ' l ' l Start pump C001 and begin to desuperheat the steam = l 50 ' openene valves F012. F006 l Measure and record all instrument signals including Acceleromet 60 ! xcelerometers ers wdi be -
'E recorded for l
10 mmutes - every 30 minutes i Open valves F001. F005. F006 to texh a steam now rate F-70 l 1001 + F.3001 > 5 Kg/s controlling that temperature T 4002 I shall be less than 180* C and pressure P 4002 less than 790 I LPs i Heat up the PCC pool water till to rexh the equihbnum l 80 bulk averare temperature Isiesdv state conditionsi . 90 ! Stan compresson C002 and C003.open partially valve F008
.ind w ait ull to have pressure P.2001 a 2.5 MPs f a
Open $alve F038 or F039 to insert the adequate onfice for From i Kg/s 100 - 10 0.1 Kg/s
, the test I open valve F038 helow
' open valve i F139 ,
f 110 ' Open partiallv valve F009 and begin to miect air i
,,n. . . . - -. - - -- < ,,n -a
D cumat j Rev l Pa4te l of SIET l i rin098PP91 i 0 i 169 1 225 semme Hemi iruwmim PANTHERS PCC PRE. TEST CHECK LIST TESTS %TTH TWO MODULES Pat,e ? of_4_
. Test a 31+36 Titse [est rvne A 1 ! Suverheated steam! air mLrtures Descriptwo l Note Status l Oper.
Phase s 1 I Signat. I Set the PIC4002 pressure set pomt equal to the PCC pressure m 120 maximum inlet absolute pressure value required for the test; absolute me table n 8 for the required pressure value) value Open valve R)08 itil to have a air Dow F 2001 or F 2002= If it is not 130 me table n.8 for the required air flow valuel verifying that possible to the air pressure P 2001 must be higher than 2.0 MPs reach the required air now merense the operung of the valve 1009 140 Operate valves F001. F005. F006. (If required adjust valves F025 and F007) to rexh steam flow F 1001 + F 3001 =(see table n.8 for the required steam Cow value) controllmg that temperature T 1002 shall he less than iNO 'C Measure the PCC inlet pressure P4002 and adjust PCC (*) See table 150 mlet condsuons m order to have the required following test N.8 for steam now. conditions:
' air Dow.
I p.1001 + FJ001 = e'l k g/s PCC intet 1 pressure and F.2001 = i') k g/s super. I heaung P-8002 = i') LPs (maximum PCC mlet pressurel degree values temperature T4002 must be superheated with a superteaune decree of (*) 'C 1 l 160 When steady state conditions are reached measure DP-025. if DP-05 is higher than 14 kPa stop the test else keep
! measunng and recording all mstrument signals for 15 I mmutes 170 Decrease the pressure set pomt of PIC4002 of about a quarter of the PCC mlet pressure vanauon range; tsee table j N Rt f
180 Measure the PCC mlet pressure P 4002 and adtust PCC mlet conditions in orcer to have the required steam now (F 1001 l + F3001) and air flow tF 200 lor F.2002) as specified in table N.8 controlling that the inlet temperature T 4002 must be superheated with a superheaung degree of 20 'C or 30 *C me table N 8) ) I
' * 7 5 ' Rev i Pase j or I
SIET i
-c uon, x - inno..i-,
,voisppoi o i io i 23 PANTHERS PCC PRE TFST CHECK LIST ,
TESTS HTTH TWO MODULES Page 3 (4_
.Tesn o 3 l+36 Titse Test troe A I T Suoerheated steam!atr mLrtures Note States l Oper. '
Descriptaon Phase aj I I Signet. 140 Repeat phase 160 200 Decrease the pressure set point of PIC 4002 of about a i quarter of the PCC inkt pressure vanation range isee ubic
!NO
}
i i 210 4 Repeat phase 180 l l 2:0 ' Repeat phase 160 DO Decrease the pressure set point of PIC-4002 el about a quarter of the PCC inlet pressure vanation trngr. (see table N Rn 240 l Repeat phase IMO l
- !O ' Repeat phase 160 260 Decrease the pressure set point of PIC-4002 of about a h
; quarter of hte PCC inlet pressure vanation range till to reac
! the PCC minimurn erlet absolute pressure value required for
' the test iwe table N R) l
?0 1 Repeat phase 180 i l l I
1 . 280 Rascat phase IN) 290 f Stop the teu I
D ***mt j Rev l Patte l of SIET I c ume Neuem treativi i 1009RPP91 - 0 I 171 1 23 P ANTHERS PCC PRE. TEST CHECK LIST TESTS WTTH TWO MODULES ] Page 4 00_. ;
. Test a 3 l+36 Tssk Test troe A ] ! Suoerheated steam! air mLitures Nns e Date. Espensent Manster Signature
Dac "' ' Rev Pase l of SIET I > l mone wemen inrevoim rayggProl O t 12 i ::3 P ANTHERS PCC PRE. TEST CHECK LIST TESTS %TTH TWO MODULES Page 1 o( L Titse Test troe A 13 Steam Only (No air in PCC tubes 1 Test a 37+49 Dewr ptmo Note Oper. Phase a t l Status lI I Sigast. t 10 i Venfy that the plant configuration is com >iete and suitable l for the scoge of test A.I.3.: complete closed PANTHERS - i PCC test loop Venfy that all mstrumentauontwith the excepoon of The PCC
- D instrumentat
; instrumentation of air injection line 21 has been calibrated.
; installed. filled. vented and is in operation sonas i meluded Venfy that the Data Acquisition Systems is in operation and 30 the conversion constants and formulas have been correctly inserted in DAS 40 Venfy that the following valves are closed ;
! FOa4. FO38. F039. F009. F013. F037. F047. F023. FN9
' F015. F018, F036. R31. F032. F030. FO34. F028 . F029.
F035. FN2. FD41. F002. F003. F025. F059. F011. F060. F022.F503. 50 ! Venfy that the following valve' are cpen: Rl9. and FO 5 R. F007. 5 F001. F017. FD l9. 5 F003. 5 F002. FNR. F007 are
, FN6. FN 5. F033. F027. F055. F020 pamally open i
\ enty that the tollowing sately valves are set at 1.0 MPs: l l
60 F016. Fn50. FNO "O j Venfv that the following control systems are available: LIC-Qn01. tic.1001. FlC 1001 l I 1 KO Ventv that pumps C001. CON and are available If pools 90 i Ventv that the tankes A001. A002. A003 are tull Pand Q are full, the tanks can be pamally full 100 l Venfv th.st the condensers are cooled i Flusiale" pump is m D OtIOn6 1 i i
**==' Rev l Psaa j of SIET I l
< nc., w . mon in.io .i .. , n0098PP91 i 0 i t73 i m
P ANTHERS PCC PRE TEST CHECK LIST TESTS %TTH TWO MODULES , P w l of i Title Test rvne A 13 Steam Only (No air in PCC tubesI Test a 37+49 N ote 1 i i Date Expenment Manager Signaturt
.. - .- . - - ~. - .- . . . -.~ _ ~.-. . . . - .
R" Page of D*'""' I i SIET I
' 174 225 00098PP91 i 0 n.nne nemian innovanvi 1 ,
PANTHERS PCC TEST PROCEDURE TESTS %TTH MODULES Page_,L_of _2, Tene a 37+49 Titse Test troe A I3 - Steam Only (No Air in PCC Tubest Note l Status Oper, . Descriptu>e l Phase a i ' I I Sirant. normal - 10 Set LIC-Q001 level set poet = 4 26 m w:uer level _ 7 l
; Start pump C004 feed the pools and controllevet L-Q001 = l 20 ! 4 26 m l Open vajve F041 and fill the condensate tankThe up levelis to level L-30 = LOO 2 = 1.75 m iWhen this levelis reached, the water starts 2.5 m above to dram hae L. through F-L001) the CT inlet nonle At the 40 Open valves: F002. F003. F004, F059. F011 and purge the openmg of PCC by steam. (Valve F003 must be fully openi valve F003 steam starts to flow Start pump C001 and begm to desuperheat the steam l I
!O openine valves F012. F006 Measure and record all mstrument sigi.ab meluding j
Acceleromet 60 { xcelerometers ers wdi be recorded for 10 mmutes I cvery 30 mmutes
! Open valve F001 and increase the steam tiowrate l 70 l i
l Throttle valve F019 im manual model m order to keep level
~
I 80 l L. LOG 1 hieher than 0.5 m and L LOO 2 = 1.75 m i Open valves F001. F005. F006 to reach a steam slow rate F-1*) Ke/s controllmg that temperature T. (*) See table 90 ! 1001 + F 1001 i 4002 shall be less than 180' C and pressure P 4002 less than N. 9 for stestn flow 790 kPa mlet i conditons 100 Measure the PCC inlet pressure P 4002 and adiust .t
. ternperature T 4002 acuna on valve F006 m order to have '
! superneated steam at PCC intet as:
I f less than 10*C of superheaung ior tests 37+41 ' t w
- f rom 10'C to tO'C of <uperneatme for tests 4J +44 b
Dac= as R*v Page of SIET I l semaw demum inestivt 1 00098PP91 1 0 8 175 n$ PANTHERS PCC TEST PROCEDURE TESTS %TTH MODULES Pagelof _ . i Tisse Test troe_ A 13 - Steam Only (No Air in PCC Tubes) Test a 37+49 Descripuoe Note Sensma Oper. Phase s l Sismat. 110 Heat up the PCC pool water td) to rexh the equshbnum buytk average temperature tsteady state condsuons) repeauna penodically phases 90 and 100 Adjust steam Dowrate to the required value F.1001 + F.3001
= (*) kg/s, controlling that the steam at the PCC inlet shall (*) See table 120 be superheated with the required superheanns degree (T. N.9 for steam flow 4002) inlet condsuons I l When Steady state condicons are reached, keep messunng I 130 I and recording all instrument sienals for 15 minutes
?
