i

NUREG/IA-0167

International

Agreement Report

Assessment Study of

RELAP5/MOD3 .2

Based on the Kalinin NPP Unit-1

Stop of Feedwater Supply to the

Steam Generator No. 4

repared by

S. Pylev

uclear Safety Institute

ussian Research Centre

Wurchatov Institute"

irchatov Square, 1

3182, Moscow

issia

ffice of Nuclear Regulatory Research

S. Nuclear Regulatory Commission

ashington, DC 20555-0001

-tober 1999

•ared as part of

Agreement on Research Participation and Technical Exchange

er the International Code Application and Maintenance Program (CAMP)

blised by ;I Nuclear Regulatory Commission
a - ýa t, A- I -'.I

|

/L

0.'

AI
ABSTRACT

This report has been prepared as a part of the Agreement on Research Participation and Technical

Exchange under the Code Assessment and Maintenance Program.

The data collected by Kalinin NPP Unit-1 Data Acquisition System and In-Vessel Monitoring

System during stop of feedwater supply to the SG-4 transient have been analyzed by using the

RELAP5/MOD3.2 and RELAP5/MOD3.2.2Beta codes. Kalinin NPP-1 is a Russian designed

four loop pressurized water reactor (VVER-1000, project V-338) rated at 1000 MWe.

RELAP5 code calculated results were compared with plant data. Sensitivity studies were carried

out to investigate the effects of modeling on major thermal-hydraulic parameters and to examine

a new heat transfer model for horizontal tube bundles.

III

I

TABLE OF CONTENTS

1.

2.

INTRODUCTION .............................................

KALININ NPP DESCRIPTION ...................................

2.1 Primary side ..............................................

2.1.1 Reactor Vessel .........................................

2.1.2 Core .................................................

2.1.3 Primary loops ..........................................

2.1.4 Pressurizer .............................................

........... 1

.......... 3

........... 3

......... 4

........... 6

........... 8

........... 9

2.2 Secondary Side ...................................................... 11

2.2.1 Steam Generator PGV-1000. ........................................ 12

2.3 Monitoring, Control and Protection System ................................ 18

2.3.1 Steam Generator Feedwater Control System ............................. 19

2.4 Plant Diagnostic Uncertainty Bands ...................................... 20

3. TRANSIENT DESCRIPTION. .......................

3.1 Initial Plant State ................................

3.2 Sequence of Events ..............................

4. INPUT MODEL DESCRIPTION .......................

5. RESULTS OF SIMULATION .........................

6. SENSITIVITY STUDY ..............................

7. RESULTS OF RELAP5/MOD3.2.2BETA CALCULATIONS.

8. RUN STATISTICS .................................

9. CONCLUSION ....................................

REFERENCES .......................................

APPENDIX-A ........................................

APPENDIX-B ........................................

APPENDIX-C ........................................

APPENDIX-D .......................................

..... . . .... +.... ...... 2

..................... 22

........... ... ... .... 22

..................... 24

..................... 31

..................... 33

..................... 36

..................... 39

..................... 40

. . . .. . . . .41 

.................... A -i

.................... B -1

.................... C-I

.................... D -1

O

V
LIST OF FIGURES

Fig. 2.1 Kalinin NPP, Primary circuit general view .................................. 3

Fig. 2.2 Reactor vessel axial view ............................................... 5

Fig. 2.3 Core M ap .......................................................... 7

Fig. 2.4 PGV-1000: Top View ................................................. 13

Fig. 2.5 Geometry of tube bundle .............................................. 13

Fig. 2.6 PGV-1000: Cross view ............................................... 15

Fig. 2.7 KaNPP-1 SG water level nomogram ..................................... 17

Fig. 2.8 Arrangement of SG level-meter vessels ................................... 21

Fig. 4.1 VVER-1000/V338. Primary circuit nodalization scheme ...................... 29

Fig. 4.2 VVER-1000/V338. Secondary side nodalization scheme ...................... 30

Fig. A-1 Reactor Power and Control Rod Group 10 Position ........................ A-I

Fig. A-2 Primary Side Pressure ............................................... A-2

Fig. A-3 Pressurizer Collapsed Level .......................................... A-2

Fig. A-4 Loop No.1: Coolant Temperature ................................ A-3

Fig. A-5 Loop No.2: Coolant Temperature ...................................... A-3

Fig. A-6 Loop No.3: Coolant Temperature ...................................... A-4