140 Stop the tes I Change PCC steam inlet condiuons ' 150 I Note
?
i I i Date Espeneneet Masaaer Sistaatsre I
. . . ____________a
l j Docent i Rev Page of SIET l 176 l l W RPP91 0 l 22.5 eraanc desion innovuivi PANTHERS PCC PRE TEST CHECK LLST TESTS WTTH TWO MODULES Page 1 o( 1 Ten a 50+53 ielle Test noe A 1I stea:n ontv 1 Air in PCC tubes! Nots Statas Oper. Descriptce Phase s l. _ S'amat. Vent ime 10 Venfy that the plant con 0guraton is complete and swtable
. for the scope of test A.I.3.: complete closed PANTHERS - closed:
temporary PCC test loop with temporary line connecung the l' air line not supply line with valve F051 shown in the PalD 20 Venfy that all instrumentauon has been calibrated installed. The PCC filled. vented and is in operauon instrumentat ionis included Venfy that the Data Acquisition Systems is m operaton and 30 the conversion constants and formulas have been correctly inserted m D AS 40 l Venfy that the followmg valves are closed : i l'
, m38. 5F004. F009. F013. F037. FD47. F015. 5 F002. F051.
l F017 F036. F031. F032. F030. F028. F029. F035. F042. Fml.F001.F002.F003.F004.F059.F011.F060.F022. I F(Ot.F014 F007. and 50 Venfy that the following valves are open: F025 are S F001. F038. 5 F003. F007. F025. FGt4. F058. F018. F027. partially F045. F033. open
\ enly that the followmg safety valves are set at 1.0 MPs:
60 FOt6.F040.F040 l 70 : Venfy that ine tollowine control systems are available: I LIC.tA01. FlC.1001. FlC 2001. T1C.1001 llc.0001 RO Venfy that pumps C001. C004 and compressors COO 2. i C001 am available Venfy that the tankes A001. A002. A003 are tull if pools P.Q 90 are full the j tanks can be I partially full I 100 I Venty that the condensers are cooled i "Fluviale' pump is in f operanoni
h*= Rev l Psee d SIET l l
+<none desuri leum I n0098PP91 i 0 f 177 t 23 PANTHERS PCC PRE TEST CHECK LIST TESTS %TTH Two MODULFJi Page_1,,,d,1_
Titse Test nve A I L Steam Only ( Air in PCC tubest Ten s 50+53 Mme 9-Date Experiment Manager Sigastarv 5
4 D""**' Rev Page j of I l SIET l u0098PP91 0 i 178 I 225 cu ee dennon Irmovstwt PANTHERS PCC TEST PROCEDL'RE TESTS MTTH TM O MODOLES Pate I of 2 l T ,1se Test nve A 13 - Steam Only IAir in PCC Tubes 1 Test a 5%53 Desmption Note l Status Oper. Fues; Signet. I i Se LIC-Q001 level set point = 4 26 m nonnal 10 w2ter level
, Set LIC-LOGI level set gemt = 1.75 (level controded by L-
' LOO 2)
- Start pump C004 feed the pools and controllevel L-Q001 =
20 ' 4 26 m i Open valve F041 and fill the condensate tartt up to level L. The levelis 30 LOO 2 = 1.75 m . 2.5 m above When the level L-LOO 2=1.75 m is rexhed.close valve the CTinlet F04 I and control the level L LOO 2 in automatz mode. nozzle i At the 40 l Open valves: F002. F003. F004. FD59. F01 I and purge operung the i FCC by steam. acting on valves F037 and F0507 of I valve F003 steam starts I l to tiow i Start pmp C001 and begin to desupernest the steam !O ! opening <alves F0:2.F006
! Acceleromet M1 ers will be
; Measure and record all instrument signals including recorded for
; xcelerometers 10 mmutes every 30 minutes
, Open valse F001. F005. F006 to reach a stearn flow rate F-70 } 1001 + F-300l>5 kg/s controlling that temperature T 4002 I shall be less than Iho 'C and pressure P 4002 less than 790
' L Pa
; Start compressors C002 and C003. open a httle valve F008 l i and wait ull to have pressure P 2001 m 2.5 MPa i 40 Heat up the PCC pool water till to rexh the equibbrium 90 bulk averare temperature asteadv state conditionsi 100 Operaie $ alves F001. F005. F006 0f teautred adjust valves l FD25 and F007) to reach steam llow F 100l+F 300l=(sec
! table N 10 for the required steam tiow t controllmg that the
' temperature T 4002 shall he less than IKO *C i
Doemment j Rev Page of SIET I woone desun Irvumtm i (0098PP91 i 0 179 < 225 PANTHERS PCC TEST PROCEDURE TESTS %TTH TWO MODULES Page_2,_of __2 Test troe A 13 - Steam Only (Air in PCC Tubest Test a 50-53 Tioe Desenptmo Note Status Oper. Pbase s l Signet. 110 Measure the PCC mkt pressure P-4002 and adjust PCC inlet (*) See table condauorts m order to have the required followmg N.10 condiuors:
- F 1001 + F-3001 = (*) Kg/s T 4002 = (*)'C (mmumum superheaung degree 6*C) and wait to reach Sicady State CorW11tlOrts Open parually valve F051 and adjust vajves R)$1 and F008 F 2002 has 120 beci idl to have an att flownte F-2002 s 0.006 kG/S c*u'=M at P=300 kPa andt=134'C Cease tesung when pressure P 4002 stops meressms or 130 . rnessure P 4002E790 kPa Note Date Expenment Manager Sigasture I
l 4 l l l 1
Doc ""** ' Rev Page of SIET l l l ence.e demmn innovenvi an00RPP91 0 i 180 ( 225 PANTHERS PCC PRE. TEST CHECK LIST TESTS %TTH TWO MODUl.ES Page.,L ,of 1_, rinne Test troe A ' 1 Effect of Pool Water level-Saturated Steam Test a 54 Descr.pmn Note Status l Opee. Phaw ai I Sirmat. 10 Venfy that the plant cont'iguiamn is complete and suitable for the scope of test type A.2.1. complete closed PASTHERS
. PCC test loop
; Venfy that allinstrumentauon awith the excepuon of The PCC 20 Instrumentat l instrumentauon of att injection line 2) has been tabbrated.
I installed, filled. sented and is in operation ionis I included Venly that the Data Acquisition Systems is in operanon and 30 the conversion constants and formulas have teen correctly insened in DAS 40 Venfy that the followtng valves are closed : FN4. F038. F039. F009. F013. F037. FGa?. FD23. FN9. F015. F018. F036. F031. F032.F030. FDM. F028. F029. F035.F042.F041.F002.F003.F025.FD59.F011.F060.
' F022. F503 Venfy that the (clicwing valves are open: F019. and 50 F058. F007. SF001, F017. FO!9. SF003. S F002. F048. F007are parually
. FN6. F045. F033. F947. F055. F020 I open Venfy that the following satety valves are set at 1.0 MPa:
64 F016. F050. FNO
?O f Yenfy that the following control systems are available:
I LIC.Q001. T1C.1001. FIC.1001 M0 Venfv that numm C001. C004 att available Venf y that the tanks A001. A002. A003 are f ull if pools P 90 and Q are full. the
' tanks can be parually full 100 Venfy that the condensen are cooled t "Fluviale' pump is in operation s i
I l l l l
N"""' Rev Page j of I l SIET I 0000RPP91 1 0 i 181 225 eine desion inno sovi PANTHERS PCC PRE TFSr CHECK LIST TESTS WTTH TWO MODULES Page 1 d_2_, t.ae Test n ne A II Effect of Pool Water level Saturated 2.eam Tess a 54 snee Date Espenment Manager Signature
, . . - . . ~. - - . - - . . .
l 4 Dac "'= ' R" Page l . of . j SIET I I I
. in@RPPol 0 i- 182 ! 22.5 i
wwr.e denturi intumim -1 j PASTHERS PCC TEST PROCEDURE TFSTS WTTH TWO MODULES -l Pane i ou i Tstle Test tyve A TI Effect of Pool Water level Saturated Steam Tess a 54 , i c Description Note 5:stus Oper. ! Phase t i Sisast.
.. I normal '
10 l Set LIC.Q001 level set point = 4 26 m water level
; Surt pump C004 feed the pools and control level L-QODI =
20 i 4 26 m ' Open valve F(Mi and fill the condensate tans up to level L-LOO 2 = 1.75 m .Iwhen this levelis reached, the water starts The levelis 30 .i
- to drain m ime L. through F.LOGI 2.5 m above i the CT intet l nonle ,
40 Open valves: F002. F003. F004.F025. F059. F011 and purge AI the the PCC bv steam. t F003 must be fully opens opemns of valve F003 j steam starts to Dow , j j Start pump C001 and begm to desuperheat the steam I 50 noenine valves F012. F006 ' I Measure and record all mstrument signals mciuding 60 Acceleromet , f xcelerometers crs will be I recorded for > 10 minutes . t every 30
' mmutes
; Open va.ve F001 and incre.de the sic.im Dowrate l l
. I ,
?O j Throttle valve F019 im manual model in order to keep level l }
l_ i N0 ) L.LOGI hieher than 0.5 m and L. LOO 2 = 175 m l Open valves F005 . F001 and F006 o reach a steam tiow l
- rate F 1001 + F.3001 = 5 kc/s.controllmg that temperature .-
90 I T4f02 shall be less than IMO*C and pressure P 1002 less ' than 740 Kpa i Measure the PCC mlet pressure P.4t02 and adiust 100 'i temperature T 4002 acung on valve F006 m order to have '
's I I .uperheated less than 10*C steam at PCC mlet as:
of superheating l Heat up the PCC pool water till to Txh the equilibrium , 110 l hulk averste temperature # steady state conditions repeatens I I penodicallv phaws W1 and 100 j 120 i Adjust steam slowrate to the required value F.llol+F- , l 200l=5 Kess,contratimg that the steam at the PCC mlet ! 4 shall be superheated with the required superheating detrec I4T4002) l 130 ' Stop pump C004
'I
.r . .,.
D"'**at j Rev Pese at SIET I seraone Newinn inno-mm , un09RP NI o 183 225 PANTHERS PCC TEST PROCEDURE TESTS WTTH TWO MODULES Past 1 of_2_ iille Test nve A ' I EtTect ot" Pool Water level-Saturated Steam Tat a 54 Ptiase 8 I Desenptme Nase Steams Oper, I Sigmat , 140 Open valves F028. F029. F031, F032 and begin to decrease Open fully the level L-0001 and L POO1
!!0 Measure flowrat.ae F R001: if F.R001 ts lower the 5 Kg/s than open partiallv valve F035 160 Penodically repeat phase 100 170 Measure pressure P 4002 and level L-Q001:if P-4002=790 KPs and/or L-Q00l=2.2 m then start pump C004 and close valves R728. F029 F031. F032 and if open F035 Fall the pools tsll to reach the normal water level L.
1A0 0001=4 26 m repeattna penodically phaw 100 Stop the test 190 . Note i { l Date Espenseat Manater Sisasture j
Da""' R" Page l of SIET l I l i
! 00098PF91 0 i 184 225 so,a keson inresim PANTHERS PCC PRE TEST CHECK LIST TESTS %TTH TWO MODULES Page 1_.of_2__
Tess # M Tasse Tat noe A 2 2 Effect of Pool Water level Saturated Steam! air mirtures Description Note oper. Phascal l l Status Signat. 10 Venfy that the plant con 0guration is complete and suitable for the scope of test type A.2.2: complete closed PANTRERS i . PCC test loop 20 Venfy that all instrumentauon has been cabbrated. Installed. The PCC Alled. vented and ts in operation instrumentat son ts included Venfy that the Data Acquisition Systems is m operauor, and 30 the conversion constants and formulas have been conectly mserted in DAS 40 Venfy that the followmg valves are closed : F03R. F039. F009. F013. F037. F047. F023. F048. F015. F018.F036.F031.F032.F030.F028.F029.F035.F042. jFD41.F001.F002.F003.F004.F059.F011.F060.F022. F v1 P014 l l F055.F007 50 l Venfv that the followmg safety valves are open: and F025 j 5 F001. 5F002. 5 F003. F007. F025. FD44. F058. F049 are parually lF017.F027.Ffu5.F033.F055 open l V,enfy tnat the tollowmg valves are set at 1.0 MPs: 60 'F016.F050.F040 70 Venfv that the f ollowing control systems are available:
; PIC aOO2. FIC-1001. FIC.2001. T1C.1001. LIC 0001 i
x0 Venfv that pumps C001. C004 and compressors C002. COO 11 are available Venty that the tants A001. A002. A003 are full if pools 90 ; Pand Q are j full. the l
.! tanks can be
' > partially full ,
l 100 i Venfy that the conoensers are cooled i ~Fluviale" pump is in i e rai,oni
1 i i I
""""' R" i P* I d SIET l l -enme wemum inno-cm WO9RPP91 0 t 185 l 23 PANTHERS PCC PRE TEST CHECK LIST f i
TESTS WITH TWO MODULES Pw 2_,of_2_ ) Tem # 55-56 Title Test nne A 2.2 Effect of Pnol Water level-SaturatedSteamlair mirrures we l Date Espenment Mansaer Signature l 1 I i 4
4 Doesment 4 Ro l Page of 1 SIET 146 225 l u o9ftPP91 0 secone Mesion into asevi PANTHERS PCC TEST Pp.OCEDURE TESTS WITH TWO MODULES Page 1 00__ Tes: s 55-56 reuse Test twe A 2 2 Effect of Pool Water level-Saturated Steam! air matures Note Status l Oper. Descrrplaon Phase a i - 1 Sirast. I I normal 10 i Set LIC-Q001 level set point = 4 26 m I water level
' Start pump CON feed the pools and controllevel L-QUO! =
20 4 26 m Open valve F04 I and ritt the condensate tank up to level L. LOO 2 = 1.75 m .t when this levelis reached, the water starts The levelis 30 to drain ime L through F L001 2.5 m above the CT intet noule At the 40 Open valves: F002. F003. FON. F059. F011 and purge the opening of PCC by steam. t Valve F003 must be fully opent valve F003 steam starts to flow Start pump C001 and begm to desupertical the steam l i 50 openine valve F012. F006 l Measure and record all msaument signals includmg Acceleromet 60 accelerometers ers will be I recorded for 10 mmutes everv 30 j minutes J Open salves F001. F005 and F006 to reach a steam l
?O l flowrate F-1001 + F 100ls5 kg/s. controlling that l temperature T4002 shall be less than 160*C and pressure P.
i am2 less than 700 kPa l i Heat up the PCC pool water till to rexh the equilibnum l
- KO ' bulk averare temperature tsteadv state corditionsi I
i 90 l Start compressors C002 and C003.open partially valve FOOR l and aait till to have pressure P.2001- 2 5 MPa 100 Open valve F03R 1 I l ! i I
!!0 Open nartially valve FV104 and heem to inject air I
i Set the PICam2 pressure ses point equal to the PCC Pressure m 120 mmimum mlet absolute pressure value requtred (nr the test; absolute Ne table N.i t for the required pressure va.uel value l
D = "' Rev Page of SIET: i -I cuone Mexicri innovaim i. n009RPPQI O 187 225 PANTHERS PCC TEST PROCEDURE TESTS %TTH TWO MODULES Page_2, ( 3_,,, Test # 55-56 Title Test troe A 2 2 Effect of Pool Water level-Saturated Steamlair mixtures Phase n i Desenpuon j None 5 sses oper.
! I Sienst.
l Open valve R)08 till to have a air flow F 2001 or F 2002 = 130 if it is not j t we table N.ll for the required air flow valuel venfymg that the air pressure P 2001 must be higher than 2.0 MPs poemtde to reach the required aar Gow mcrease the operung of the valve R)09 Operme valves F001. F005. F006 (if requtred adjust valves 140 F025 and F007) to reach steam flow F 1001 + F-300latsee table N.ll for the required steam flow valuelcontrolling that the temperature T4002 shall be less than 180*C Measure the PCC inlet pressure P4002 and adjust PCC anlet 150 condmons in order to have the required following test (*) See table conditions: N.!I for F-100l+ F.300l=P) K g/s steam flow. F 200l=i') Kg/s air flow. P4002=t *) LPs (mmimum PCC inlet pressurei temperature PCC inlet I T 4002 must be superheated with a superheaung degree less pressure I than 10 *C i 160 Measure DP-025;if DP-025214 KPs mcrease PCC inlet essure tadjusting PIC 4002 set pomt till to have DP4)25 <
. . u Pa 17 0 If the Pressure set pomt of PIC 1002 has been changed (*) See table
, adjust PCC inlet conditions in order to hoe the required N.llfor
! ollowing f conditions: required
! PCC inlet F- 100l + F-300l =i a l K g/s condstens I F.200l=c*) Kg/s lP g 4002=PIC-4002 up date set pomt I
j T4002=superheatmg with a superheatmg degree less than
! 10 *C i
180 Set PIC 4002 controller m manual made and mantaan vent tank discharge valve a R)201 posioon throurhout the test 190 Measure PCC inlet pressure P4002 and adlus: anlet temperature T4002 in order to have super $cated steam at PCC inlet with less than 10*C of superheasant
i 1 i D ("" Rev Page of SIET ! l l l
' O +
IRA I 225
< ... .ne w e ern tw nm 0009RPP91 l PANTHERS PCC TEST PROCEDURE TESTS WTTH TMO MODULES Pase 2 of_3_
Tes # 55-56 T,tse Tat tyve A 2 2 Effect of Pnot Water level-Saturated Steam! air mtttures Ph ase s , Desenptu>o . Note Oper. Status l Signat. I I 200 Stop pump C0fM .