Fig. A-7 Loop No.4: Coolant Temperature ...................................... A-4

Fig. A-8 MCP No.1 Head ................................................... A-5

Fig. A-9 MCP No.2 Head ................................................... A-5

Fig. A-10MCPNo.3 Head .................................................. A-6

Fig. A-I MCP No.4 Head .................................................. A-6

Fig. A-12 Reactor Vessel Pressure Drop ........................................ A-7

vi
I

Fig. A-13 SG No.1 (Primary Side) Pressure Drop ................................. A-7

Fig. A-14 SG No.3 (Primary Side) Pressure Drop ................................. A-8

Fig. A-16 SGNo.4 (Primary Side) Pressure Drop................................. A-9

Fig. A-16 SG No.i: Steam Dome Pressure ...................................... A-9

Fig. A-17 SGNo.2: Steam Dome Pressure ..................................... A-9

Fig. A-18 SG No.3: Steam Dome Pressure ..................................... A-10

Fig. A-19 SGNo.4: Steam Dome Pressure ...... ............................... A-10

Fig. A-20 SG No.1: Collapsed Level .......................................... A-1I

Fig. A-21 SG No.2: Collapsed Level .......................................... A-Il

Fig. A-22 SGNo.3: Collapsed Level .......................................... A-12

Fig. A-23 SGNo.4: ColFapsed Levelr .......................................... A-12

Fig. A-24 SG No.l: Feed Water Flow Rate .................................... A-13

Fig. A-25 SG No.2: Feed Water Flow Rate .................................... A-13

Fig. A-26 SGNo.3: Feed Water Flow Rate .................................... A-14

Fig. A-27 SGNo.4: Feed Water Flow Rate.................................. A-14

Fig. A-28 Run Statistics: CPU Time .......................................... A-15

Fig. A-29 Run Statistics: Advancement Count Number ............................ A-15

Fig. A-30 Run Statistics: Time Step .......................................... A-16

Fig. A-31 Run Statistics: GRIND Time ........................................ A-16

Fig. B-1 SGNo.1: Tube Bundles (Layer 5) Heat Transfer Coefficient .................. B-2

Fig. B-2 SG No.1: Tube Bundles (Layer 4) Heat Transfer Coefficient .................. B-2

Fig. B-3 SG No. 1: Tube Bundles (Layer 3) Heat Transfer Coefficient .................. B-3

Fig. B4 SG No.1: Tube Bundles (Layer 1) Heat Transfer Coefficient .................. B-3

.vii
Fig. B-5 SG No. 4: Tube Bundles (Layer 5) Heat Transfer Coefficient ................. B4

Fig. B-6 SG No.4: Tube Bundles (Layer 4) Heat Transfer Coefficient .................. B4

Fig. B-7 SG No.4: Tube Bundles (Layer 3) Heat Transfer Coefficient .................. B-5

Fig. B-8 SG No.4: Tube Bundles (Layer 1) Heat Transfer Coefficient .................. B-5

Fig B-9 Primary Side Pressure ............................................ .. B-6

Fig. B-10 Pressurizer Level .................................................. B-6

Fig. B-iI Loop No.l: Coolant Temperature ..................................... B-7

Fig. B-12 Loop No.4: Coolant Temperature ..................................... B-7

Fig. 3-13 SGNo.i: CollapsedLevel ........................................... B-8

Fig. 3-14 SG No.2: Collapsed Level ........................................... B-8

Fig. C-I Reactor Power and Control Rod Group 10 Position ........................ C-2

Fig. C-2 Primary Side Pressure .............................................. C-3

Fig. C-3 Pressurizer Level .................................................. C-3

Fig. C4 Loop No. 1: Cold Leg Coolant Temperature .............................. C4

Fig. C-S Loop No. 1: Hot Leg Coolant Temperature .............................. CA

Fig. C-6 Loop No. 2: Cold Leg Coolant Tempature .............................. C-5

Fig. C-7 Loop No. 2: Hot Leg Coolant Temperature .............................. C-5

Fig. C-8 Loop No. 3: Cold Leg Coolant Temperature .............................. C-6

Fig. C-9 Loop No. 3: Hot Leg Coolant Temperature .............................. C-6

Fig. C-10 Loop No. 4: Cold Leg Coolant Temperature ............................. C-7

Fig. C-i I Loop No. 4: Hot Leg Coolant Temperature ............................ C-7

Fig. C-12 Reactor Vessel Pressure Drop ........................................ C-8

Fig. C-13 SG No. I (Primary side) Pressure Drop ................................. C-8

viii
I

Fig. C-14 SGNo. 3 (Primary Side) Pressure Drop ................................ C-9

Fig. C-15 SG No. 4 (Primary Side) Pressure Drop ..................