; Open valves F028. F029. F031. F032 and begin to decrease Open fully 210 I the level L-Q001 and L-P001 1 i 220 i Measure flowrate F.R001: if F.R001 is lower than 5 Kg/s I then open parcallv valve F015 230 Penodically repe.at phase 190 240 Measure pressure P 1002 and level L-Q001:if P 4002x790 KPa and/or L-QO0l=2.2 m then start pump C004 and close valves F02R. F009. F031. F012 and if open F035 250 Fill the pools till to reach the normal water !cvel L.
Q001 4 26 m 260 l Repeaune penodically phace 100 i l f i l i 2*0 Sinn the test Neue Date Expenment Manager Signature l
D**= "' Rev Page of SIET I l riOO9RPP91 1 0 189 225
*coone dennon troovoim i PANTHERS PCC PRE TEST CHECK LIST l TESTS WTTH TWO MODULES Page 1 of_2_ ..
Test s A.3,1 Title Test troe A.3 l- Simulated LOCA Pressuri ation Desenptme Nme . Stams Opee. Pbue#l sinnen-I 10 Venfy that the plant configuraton is complete and suitable for the scope of test type A,3.1: complete closed PANTHERS PCC toop, sacam bypass bne 7 connected to sicam ime I and bvpass valve F053 in operanon 20 Venfy that all instrumentacon . with exception of PCC tube wall thermocouples, has been cahbrated. mstalled. filled. vented and is m operauon = Venfy that the Data Acquasation Systems is m operaten and 30 the conversion constants and formulas have been correctly insened in D AS 40 Venfy that the following valves are closed : > F001.F002.F003.F005.F039.F008.F013.F018.F027 F028.F029.F031.F032.F035.F036.F015.F037.F041 FD42.F047.F004.F503.F048.F011.F059.FDl7.F046. F034. F053 Venfy that the following valves are open: 1909.1955. 50 5 FD01. 5 F002. 5F003. F007. F025. F044, F058. F049. 1907 and F055.F030.F045.F033.F038.F009 F025 are partially open V'enly that the following salery valves are set at 1.0 MPa: 60 lF016.FG40.F050 i 70 Venfy the followmg control systerrs are available: L!C.LOGl . PIC- 8002 MO Venfy that pumps C001. C004 and compressors C002. l C001 are available Venfy that the tanks A001. A002. A003 are full if pools P ' 90 and Q are full the tanks can be partially full 100 Venfy that the condensers are cooled ( "Fluviale" pump es in e neerationi 110 Venfv that the steam bvpass loop is suitable and in operation . I
SIET I
* * *' l Rev l Pac - j of s<none desvm Inno anvi (t @ 8PP41 0 1 190 6 23 PAVTHERS PCC PRE. TEST CHECK LIST TFSTS WTTH TWO MODULES Pmt* L d.2._
Test s A.3. l Title Test troe A 3 l- Simulated LOCA Pressurication Not e Date Expenment Mansaer Siansture
O r . l, Doemsset j. Rp Page {' at . , SIET I -I a009APPol 1 0 191 l 225-
< rame Weasuri innovstm ! ,
PANTHERS PCC TEST PROCEDURE ' l TESTS WTTH TWO MODULES
- Page I af_2 -
. Tenn e A3,1 s Tase Test troe A 3.1. Simulated LOCA Pressurr~ation .
Descripuos Nase - Status .. Oper. Simaan. j Phase s l 10 Open valve F041 and fill the condensate tank up ievel L. : LOO 2m 1.75 m then close F041 Set PIC 4002 set pomtm480 KPa. see PIC 4002 controller in
- manual mode
- and open valve F020 20 Measure and record all mstrument signals includmg >
M xcelerometers
!f required q 40 Start air compressor C002.C003 and want till to rexh a pressure P.2001a 2.5 MPa adjust valve F009 Operate valve F008 tall to have an air flowrate F 200lm F)
(*) this 50 k g/s. value willbe determmed later
- 5 Open fully valves F004. F053.F003 ;
Openmg ' 60 valve f003 .1 steam stans , i slowly to ! Ilow l Open valves fD59.F006 and start pump C001 to desup. cst
*0 f the steam l l Open pantally valve F002 40 E
90 l' bpen fullv valve F001 , b 100 Adjust desupemeaung xung on valve F006 m order to have steam in live 7 m saturauon conditions controlling pressure . P 7001 and temperature T 7001 Set LIC.L001 set pomt = 1.75 m and set LIC-LOGI 110 controller m ~ automauc mode
- controffmg level L. LOO 2 120 Open valve F0lR .;
Simultaneously periorm these acuons:
- switch controller PfC 4002 in *automaue mode': l 130
- open valve f005 l
- dose valve P053 ,
. .idjust desupeahenung m order to have saturated steam m ime 4 controllmr P 4002 and T-1002
) Want till to rexh pressurt P.a002=4MO kPa m steady stase 140 f condstaons l Stop the test ,
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Dae="' Rev age. { of . SIET. 1- I l-0 1 192 '- 223 snene Neuen Innowstivi 1009RPP41 - PANTHERS PCC TEST PROCEDURE - TESTS %TTH TWO MODULES - Pase_2_.d_2_., ;
'1 Titse Test rvoe A 31. Simulated LOCA Pressurtration _ Tessa A.~3.1 )
Descripame Nase States. Oper. Phaw
- i -
Signet.
- I i {
160 i Perform 10 Simulated LOCA Pressunt.arions starting with .i l FCC pool water tempenture less than 4PC-
?
%nte
.t I
a .
?
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Date Expenmes Mansuer Signature k l r
?
Dae**'"' - Rev Page of SIET } I i fiOmRPP91 0 193 225 wraone Mcminn Intevoti" PANTHERS PCC PRE. TEST CHECK LIST TESTS WITH TWO MODULES Page 1 -af l._. ! Title Test troe A 3 2. Simulated Leak Testine Tess e M i
~!
Descriptme Note Sensus Oper. ; Phaw s Simmas. ; 10 Venfy that the plant configurouon is complete and suitable for the scope of the test A.3.2: PCC pool full up to NW1. vent and dram ime closed. 9 Venfy that the following instrumentations has been 20 calibrated, mstalled, filled. vented and is is operauon: P. 200 i f.2001.T.200 i f. A001 f-40021-Q001.L.P00 l l. LOO 2. Venfy that the Data Acqutsauon Systems is operzuonal and 30 the convermon constants and formulas have been correctly > insened m the D AS 40 Venfy that the following valves are closed : t F001.F002.F003.F059.F0ll.F013,F018.F007.5F002. , SF003. F017. F018. F033. F034. F503. F039. F028. FD29 F011.F032.F03R. F009.partily 50 Venfy that the followmg valves are open: open F03R. F000. SF001. F044. F015. Venf y that the control system P!C.L001 is available i M 1 70 Venfy that the followmg saf ety valves are set at 1.0 MPa: FD165050 : 1 , MO ! Venfv that compressors C002. C003 are available i
%ne
, Date Espernment Manager Sistnature y ,..-e. -....3-, -y , -p-.,- 9
,, . . . . . . . . _ . - -. . . - .. - - - . . . ~ . - - - .
Rev Pase . of Document l- l l
. SIET 1
'~
arr)08PP91 - 0 I- 104 1 215
<.wmc n eanon Innevanvi
- PANTHERS PCC TEST PROCEDURE '
TESTS %1TH TWO MODLLE.S t_L,.of. _. P l 1 T est e M 1 Titte Test rvne A 3 2- Simulated Leak Testine .1 Oper. ;; Descripuos ~ Nose - ' Phase a ! l Status Signet. I - 10 l Open valve F041 and fill condensate tank till to have 3 l *ater level L. LOO 2 a 2 m. when the required level ts :
' reacned clow valve RMI 'i
- Set PIC LOGI pressure set point equal to 559 MPs and set j I the pressure controller PIC LOOL in
- automatic mode
- 20 ,
j Start compressors C002. C003 and wait to pressunze this phase tank U M l till to about 2.8 MPa shall be performed , only at the first cycle of exh testmg dav 40 l- Aleasure and record all instruments t Operate valve FOOR and adjust att dowrate in order to have 50 f F-200lm 0.2 Kejs. When P LOOlsd59 MPs asteady state condiuons) is rexhed 60 wait for i minute if the check for leaks es not performed Look at PCC pool water sur' ace from the manhole and cinect this phase l*1 for leaks of PCC by venfymg the absence of air bubbles -t shall be performed at .