Fig. C-16 SGNo. 1: Steam Dome Pressure...................

Fig. C-17 SGNo. 2: Steam Dome Pressure .......................

Fig. C-18 SGNo. 3: Steam Dome Pressure .......................

Fig. C-19 SG No. 4: Steam Dome Pressure .......................

Fig. C-20 SG No. 1: Collapsed Level ............................

Fig. C-21 SG No. 2: Collapsed Level ..............................

Fig. C-22 Run Statistics: CPU Time .............................

Fig. C-23 Run Statistics: Advancement Count Number ...............

Fig. C-24 Run Statistics: Time Step ...........................

C-9

............. C-10

............. C-10

............. C-1I

............. 

............. C-12

............. C-12

............. C-13

............. C-13

............. C-14

Fig. C-25 Run statistics: GRIND Time ............................ C-14

ix

I

LIST OF TABLES

Table 2.1 Reactor vessel main parameters ............................................................................... 4

Table 2.2 Reactor vessel volumes and mass ............................................................................. 6

Table 2.3 Main circulation pump characteristics ........................................................................ 8

Table 2.4 Primary loops characteristics ........................ * ........................................................... 9

Table 2.5 Pressurizer main characteristics .............................................................................. 10

Table 2.6 Pressurizer surge line characteristics ............................................................................. 11

Table 2.7 Pressurizer heaters characteristics ................................................................................. 11

Table 2.8 Main SG PGV-1000 parameters (design) at the nominal operation mode ............... 16

Table 2.9 Secondary side volume and heat transfer surface of PGV-1000 ................................ 17

Table 2.10 Uncertainties of measurement ............................................................................... 21

Table 3.1 Plant status prior to transient .................................................................................... 22

Table 3.2 Sequence of events ................................................................................................... 23

Table 4.1 Plant status prior to transient .................................................................................... 28

Table 5.1 Sequence of events in the RELAP5 simulation ...................................................... 31

Table 6.1 Heat transfer coefficient for option 101 and 134 on - - 0.0 s .................................. 33

Table 6.2 Steady-state parameters for option 101 and 134 ..................................................... 34

Table 7.1 RELAP5/MOD3.2.2Beta Steady State Parameters ................................................. 37

Table 7.2 Sequence of events in the RELAP5/MOD3.2.2Beta simulation .... ...................... 38

Table 8.1 Run Statistics .......................................................................................................... 39

xi

L

EXECUTIVE SUMMARY

This report has been prepared as a part of the Agreement on Research Participation and

Technical Exchange under the Code Assessment and Maintenance Program.

On July 1996 at the Unit-I of Kalinin NPP (VVER-1000/V-338) the break of the check valve

occurs in the steam generator No 4 feedwater supply pipeline, that initiated the transient with

sharp decreasing of thefeedwater to the steam generator.

In the present report the data collected by Kalinin NPP Data Acquisition System and In-Vessel

Monitoring System were used to assess RELAPS/MOD3.2 code capabilities to simulate reactor

unit with VVER-type reactor behavior during transient with stop offeedwater supply.

The model has been developed from Kalinin NPP plant drawing and documentation. Principal

characteristics of the model include: reactor vessel, four circulation loops, pressurizer, four

steam generators with steam lines, main steam header, control and trips also were modeled.

A point kinetic option was selected for core neutronic feedback, as considered adequate enough

for this kind of transient. To get the reactivity coefficients BIPR-7 code was applied.

The comparison of calculated and measured data showed, that RELAPS/MOD3.2 code well

describes main parameters in primary and secondary circuits, such as: pressure and pressure

drops, coolant temperatures, collapsed water levels in a pressurizer and steam generators.

Divergence between the calculated and measured data did not exceed limits of measurement

accuracy for the most parameters of the transient.

The sensitivity study was carried out for estimating a heat transfer model in the

RELAPS/MOD3.2 code. For the additional calculation boundary geometry for horizontal tube

bundles (option 134) was applied. The sensitivity study showed that the heat transfer coefficients

at the outer surface of the SG tubes for option 134 approximately is 1.54-2.52 times larger than

for the option 101. A choice between options 101 and 134 in simulation the tube bundles heat

transfer practically does not influence the main parameters behaviour.

RELAPS/MOD3.2.2Beta calculations were performed to estimate differences in simulating

considered transient by two code versions: MOD3.2 and MOD3.2.2Beta.

Analysis of the simulation results for two RELAPS code versions showed that for the same input

deck, the practically identical results with MOD3.2.2Beta and MOD3.2 were obtained.

XIii

I

NOMENCLATURE

AKNP - Neutron Flux Control Systems;

ARM - Automatic Reactor Power Regulator;

BRU-A - Fast Acting Relief Device Dump Steam to the Atmosphere;

BRU-K - Fast Acting Relief Device Dump Steam to the Condenser;

DAS - Data Acquisition System;

ECCS - Emergency Core Cooling System;

EGSR - Turbine Power Electric-Hydraulic Regulator;

KaNPP - Kalinin NPP;

HT - Heat Transfer Coefficient;

MCP - Main Circulation Pump;

MER - Main Feedwater Regulator;

MSH - Main Steam Header;,

MSIV - Main Steam Isolated Valve;

OR SUZ - Emergency Protection System;

PTU - Protection Tubes Unit;

RCS - Reactor Coolant System;

ROM - Reactor Power Limitation Regulator;

PRZ - Pressurizer;

RU - Reactor Unit;

RV - Reactor Vessel;

SG - Steam Generator,

SF - Safety Valve;

SPS - Submerged Perforated Sheet;

SSFR - Stop - Start-up Feedwater Regulator;

FIV - Fast Acting Isolated Valve;

TPN - Turbo-Feedwater Pump;

CL,- Cold Leg of Loop No i;

HL,- Hot Leg of Loop No i;

SG, - Steam Generator of Loop No i.

xv

I

1 INTRODUCTION

Experimental or transient data obtained at operating NPP are base for assessment of computer

codes applied for substation of the power plant operation and reliability of equipment.

One of the most important parameters to be controlled at Russian designed NPP with VVER type

reactors is a water level position in steam generators. When it exceeds the maximum permitted

value, humidity of vapor entering turbine will be increased. If the water level will decrease heat

exchange will be degraded.

In July 1996 at Unit-1 Kalinin NPP occurred the activation of the I' kind emergency protection

caused by decreasing of the steam generator No 4 water level during unit operation with I1 "t fuel

cycle. The feedwater flowrate to the SG sharply decreased caused by the failure of the check

valve in the SG feedwater supply pipeline.

The plant data collected at July 07 1996 by plant Data Acquisition and In-Vessel Monitoring

Systems [1] were used at analyses performed as one of the stages of RELAP5/MOD3.2 code

verification.

The main goals of this analysis are the RELAP5/MOD3.2 code assessment for the heat transfer

removal accidents on the NPP with VVER-1000 reactors caused by stop of feedwater supply.

In the comparative analysis of the calculated and plant data the following parameters are

considered:

Primary circuit parameters:

" Reactor power,

" Primary circuit pressure,

" Reactor vessel inlet/outlet coolant temperature,

" Main circulation pumps head,

" Reactor vessel pressure drop,

" Steam generators pressure drop,

" Pressurizer collapsed water level.

Secondary circuit parameters:

" Steam generators pressure,

* Steam generators collapsed water level,

1
" Feedwater mass flowrate,

" Feedwater temperature.

A brief description of the Kalinin NPP is provided in Chapter 2.

Description of transient is presented in Chapter 3.

An input deck developed to simulate this transient is described in Chapter 4.

Chapter 5 describes RELAP5/MOD3.2 code assessment against transient data on stop of

feedwater sukply to the SG-4 during Kalinin NPP Unit-I operation at nominal conditions.

Sensitivity study for estimating a HT models for horizontal tube bundles is given in Chapter 6.

A brief description of the RELAP5/MOD3.2.2Beta calculation results is provided in Chapter 7.

Chapter 8 shows the run statistics.

Conclusions are presented in Chapter 9.

APPENDIX-A - Base case results.

APPENDIX-B - Sensitivity study results.

APPENDIX-C - Results of RELAP5/MOD3.2.2Beta calculations.

APPENDIX-D - Input deck.

2
I

2 KALININ NPP DESCRIPTION

This section provides a brief description of the power plant and principal systems relevant to

understand the examined transient NPP with VVER-1000 type reactor. The substantial systems

associated with the event are the reactor coolant system, steam and feedwater lines, emergency

protection systems (AZ-1), automatic reactor power regulator (ARM), reactor power limitation

regulator (ROM) and electric-hydraulic regulator of the turbine power (EGSR).