' the first ,
i cycle and after every j . 50 4 > pressunzauo I j n eveles i t i Close valve F008. set PIC.L001 in " manual n Je", open i 40 l valve Fn21 and depreuurire the svstem 90 Stan a new pressurizauon cycle repeating phases 4 20 40.50 60.70M0. 100 Perform 100 preuunzation eveles to complete the test. u l
Dwomme Rn. Page of SIET I l ' t an09gppgl -4 0 1 195 ' 225 wnone Neurn learm :} P ANTHERS PCC TEST PROCEDURE '! TESTS WTTH TWO MODULES
.Page 2__of,2_ .
Title Test troe A 3.2. Simulated Leak Testine Test a M } 6 Nrne E v
}
f
.i i
9
.~
l a i 6 Date Expenment Manager Signature : - - - . ~ - . .. .- . .. -- s . , . .
. = .. - -- - .
[ of . D*c ="' Reo Pese l: l
- i. SIET I
' 196 225 ,
00@RPP91 O ! sencme Hemian Inte*m's < PANTHERS PCC PRE. TEST CHECK LIST TESTS WTTH TWO MODULES Pase L d.1 Pressure losses air only Tess s A.4 Tisse Test noe A .I Note Status Oper. Descriphon Signat. Phase 81 I I 10
> Venfy that the plani con 6guration is complete and suitable
! for the i.urg of tes A 4 :
Venly that the following instrumentatson has been : 20 . calibrated. installed. Giled. vented and is operation: I .F.2001. P.2001. T.2001 -;
.F.T001. P.T001. T.TD01
.P-.1001. P 4002
.L.L001. L. LOO 2. P.LOGI '
DP-001. DP 002. DP4103. DP-fnt. DP405
.DP-006. DP407. DP-008. DP409. DP.010
.DP-011. DP412. DP413 '"
.DP-014. DP-015. DP416. DP 017. DP418 DP.019. DP-020. DP 021. DP 022. DP 023 .
.DP 024. DP-026. DP.027. DP428. DP 029
.DP430 P. A001. P 1001 Venfy that the Data Acquisioon Systems is in operauonal 30 and the conversion constants and formutas have been correctiv insened in D AS All the 40 Venfy th the following valves a;.'c closed :
purge and
! vent valves .
lF001,F002.F003.F011.F013.F015.F017.F0lH.F023. .; must be
;F025.F037.F039.F041.F047.F048.F055 closed F009is '
50 ! Yenfv that the tollowing valves are open: parually I F009.F020.F038.F044.Fot9 open l-I5Fn01.SF002.SF001 , i Venfy that the followmg salery valves are set at 1.0 MPa: l 60 .F016.F050.FG10 l
! and the vasie FAtt n set at 4 MPa 70 Venfv that the air compressors C002. C003 are available l l Veniy that the followine contro! systems are available: PlC 4t02 in i 40 " manual mode" PIC 4002
' FfC.2001 1
I I
')
h= a ' Rev Page d i SIET l } ~ersone Nearun innovsam i r10098PPQI { 0- l 197 H5 PANTHERS PCC PRE TEST CHECK LIST TESTS WITH TWO MODULES Pas,_2_,,d_1_. Tests A.4 Tisse Test nve A 4 Pressure losses air oniv % <w e Date Experiment Manaaer Sianature l l 1 1 i l
Page of
. Doce m ..a . .l SIET l 198 I 22.5 00098PP91 F 0 t
< re m neuen inno*u m i PANTHERS PCC TEST PROCEDURE TESTS WITH TWO MODULES Page_.L.of_?,_._
Titse Test ryne A J Pressure losses air oniv __ Test a M Note Steens Oper. Descriptem Phase ai Simast-t 10 i Open the valve F041 and fill the condensate tartk up to
; level L-LOO 2 s 1.75 m. then close F041 I
, Start au compressors C002. C003 and wait stil to reach an If requued 20 air pressure P 2001 a 2.5 Mpa adjust valve ,
R)D9
' Operate vahe F0081if required adjust valve F009) ull to have an air flo* rate F 200l=0.25 kg/s P 2001 must 30 be 21.0 MPs If reqtured 40 Operate in " manual mode' valve F020 ull to xach a open valv:
pressure P 100l+DP-023+DP-030=110 kPa F055 i When steady state condicons are reached measure and l ,
!0 l record all instrument for 300 s Operate valve F008 tai required adjust _ valve F009) ull to .
have an att flowr:re F-2001:0.4 kg/s P-2001 must 60 be 21.0 MPs
; Repeat phase 40
?n i ;
! Repeat pnase 50 40 P 2001 must 90 , Operate vavle FOOR of required adjust valve F009) till to he 21.0MP3 i *
' have an air tiowrate F 200!=0.6 ke/s l l
! i l '
100 t Repeat phase afi i a l .
!!0 ! Repeat phase 50 .
! P 2001 must 120 l Operate valve F008 Of reyutred adiust valve F009)he till21.0 to
} have an air l'owrate F 200lm).7 kg/s MPs i
1.20 Repeat phase 40 140 Repeat phase 50 l I P-2001 must I
!!0 Operate wavle FD08 tif recuired adjust valve F009) till to l he 21.0MPs I have an air flowrate F 2001mRM Kt/s 160 Repeat phase 40 l
l l i I i
9 Dermet Rec Page of SIET ; .l-
.00098PP91 -t 0 199 225 4enone Mesum Innovnim t PANTHERS PCC TEST PROCEDURE TESTS WITH TWO MODULES Pase.l of_L. :
Titu Test rvce A.4 Pressure losses air only Tees a M Descriptsos Nase Staeus Oper. , Phase s sw , 170 Repean phase 50 180 Operuse vavle F006 (if required adjust vavle F009) till to have an aar flowrate F 2001 a i kg/s Repean phase 40 190 l Repeat phase 50 200 l Stop the tes: 210 Some
.i I
-g I
e Date Erperiment Manaser Signature I 1
- + , .
d Docia Rev P*se j d SIET I I igs gppor o > 00 ; :3 n2one xcuian innovoim PANTHERS PCC PRE. TEST CHECK LIST TESTS WTTH ONE MODULE Page I o( L Title Test txne B I Steam Only INo Air in PCC tubesI Test n 66+72 Descripum Note Staans Oper, Phaw si l i Sittmat. 10 Venf v that the plant contiguration is complete and suitable
, for the scope of test type B.l; complete closed PANTHERS i . PCC test loop . one module. pool P with dzaphrarm Venfy that allinstrumentation Iwith the etception of The PCC 20 instrumental
!I iinstalled.
nstrumentation of as filled. vented and airm mjection operauon ime 2) has been sonis calibrated, I mciuded l Venfy that the Data Acquisition 5ystems is in operation and 30 the conversion constants and formulas have been correctly insened in D AS 40 Venfy thas the following valves are closed : i Rua. F038. F039. F009. F013. F037. FG17. F023. FN9 IF015.F018.F036.F031.F032.F030.F034.F023.F029.
;F035.FG42.F041.FD02.F003.F025.F059.F011.F060.
F022.F501 4 Venfy that the followmg valvc; an open: F019. and 50 ,
- F058. F007,5F001. F017. F019. 5F003. 5F002. F04M. F007 are pantally FN6. FG15. F033. F027. F055. F020 noen Venly that the following salety valses are set at 1.0 MPa:
60 F016. F040 FNO
*0 Venly that the followmg control systems are avaslable:
4 Lic-ryyll . TIC.imi . FIC.1001 I
! i 40 Venty that pumps C001. C004 are available 1
, Veniv that the tanks At101. A002. AOO3 are tull If pools P.Q 00 are full. the tanks can be partially full i I
l 100 Venf y that the condensers are cooled ( *Fluviale" pump is m l operationi
, ~. = . . . . _ . . - .. . . -. .. ..
Reo Page of . .g D* **" ' SIET l l > 00098PP9I 1 0 ! 201 225 . woone kemum tanewm 1 PANTHERS PCC PRE TEST CHECK LIST TESTS WITH ONE MODULE i Fane.1- ei1 T ne Test troe B 1 Steam Only (No Air in PCC tubesI Tens a 66+72 h
-}
Nrm e I i
)
i I i e i
.i l
l Date Expensent Manaaer Signature 3 i t I g,, i s
. . . . , , , _ _ - . . - . . .- . ~ , . .
of SIET ! Doc ="' l Rev Page l i ar109MPP91 0- t 202 I 225 l
-e wne deanori inimauve i i
PANTHERS PCC TEST PROCEDURE TESTS WITH OSE MODULE Page_,L ,of L Test a 6&72 ' , Title Test noe B l Steam Oniv (No air PCC tubesi Dewription l Nase Status l Oper. ; Phaw # I I I - Sismat.' _; i normal 10 .l Set LIC-Q001 level set point = 4.26 m water levei
; Start pump C004 feed the pools and controllevel L-Q001 = l l I l_
20 : 4 26 m 'f 30 l LOO Open valve 2 = 1.75 F041 m .t
- hen this leveland fill the is reached, the condensate water starts The levelistarsk up to level L-to drasn m ime L.through F L001 2.$ m above the CT inlet noule E
At the 40 Open valves: opening of FDN, F002. F003. F025, F059, F011 and purge the PCC by valve F003 steam (F003 must be tully openi steam starts
' to now ~
Start pump C001 and begin to desupernest the steam $0 opening valves F012. F006 l Measure and record all instrument signals ir.cludmg Acceleromet 60 l' xccierometers ers wtil be , recorded for 10 mmutes every 30 minut-s
' Open valve F001 and increase the steam tiowrate in
' Throttle valve F019 im manual model m order to keep level l I.
Ma i L 1001 hieher than 0.5 m and L.ll)02 = l.75 m * )
, Open valves F005.ind F006 to rexn a steam tiowrate F. l 90 ! 1001 + F.100l=
- kg/s. controllms that temperature T4002
- See table l i 12 for steam
[ shall be less than 180*C and pressure P4002 less than 790 Dow mlet I, Kpa conditions ,
, Measure the PCC inlet pressure P4002 and adjust 100 ' temperature T4002 acung on valve F006 m order to have superheated stearn at PCC inlet as:
tess than 10*C of superheating Heat up the PCC pool wster till to rexn the cuuibbrium } j i bulk aversee temperature tsteady state conditionst repeating j 110 I ,
' periodically priases 90 and 1(X) ,
- See table 120 Adjust steam dowrate to the required value F.100l+F.
300l=* Kg/s,controumg that the steam at the PCCinlet 12 for steam shall be superheated with the required superheatmg degree Dow nlet conditions iT 1002I
Dact'*"' R"' Pae'- of I SIET l inn 098PP91 ! O I 203 225 , emme Neanon Inmasive r b PANTHERS PCC TEST PROCEDURE , TESTS WITH ONE MODULE Page_2,_,of ,2 Test nne B 1-Steam Only INo air PCC tubes 1 Tan a 66+72 Tisse Desenptsoe Nose Seness Oper. Phaw a SieneL P 130 When Steady state condauons are texhed. keep me.asunng and recortiang allinstrument signals for 15 minutes 140 Stop the test if0 Change PCC steam inlet conditions : Note t h i
'f
[ Date Espensseet Manaaer Signature I l
N == Ro Page of
' l l l SIET n009APPH i 0 t :04 l 225 s none k cancri Inrewstivi PANTHERS PCC PRE. TEST CHECK LIST TESTS WITH ONE MODULE Page i .of,2__
r,ste Test nne B I. Steam Only tAir in PCC rubest Test n 13 74 Descripton Note Status Oper. Ph4w a i Signat. Vent line 10 ; Venfy that the plant configuraton is complete and suitable closed:
' for Lbc scope of test typeB.1: one module. PCC pool buffled temporary test loop with temporary hne connecting the l' att supply hne not hne with valve F051 shown in the
! P&ID The PCC 20 ! Venfv that allinstrumentation has been cahbrated tnstalled.
instrumental
' filled. vented and is in operation ionis included Venly that the Data Acquisition Systems is in operaten and 30 the conversion constants and formulas have been correctly inwned in DAS 40 Venfy that the followmg valves are closed :
F038. 5F004. F009. F013. F037. F047. F015. SF002. F051. F017. F036. F031. F032. F030. F028. F029. F035. F042. Fnt 1. F001. F002. F003. F004. F059. F011. F04). F022. F503.F014
! F007 and !0 l Venfv that the following valves are open:; S F001. F039. SF003. F007. F025. FD64.
F025 are partally
! F045. F033 open
; Ventv that the following valves are set at 1.0 MPa:
'l e4 F0f 6 F050. F040 70 l Venfv that the following control systems are available:
1 i 1 I LIC.llol FIC.1001. F1C 2001. TIC.ltial . LIC-0001 40 Vet 11y that pumps C001. C004 and compreswrs C002. {' C001 are available If pools 90 Venfy that the tanks A001. A002. A003 are full Pand O are full, the I tanks can be i ! I I pantally full 100 Venfy that the condenscrs are cooled ( 'Fluvtale" pump is an i operationi f 1 l
~ D " = '** Rev l Page l of l SIET I I no098PPol 0 205 1 225
-enw Nemon innovoim .
PANTHERS PCC PRE. TEST CHECK LLST TESTS %1TH OSE MODULE Page 2_ of_2_ Title Test noe 8 f -Steam Only (Air in PCC tubess Test s 73+74 wue page Espenment Manaaer Signature
, ~ ,- .- - - n. -
n ~ . -- . . . . ~ . .- - i
""- Page -l. of
.I Da* *"* ' i 1 r SIET 223
' 0000RPP91
' O I 206 1 wi.ione deanon innoveuvi :
i PANTHERS PCC TEST F ROCEDURE . , TESTS WITH ONE MODULE Page_ Lot 2,_ l Titse Test nve B I -Steam Only (Air in PCC rubesi Test n 73+74 , Descriptaon Note Status . Oper. _ l Phase s , Sissat. j [ 5et LIC-Q001 level set pomt = 4.26 m. normal 10
' wata level
,i Set LIC. LOO! level ses pomtal.75 m (level comroued by L. '
LD02) 1 l
! Start pump C004 ieed the pools and control level L-Q001 = I
- - 20 ! J 26 m f
; Open valve FDsI and fill the condensate tank up to level L-The level as 30 i LOO 2 = 1.75 m .
2.5 m above '#
' When the level L-L0002:1.75m is reached close valve the CT inlet FD.11 and conuel the level L LD02 in automatic mode !
nozzle 40 Open valves: F002. F003.1904. F059. F01 I and purge the PCC bv steam. acting on valves F037and F507 ' Start pump C001 and begm to desuperheat the steam i' to noenme valves F012. F006 j Measure and record all mstrument signals meludmg Acceleromet .[ 60 ccelerometers crs wtilbe , iecorded for I lammutes f i every 30 . minutes f
; Open valves F001. F005 and F006 to reach a steam !
70 ) Howrate F-1001 + F-300l>5 KG/S. controlling that ',
, temperature T 4002 shall be less than 180*C and pressure P-
' Ann 2 less than 740 kP3 l
- Start compressors C002 and C003.open a little valve F008 i
M0 and wait till to have pressure P 2001a2.5MPs l ( l
! Heat up the PCC pool water till to rexh the equibbnum ! !
f 90 I hulk averare temw ;ure esteady state conditions # / 3 100 i Operate valves F001. F005. F006 tif required adjust valves '!
~ Pn25 and F0071 to reach steam 11ow F-100l+F.3001= we !
table N.13 for the required steam 00= > controlhna that the l temperature T an02 shall he less than 1MO*C l l ; Measure the PCC inlet pressure P4002 and adjust PCC mlet (*) See table ' 110 conditions m order to have the required followine N.13
~i
; sonditions: ,
a: j: F-100l+F 100l=t*I Kg/s > t T4002=i*i'C (mmimum superheatmg degree o*C) and wait : l to reach steady stase condstions 4 1
. _ _ .i
D ' """ ' Reo l Pate l of SIET I l seam weation innovaim i 40CNRPWI O 207 l :3 PANTHERS PCC TEST PROCEDURE TESTS %TTH ONE MODULE Page_2_.of_2__ r,sse Test nve B 1 -Steam Only (Air in PCC tubest Test a 73+74 Dexnptum Note Status Oper. Phase s l Skaat. I Open panully valve F051 and adjust vajves F051 and F008 F-2002 has 120 idi to have an air Dowrate F-2002a0.003 Kg/s been calculated at i P=300MP l and := 134*C l Cc.ne tesong when pn:ssure P 4002 stops increasmg or 130 i pressure P 4002a790KPs Nwe Date Expenment Manaaer Signature I
Dac== Rev Page j ' of SIET I 1 l 4 0 t 208 f 215 f wnonc deston twaim - m09RPP91 i PANTHERS PCC PRE TEST CHECK LIST TESTS %TTH ONE MODULE Page 1 of,2,_ j r,tse Test nne -8 2 Effect of Low Densirv Noncondensibles Teen s 75+78 Description Note Oper. , Phaw s, l Staeus i - Signet. S Vent ime 10 ! Venfy that the platit configurauon is complete and suitable for the scope of test type B 2.: one module. FCC pool buffled closed: lest loop with temporary hne connecung the l' air supply temporary hne not Ime with valve F051 shown m the , Pa!D - ! i l The PCC - 20 l Venfy that all mstrumentauon has been cahbrated.instaded. instrumentat filled. vented and is m operation sonas ; included Venfy that the Data Acquistuon Systems is m operaton and ! 30 the conversion constants and formulas have been correctly. msened m D AS 40 Venfy that the following valves are closed : f F038. 5F004. F009. F013. F037. F047. F015. SF002. F051. j F017.F036.F031.F032.F030.F028.F029.F035.F042. ! l Fo* 1. F001. F002. F003. F004. F059. F011. F060. F022. t6.803.F014
} F007 and ,
50 ; l Venty that the followmg valves are open:S F001. FU25 art F039. SF003, F007. F025. FN4. F058. F018. jF g parually jF045.F033 open l Ventv that the followmg valves are set at 1.0 MPa: ' fio IF016.F050.FNO e 70 Venfy that the following control systems are avasisble-LIC LOGl . FlC-tml . F1C.2001.T1C.lmi. LIC-0001 40 Venfv that pumps C001. C004 are avait le l l Venfy that the tanks A001. A002. A003 are full If pools 90 i Pand Q are full. the tanks can be partially full 100 Venf y that the condensers are cooied i 'Fluviale" pump is in operation 6 1 1
+
4 l
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D'*** l' -l SIET ' I' i I 209 225 -_ l i d()D9RPP91 ,- secone Hemian innovenvi PANTHERS PCC PRi> TEST CHECK LIST TESTS %TTH ONE MODULE - Page_2_,,of_2.,,_
^ Tenn s 75+78 Tisse Ten troe -B 2 EWect of Low Density Noncondensibles
' I Note Siness - Oper. . '
Desenpuos - Phase a Sirast. Hebum for 110 Venfy that Hebum bottle or ar/Hebum 13 A part of at and i tests 75,76 part of Hehum) bonic has been connected to valve f051and as/Hehum for tests 77. . 78 r li installed Vertfy onthat the Hebum or ar/Hehum bottle has been a suitable weighting machine : 120 *
-i Nme I
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Paste of SIET
- Dac = I Ry l l w m ee Heaimn inno**'m 00fAMPP91 0 2!0 f 225 -
PANTHERS PCC TEST PROCEDURE TESTS WTTH ONE MODULE Page i of _2_. Titse[est nrcB 2 Effect of Low Denstry Noncondensibles Test a 75+78 Ph aw a , Description N ote iI Status l Oper. j i Signet. Set LIC-QOOI level set pomi = 4.26 m normal 10 : water level
! Set LCl LD01 level set potnt=1.75m tievel contreued by L.