PR

Unit-1 of Kalinin NPP is the Russian design water pressurized reactor VVER-1000 (project V338) rated at 1000 MWe. The general design features of VVER-1000/V-338 are similar to the

standard VVER-1OOO/V-320, excepted of the main circulation loops configuration [2,3].

Each primary loop of project V-338 is equipped with main gate valves on the cold and hot legs.

General view a reactor coolant system of Kalinin NPP is shown in Figure 2.1.

The main VVER-IOOON-338 reactor parameters are listed bellow:

Thermal power - 3000 MW,

Coolant Pressure - 15.7 MPa,

Circulation loops number -4,

Coolant flow through reactor - 84800 md/h,

Coolant temperature Inlet - 289.7 C,

Coolant temperature outlet - 320.0 C.

2.1 Primary side

3
Primary side consists of reactor vessel, four circulation loops, pressurizer and four

hydroaccumulators.

Unlike, standard VVER-1000 (project V-320), hot legs and main circulation pumps are located

approximately at the same elevation, the hot and cold legs have the main gate valves, loop seal is

shorter. The main equipment of reactor unit (RV, MCP, SG, PR) are same type as project V-320.

2.1.1 Reactor Vessel

The reactor vessel is a cylindrical high pressure container where the fuel assemblies and vessel

internal equipment are situated.

There are eight nozzles (DN=850 mm) in two levels (four nozzles at each level) in the reactor

vessel. The nozzles are connected with the four primary circuit's loops.

Each level has two nozzles that are connected with hydroaccumulators of Emergency Core

Cooling System (ECCS).

Main specifications of reactor vessel are shown in the Table 2.1.

Table 2.1 Reactor vessel main parameters

Paraiet& ;K.Value:

1. Length, m 10.88

2. Diameter, external on the flange, mm 4570

3. Diameter, external on the cylindrical part, mm 4535

4. Maximum dimension on the branch pipe section, mm 5280

S. Thickness of the cladding layer, mm 7

6. Reactor vessel weight, t 304

7. Reactor vessel material 15XHM0DA

Volume and mass of the major reactor vessel components are presented in the Table 2.2.

Reactor consist of the following equipment: reactor pressure vessel, internal core barrel and

baffle, protective tube unit, upper block, drives of control rods, trains of neutron measurement,

core etc. Axial cross section of the reactor vessel with the in-vessel components are presented on

Figure 2.2.

4
I

2.21.155

2.20.135

2.17.405

V 16.785

2.16.615

2.25.605

1123963

2.23.745

V 10.433

V.9.718

V.8.688

5
Table 2.2 Reactor vessel volumes and mass

1. Rteactor vessel total volume, m 3 110

2. Upper plenum volume, m3 38.0

3. Downcomer and lower plenum volume, m36.0

4. Core volume, &n 13.7

5. Protective tubes volume, m3 5A3

6. Measurement units volume, n? 2.3

7. Upper head volume, &n 20.0

8. Core heat transfer surface, m2 5130

9. Mass of fuel In the core, kg 80100

10. Mass of cladding In the core, kg 22630

2.1.2 Core

Core of the VVER-1000/V-338 consists of 163 hexagonal fuel assemblies (Figure 2.3). Each of

fuel assembly consists of 312 fuel rods with fuel pellets of uranium dioxide, central tube and 18

guide tubes for absorber of control rods. Fuel pellets have central axial hole. Material of fuel rod

cladding is Zrl O/Nb alloy. Stainless steel grid spacers are located at every 255 mm along the core

height.

Fuel assemblies of the VVER-IOOON-338 differ from that VVER-440. Opposite to VVER-440

fuel assemblies of VVER-1000 have no shroud. VVER-1000 fuel assembly has larger size, more

fuel and control rods of different design. There are 61 assemblies of control rods in the core. Each

assembly includes 18 absorber elements. Absorber material is B4C. Control rod assemblies are

combined into 10 groups one of which is the operational group (group No 10). This group of

control rods is partially immersed into the core during operation.

6
I

Groups

I-II Gr.

I-M Gr.

N-YIGr.

5-YIJGr.

EYI-Ii Gr.

U-Ix Gr.

I-X Gr.

7
2.1.3 Primary loops

Each RCS loop (Figure 2.1) includes a horizontal steam generator, a main circulation pump, hot

and cold legs, two main gate valves. Four primary loops have a common flow path through

reactor vessel, but otherwise they are independent in operation.