I Ln02 1 Stan pump C004 feed the pools and control level L.Q001 = l l I f. 20 1 4 26 m i Open valve F041 and fiU the condensate tard up to lesel L.
' LOO 2 = 1.75 m , when the level L.L002=1.75m is reached. The level ts 30 i
close valve F041 and control the level L. LOO 2 m automauc 2.5 m above mode the CT inlet nouje i 40 i Open valves: F002. FD03. F004. F059. F011 and purge the At the l PCC by steam. acting on valvet. F037 and F507 openmg of valve F003 steam starts
' to flow l Start pump C001 and begm to desupertest the steam j
~* I openine valves F012. F006 l
; Me.uure 34.3 record all instrument signals mcludmg 60 j xcelerometere Acceleromet ers will be recorded for 10 mmutes every 30 g
mmutes i Open valves F001. F005 and F006 to reach a steam 70 l flowrate F 1001 + F.300l>5 kg/s controlling that I temperature T t002 shall be less than 180*C and pressure P. l f 1 4002 less than 700 k Pa Heat up the PCC pool water till to rexh the equibbnum l I 40 hulk aser3re temperature atteady state conditions) 90
- Operate valves F001.F005. F0061if required x!)ust valves FO 5 and F007) to texh steam flow F 100l+F.3001: ewe
! table N 14 for the requue? steam flows controllmg that the I temperature T 4002 shal be less than IMO*C 100 Measure the PCC inlet pressure P 4002 and adjust PCC mlet (*1 See table sonditions m order to have the required followins N.14 l conditions:
l F 100l+F.300!=i') Kg/s l
; T,4002=t * >*C (mmimum supertestmg degree 6'Cl and want
! to reach steady state conchtsons
! l 110 i
' Weight the bottle the weight is : .Kr 4 i
1 l 1 l i
Doc ="" ' Rev Page l of SIET i I l mm desirsi imerm firmWPPQ1 1 0 211 1 225 PANTHERS PCC TEST PROCEDURE TESTS %TTH ONE MODULE Paae i oO _. Tase Tar rvne -B 2 Effect of Low Density Noncondensibles Test a 75+78 Descriptaos Nate Status Oper. Phaw a Signet. Open valve F051. op:n botue valve and adjust the botue The pressure 1:0 pressure reducmg valve. Start a chronometer to measure the bleeding time of the gas into the steam. The Helium mass reducmg Doweste (tes N.75. 76) should be about 0.0002 k g/s. valve possuon to The air / Helium mixture mass nowrate ttest N.77. 78) should be about 0.0008 Kg/s.\ obtain the required gas Dowrate can t2 l, determmed tefort testmg When pressure P-1002 stops increasing or reaches 790 kPa 130 close gas bottle. stop the chronometer and weight the bottle:
- the gas injection time is.. s
- the bottle weteht it.. .ke j Stop the test l I.
140 i Nrwe Date Esperiment Manager Mgnature
Doc m at Rn Page l of SIET l l l 40098PP91 i o t 212 ! 225 w uc.ne demuri innovum PART 111: QUALITY ASSURANCE PLAN TABLE OF CONTENTS 212
- 1. INTRODUCTION 214
- 2. DESIGN RECORD FlLE 215 A PRE TEST CONTROLS AND PROCEDURES
- 4. TESTING CONTROLS, PROCEDURES AND RECORDS 218 219
!. DATA REDUCTION AND AN ALYSIS PROCEDURES 220
- 6. DESIGN VERIFICATION 220 h1 Document ventkauon i
i
T Doca m t Rev . Page - of l l l SIET i 0009RPP91 I O I 213 I ::.5 ;
<enca Nemiori innovoim I
- f. INTRODUCTION The tests in the POTERS frihues are performed by SIET under a research contract with ENEA. m the '
tramework of the four. party Agreement (General Electnc. Ansaldo. Enel and Eneas on the Design I Development. Procurement. Fabncanon and Tesung of ICS and PCCS Components.Besides PCC tens performance, the contrxtual Siet atuvmes include' the design and implementauon of the facthty modificauons necessary to xhieve the best condiuons for test perfonnance; and all addauonal services Enea may request. mcluding specific acuon necessary to perform the tests in comphance with the Quably 1 usurance Requirements. This secuon summarizes the contents of the document "Quahty Plan (cr the Wort Orders m the Nuclear ves' (00006.QQ). with parucular regard to aspects of interen fcr - or spect5c to PCC tesung in the PANTHERS facshty. The purpose of the QA Plan is to define the actions necessary to assure that the tests are performed in ' manner such that high quahty, non ambiguous data is obtamed, that the data have been processed. all these steps . reduced, mterpreted. and pubbshed m compliance with fully qualified procedures. that have been checked using appropnate venficauon means, and that Mequase records of these data are kept. ~ Siet's Organization (staff; Technical Service; QA Unitst is citensively illustrated in the above menuoned l Quahrv Plan. Enea s Orgaruzauon is represented by: 2 the Test Program Manager (RPS), w ho coordinates all the technical /administrzuve activiues L relauna io the Test Program and the official relanonships among the Orgaruzauons involved; the Responsible Tes: Engmeer tRTE),appomted with the agreement of the Test Requestor (GE) as the RPS's delegate with the assiened responsibihty for making the reviews, approvals venficapons
.md decisions on technical matters as designated in Secuons 3.6. 3.7 and 3.8 of GE's IC/PCC t Test Requirements Specificauon 5 I
-l l
l 1
J Reo j Page j of j Doc =*a' l SIET l f un04HPP91 , 0 i 214 i 225
< wwie Aceiori trinovan*i
- 2. DE. SIGN RECORD FTLE IDRF) ul information received by SIET or issued by SLET for etternal distnbuuon are recorded and filed in the DRF under the responsibibiy of the IC PCC Profect Manager tRPG)in order to keep full traceabdity ot input data.
DRF is Icrmed by files where documents. letters, fates. teletes. reports, etc. are subdmded acconimg to me issuing Organization and collected m a progressive and chronological order. Documentauon filed m the DRF enables to reconstruct at any time the development of project acovsties. Input data contamed m the DRF and actually used, are taken from official documents, which are venfied
.in d issued W SIET and then approved by ENENs Test Program Manager tRPS) (or Responsible Test En nect RTE 1 and (if required by the Work Order provisx>ns by other external Orgaru.zauons. . DOC. SIET 0006 - QQ- 92 QUALITY PLAN Sect. 4.3.1)
i Doc === Rev Pate of l l SIET I wnone Reaturi frmveneve , 0009 APP 91 1 0 l :]$ i 73 l A PRE. TEST COVTROLS AND PROCEDURES Bef ore the beginnmg of tests, the cortectness of plant configuraDon is v.nfied by using a Check.Ltst of prehminary controls. Final control of cortect plant preparation is perform.d by the Espenments Manager. .ind conftrmed by his signing the Check. List. The signed Check Lists are filed m DRF and in SIET File. DOC. SIET 0006. QQ . 92 QUALITY PLAN Sect. 7.1) l
Da**aseet Reo Page- et SIET I 225 (OfRAPPol i O 216 scraone Memenri in mveuvi 1 IC.PCC / PANTHERS , PRE. TEST Q A CHECK LIST i TEST SERIES- . P i The persormel meet the requirements for any of their posiuon. They have been tramed in the requartments J and responsabsbues of each of them for the test program. . POSITION I QUALIFICATION l I i ,
, I I
i DAN UGQ 1 The Iollowmg procedures related to test pcrtormance have been regularly issued and vertfsed:. i
'~
APPROVED l .NOT APPR. DAN UGQ PROCEDURE l I ! ' l ! l t The DAS (Data Acquisition Systemt has been venfied as presenbed m Doc. 00098 PP 91 Rev.0, Part I and it w as f ound in accordance w sah prescriptsons. YES NO . DAN- UGQ 4 Plant Log and S AD Log have been regularly prepar-;.