Main circulation pump is a vertical one-stage pump with the following main parameters:

Type - 195M;

Capacity - 20000 m3/h;

Head - 6.75± 025 kg/cm2 ;

Suction side pressure - 15.3 MPa;

Primary circuit coolant temperature - 300 C.

Main circulation pump is capable to provide special law of flow decrease at accident with loss of

off-site power. The MCP main characteristics are shown in the Table 2.3.

Table 2.3 Main circulation pump characteristics

- Paramer- VAlue.

1. Power, kW 8000

2. Nominal speed, rpm 1000

3. Loss coefficient of stopped pump, relative to the loop velocity

Positive flow direction 27.0

Reverse flow direction 32.7

4. Nominal torque, Nm

Hot water flow 47500

Cold water flow 64800

5. Internal rotor torque, Nm 73600

The characteristics of main circulation legs are presented in the Table 2.4.

8
Table 2.4 Primary loops characteristics

~ .. eramter Vahift

Hot leg

1. Length from reactor nozzle, m 16.94

2. Inner diameter, mm 850

3. Outer diameter, mm 990

4. Length from reactor nozzle to the main gate valve, m 6.82

5. Length from reactor nozzle to the pressurizer surge line, m 3.81

6. Volume, m3 9.61

Cold leg

1. Length, m 28.72

2. Inner diameter, mm 850

3. Outer diameter, mm 990

4. Length from MCP axis to the main gate valve, m 4.215

5. Volume, n? 16.3

2.1.4 Pressurizer

A pressurizer is connected to the hot leg of the loop No 4 by a surge line. The surge line length is

18 m. Pressurizer spray line is connected to the cold leg of the loop No 1. Spray can be also

performed via make-up pipeline. A set of heaters is installed in pressurizer. The heaters are

intended to keep pressure in case of its decrease. The steam dome of the pressurizer is connected

to bubble condenser by steam dump pipelines. Steam and gas is released via three safety valves

or emergency gas removal system.

The main characteristics of pressurizer are shown in the Tables 2.5+2.7.

9
Table 2.5 Pressurizer main characteristics

1. Total volume, m3 79

2. Nominal water volume, m3 55

3. Total height, m 12.92

4. Inner diameter, mm 3000

5. Outer diameter, mm 3330

6. Dry weight, t 191.5

7. Number of heater blocks 28

8. Power per heater block, kW 90

9. Operation temperature, C 346

10. Design pressure, MPa 17.7

11. Operation pressure, MPa 15.7

12. Number of pressurizer relief valves 3

13. PORV opening/closing pressure, kg/cm2

Control valve 2YP21SO1 185/180

Operational valve 2YP22SO1 1901180

Operational valve 2YP23SO1 190/180

14. PORV opening/closing time, s 1

15. Flow rate through one PORV, t/h 180

10
Table 2.6 Pressurizer surge line characteristics

C fElevation

7 ])spI~emen ~Legt~i~m change,m

1. Hot leg connection nozzle 45' 0.62 -0.74

2. Direct part -450 0.97 -0.69

3. Bend part 456 1.335 -1.21

4. Vertical part -90 1.433 -1.433

5. Bend part (bend radius R - 1.7 in) 90g 2.67 -1.7

6. Horizontal part of 0.3 0.0

7. Bend part (bend radius R = 1.7 m) 90g 2.67 0.0

8. Horizontal part 00 1.325 0.0

9. Bend part (bend radius R = 1.7 m) 90g 2.67 0.0

10. Horizontal part 04 1A62 0.0

11. Bend part (bend radius R = 1.7 mn) 90 2.67 1.7

12. Vertical part to the PRZ nozzle 90g 0.15 0.15

Total 18.275 -3.923

Table 2.7 Pressurizer heaters characteristics

-' Pressu~rer~c 2

:Group M, Noiienclature K ,,FOwmk7 1w O ntc

lDV11VDI 90

DD09 180 158.5 161

1DVI1V16 90

2 DD10 180 157 159.5

DDO1 180

DD02 180

3 DD05 180 155 158

DD06 IS0

DD03 180

DD04 180

4 DD07 180 153 157

DDO8 180

2.2 Secondary Side

11
Kalinin NPP secondary circuit includes feedwater system, steam generators, steam lines, turbine

generator and condenser system.

2.2.1 Steam Generator PGV-1000

Kalinin NPP steam generators are of horizontal type of series PGV-1000.

Steam generator is designed for heat removal from primary coolant and for generation of dry

saturated steam. Steam generator ensures primary circuit cooldown to prescribed temperatures in

all design basis regimes. Construction of primary circuit together with steam generator provides

primary circuit cooldown.

Steam Generator PGV-1000 is a vessel heat exchanger with the horizontal tube bundles

submerged in a water volume and with the separating devices arranged in a steam volume. The

vessel is a horizontal cylinder with elliptical faces having an inner diameter of 4 m and length of

11.8 m (Figures 2.4+-.2.6). The thickness of the vessel wall is 120 mm at the ends, 145 mm at the

central part and 105 mm at the other. The vessel is covered outside with thermal insulation. The

heat exchange area is composed of I1000 U-shaped tubes of diameter 16x1.5 mm. The tubes are

collected in staggered bundles (Figure 2.5). The tube ends are connected to vertical inlet ("hot")

and outlet ("cold") primary collectors. The upper tube row is located at 2190 mm above SG

bottom.

The collectors have an inner diameter D = 834 mm and wall thickness 168 mm in their perforated

zone. The submerged perforated sheet is arranged 250 mm above the top row of tube bundles to

decrease kinetic energy of steam-water mixture and equalize steam loads at evaporation surface.

Feedwater is injected above "hot" side of tubes through distributing nozzles (Figure 2.4).

Separating is of gravitational type with subsequent draining by a louver separator mounted in the

steam dome. The separated liquid is moved down below the mixture level.

12
Feedwater

Distributing

nozzles

Tube

Bundles

Hot

Collector

Feedwater

Collector

Fig. 2.4 PGV-1000: Top View

Cross section for tube bundle of the PGV-1000 is shown in Figure 2.5

L.667

d -16mm

S. . 23 mm

S2 S2 -19 mm -~-~ -e : -~2S'2 22.2 min

II. L 667 rmm-Bundle Wide

S, tFlow

Fig. 2.5 Geometry of tube bundle

13
As follows from PGV-1000 design practice a flow area of the horizontal tube bundle is defined

as:

Fb = FS1 -d

St

Where:

Fb - effective flow area of a tube bundle;

F-total area of the tube bundle, derived from Its width and length.

Form loss coefficient of a tube bundle is defined as:

4b (Z+1),

where:

--form loss coefficient of one tube row;

Z-- number of tubes in the depth of a bundle.

For the central bundle Z = 110, for the side bundle Z = 88; in diverse estimates based on

experimental data 1 varies in a range of 0.15 to 0.40.

Hydraulic diameter of the bundle is 17.4 am.

Heat exchange tubes and most in-vessel structures of SG are made of stainless steel 08X18H1OT.

Collectors and SG vessel are made of steel 10FH2MMA.

Cross section of PGV-1000 in vicinity of "hot" collector is presented in Figure 2.6.

Main design characteristics are presented in Tables 2.8+2.9 and Figure 2.7.

14
Steam Header

II

I

Cold Coliectr Hot CoUecor

Fig. 2.6 PGV-1000: Cross view

15
Table 2.8 Main SG PGV-1000 parameters (design) at the nominal operation mode.

-Paramet~er Vaue

Thermal power, MW 750

Steam pressure, MPa 6.3

Steam capacity, kg/s 408

Averaged steam velocity at evaporation surface, m/s 0.38

Steam humidity at the SG outlet, % _50.2

Water collapsed level (at downcomer part, related to 2.25

the SG bottom), m

Water mixture level (related to the SG bottom), m 2.55

Feedwater temperature, K 493

Primary coolant pressure at thd SG inlet, MPa 15.69

Primary coolant temperature, K:

- inlet to SG 593

- outlet from SG 563

Primary coolant flow rate, m3/s 5.89

Primary coolant velocity in tubes, rn/s 4.2

Pressure difference at SG primary side, MPa 0.15

Total heat exchange area, m2 6115

Specific heat flux, kW/m2:

- average 123

- maximal 227

Average coefficient of heat transmission, kW/(m2 K):