-i YES NO DAN UGQ Date ..
** er' " "
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- r J r e---frm- -mi e 7hifh - e--fg---9 p 7 iN -+t f
b D"""' "' Page- of. SIET l 'l I l 0 I- 217 225
*none Neman tw-um i 00098PP91 IC.PCC / PANTHERS PRE. TEST Q A CHECK LIST TEST SERIES... ... - -.
l, TEST TYPE .. ..
- 1. The following systems of the facilities used for the test have been checked. informing all the Units involved.
NOT OK UNIT RESPONSIBLE OK i SYSTEM FACILITY ' i 4 DAN UGQ ;
- 2. Test Bnefing has been performed. -
YES NO DAN- UGQ
^
; PRESENTS QUALIFICATION - ,
I l' ) i i I t-D a te .. .. .. . . ..- . . t
... _ - . ~ . _ . . _ . . . _ - . _ _ _ - . . _ . . . - - -
Da'"""' Reo Page of SIET l }
, 0009RPP91 0 218 225 owne wennan innoveim
- 4. TFSTISG CONTROL
S. PROCEDURE
S ASD RECORDS b .dsted before, the Espenments Manager is responsible for the quahry of test performance and for the auahov of result.s obtained in the tests.In order to assure such quahty.each Test Pmcedure is compiened hv a Check Lis?. which is used to venfy the conect performance of every single step in the test. In this phase. the Expenments Manager has the authonty to introduce some modafacanons to the Test Prncedures if he deems such modsfacations necessary for attaining the required quality level of test results. Such modifrauons are reponed ;n an appropnate Deviauon Form (Doc. SIET 0006 QQ 92 QP Sect.7.2). When the modificauons affect Test Procedures approved by the Test Requessor, the Expenmets stanager has the duty to obtain approval by the ResponsibleTen Engtneer directly or via teles or fax. Such modificauons are included in the appbcable Check List. filed m the Test DRF. Any mstrument replacements are recorded both in the Test DRF and in the Insinament List. t k
?
, ~-. . y -
Doc "" ' Rev Paste l . of SIET , l n009RPPQI . 0 219 8 225 Aersone Newton innovaim !. DAT A REDUCTION AND ANALYSIS PROCEDLRES Test results are reponed in documents called *Espentnental Data Reporu*. containmg balances and songruence ana. lyses, as required by the single test procedures. These documents are sent to the Test Requestors for approval and to a work 2ng group including SIET. ENEA. ANS ALDO and Test Requestor, for revu:w and analysis. The wortmg group is co ordmated by ENEA's Espenmental Program Maruger (RPS). The procedures for data elaborauon and evaluauon are dealt with in specific documenu. Magnetic supports are archived in the Acquistuon Data room as well. This Documentanon is kept by SIET for a five yearf penod maintaaning also reading system of programs and magneuc supports efficient. the The ongmals of all the technical Documents contained in DRF and of Wort Order documents: documents produced dunng test xtivities (Plant and Test bgs: completed Check Lists: tratnmg reports and audits, etc.) the magneuc supporu of data recordings, are archived in a dedicated room, in order to l d in order to prr<ent the
.nsure their retrieval (File Cards: and their protection against damage or oss an xcess by unauthonzed people. . Doc. SIET 0006 QQ 92 QP Sect. 9 and 4.3) l l
., __ _ . . _ . . _ _ m _ . . . __ _ . _ _ _ ._ . 4 k:mt j Rev Page of SIET l on09APPol 1 0 220 225 sedne Hemian lesim A, ()ESIGN VERIF1 CATION ' This section retages to the steps ahoch must be taken in oroer to assure that all aspects O(test plannsng, tacthty constructen, testing procedures data reduction and data analysis are appropnately vmfied. and that adequate records of thts venficatson process are kept. l 6.1 Document verifkation
' Actually. the steps concernmg documents issue and venficanon procedures are dealt mth in the '!
internal procedure " Document Conuol' (0002-QQ). par. 5 + 12 and SIET 0006 QQ 92 QP Sect.'4. ' Facibly vertication. mecharucal and electncal sub-systems and controls, instrument installataan, instrument 5 calibrauon are specified in appropnate PRE TEST CHECK LISTS.- iSIET 0006 QQ 92 QP Sect. 7.1) l
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.. . . . . . . . . ~ i l Document Rev Page of SIET l woone peanari innoverm orX)9RPP91 0 223 225 i Enclosure 3 sammuseum open line ,l i a e a a e a cheart line ! i
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n009EPPH I O 224 2:3 senone Meannn intuwam i i
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- J I 1 i
L RAI Number: 950.24 Question: Provide a description of PANTHERS that contains information to facilitate review of the test plan and to develop a RELAP5 input deck, including:
- a. geometrical design data
- b. valve characteristic data
- c. instrumentation and calibration data
- d. control system data
- e. test documentation GE Response:
- a. Geometrical design data for the test facility will be contained in the document
" PANTHERS-PCC TEST FACILITY DESCRIPTION to be issued November 15, 1993.
- b. PANTHERS-PCC test facility valves are standard, "off-the-shelf' valves. The only readily available characteristics are the valve size and type which are indicated on the P&ID included in the Test Plan and Procedures. Since the tests are to be performed at steady-state and the valves are not part of the PCC, the valve characteristics do not impact the PCC performance.
- c. The instrumentation is described in the Test Plan and Procedures. The calibration data for the PCC instrumentation will not be available until the instruments have been calibrated..which is expected to be in November 1993.
- d. The PANTHERS-PCC test facility control system is shown on the P&lD drawing, which is included in the Test Plan and Procedures.
- e. GE believes that the available documentation on thePANTHERS PCC tests have been supplied either with this submittal or previously.
1X.) J
i RAI Number: 950.25 l Question: To facilitate the transfer of information on the PANTHERS facility, provide the TRACG input deck, noding diagram, and input description. GE Response: TRACG is currently being used for PANTHERS-PCC pretest performance predictions but the inputs have not been fmalized and adjustments are still being' made to the model. The requested input deck, noding diagram and input discription are expected to be available by the first week ofJanuary 1994. , t s i i 1 1 l l 30
i j q l
.i RAI Number: 950.26 Question:
1 Provide the following documents:
- a. Isolation Condenser System Piping and Instrumentation' Diagram, Drawing j No.107E5154.
- b. Isolation Condenser System Design Specification, Document No. 25A5013. ,
r
- c. Isolation Condenser System Interlock Block Diagram, Drawing No.137C9292.
- d. Isolation Condenser System Process Flow Diagram, Drawing No.107E6073. ;
- c. Passive Containment Cooling System Piping and Instrumentation Diagram, Drawing No.107E5160. .
- f. Passive Containment Cooling System Design Specification, Document No. f 25A5020. a
- g. Passive Containment Cooling Sptem Process Flow Diagram, Drawing No.-
107E6072.
- h. SBWR Composite Design Specification, Document No. 23A6723.
- i. Containment Configuration Data Book, Document No. 25A5044.
- j. IC H.X. Equipment Requirements Specification, Document No. SBW 5280 TNIXN014000. !
- k. PCC Equipment. Requirements Specification, Document No. SBW 5280 TNIXN015000. .
- 1. Passive Containment Cooling and Isolation ' Condenser Prototype Structural Instrumentation, Document No. SBW 5280-TNIX-1115000.
.i t
t 31 , 1 l
. . . . . - . _= - .. i I
- m. IC Pool Compartment Arrangement, Drawing No. SBW5280DMNX1103.
Documents listed in this question were referenced in the following:
- a. " Confirmatory Tests of Full-Scale Condensers for the SBWR Isolation -
Condenser System and the Passive Containment Cooling System," S. Botti, G. Fitzsimmons, and P. Masoni, undated.
- b. " PANTHERS Test Program," Presentation to the ACRS by P. F. Billig, June 2, l 1992.
- c. "Isoladon Condenser & Passive Containment Condenser Test Requirements,"
GE MPL Item #B32-3030/T15-3030, November 12,1992,
- d. "PCC Test Plan & Procedure," SIET 00096 ED 91 Rev. A, undated.
- c. " Technical Specification for PCC Instrumentation Installation," SIET --
00157ST92 Rev. A, undated. GE Response: Documents a.-SSAR Fig. 21.5.4-1 sh 1-2, c.-21.7.4-5 sh 1-13, and e.-21.6.2-1 are included in the SSAR, although the document numbers have been replaced by figure numbers Copies of the remaining listed documents are enclosed. , a k f i r 32
- _}}