- with account of fouling 5.4

- for clean surface 6

Mean logarithmic temperature difference, K 24.7

Temperature of the SG vessel wall, K 548

16
Table 2.9 Secondary side volume and heat transfer surface of PGV-1000

Elevation,' m Heat transferinsmface,ýzn .Secodaiy Side volumm

0.0 0.00 0.53

0.2 10.23 2.18

0.4 446 5.90

0.6 877 10.76

0.8 1385 15.80

1.0 1673 18.50

1.2 2627 28.00

1.4 3342.5 34.40

1.6 4057.5 42.00

1.8 4772.5 47.80

2.0 5487.5 55.16

2.19 6115 62.80

2.5 - 77.63

2.6 82.50

3.0 100.50

3.5 119.90

4.0 127.00

Fig. 2.7 KaNPP-1 SG water level nomogram

17
2.3 Monitoring, Control and Protection System

Kalinin NPP Control and Monitoring System include the following main controllers:

- ARM - Automatic Reactor Power Regulator;,

- ROM - Reactor Power Limitation Regulator,

- Primary circuit pressure controller;

- PRZ water level controller;,

- SG water level controllers.

ARM, ROM and SG water level controllers are briefly described herein.

Automatic reactor power regulator (ARM-5C) include two regulators:

- Regulator of thermal-hydraulic parameters;

- Fission reactor power regulator.

Influence to the I0"e control rods group ARM provides steady state conditions of the following

parameters:

- Reactor power, measured by AKNP (the mode "H");

- Pressure in the main steam header (the mode "T").

ARM operated together with turbine electric-hydraulic regulator (EGSR).

Influence to the turbine control valve EGSR provides a stable level of the following parameters:

- Turbine-generator capacity (the mode "RM");

- Pressure in the main steam header (the mode "RD ")

Reactor power limitation regulator (ROM-2M) decrease the reactor power to the given set point

in the following cases:

- Stop one of four MCP-to 67% of power current value;

- Stop two opposite MCP - to 50% of power current value;

- Stop two neighboring MCP - to 40% of power current value;

- Stop one of two TPN-to 50% of power current value;

- Stop two of two TPN - to 8% of nominal power,

18
- Closing two of four FIV - to 40% of nominal power.

Power decreasing due to subsequent insertion (one by one) the 10 , 9", 84 etc control rods

groups with operational speed of 20 mm/s.

An algorithm of control rods groups insertion in the core provides the start of the next group

moving, when the previous one gets the position 20% of the whole core height of core bottom.

2.3.1 Steam Generator Feedwater Control System

The SG feedwater control system is intended for maintaining a water level in SG within

permitted range under steady state and transient conditions by means of changing a feedwater

flow rate. Each steam generator has two types of water level control: main (RL71C02, RL72C02,

RL73C02, RL74C02) and stop - start-up (RL71CO4, RL72C04, RL73C04, RL74C04) feedwater

regulators.

Stop - Start-up feedwater regulators (SSFR) should realize SG water level maintaining with

accuracy ±50 mm in stop-start-up modes of the unit, and at the main feedwater regulator

switching off.

In the operating mode SSFR should support the sum of the following signals:

ESF-= a, * Lsp-a 2 * m-a3 * Li,

where:

m - valve RL7IC04 stem position,

Li - SGi water level,

Lsp - set point value of SG water level,

ai - weight factors.

Main feedwater regulator (MFR) should realize SG water level maintaining with accuracy

±50 mm.

In the operating mode MFR should support the sum of the following signals:

EMFR= a, * Lsp- [a2 * Li,-a3 * Gsi + a4 * CGi + as * (dPMsH/dt) + a6* (dOL/dt)],

where:

G1d - SGi steam flow rate,

PMSH - main steam header pressure,

Li - SGi water level,

19
L7- set point value of SG water level,

a6 * (dLI /dt)-is formed with dead zone - ±1%,

ai- weight factors.

2.4 Plant Diagnostic Uncertainty Bands

Measurement of a collapsed water level in SG is measured by a hydrostatic method with use of

static pressure taps, differential manometers and secondary registering instruments. Two types of

level gauges are used: one with a base length, i.e. with a distance between taps is 4000 mm (level

gauges 1, 2) and another with base length 630 mm (level gauges 4, 6, 7, 8). Two level gauges

with a 4000 mm base take a collapsed level relative to the SG vessel bottom. Four level gauges

with a 630 mm base length are staggered near the top row of tube bundles. The one-chamber

transducers measure level on a base of 4000 mm. The measuring device is intended to fix a level

in a plus pulse line and to create the sufficient water volume being able to compensate changes of

water volume in a plus chamber of the differential manometer. Measurement accuracy depends

on that as exactly known average water density in the plus pulse line which is installed separately

from the minus pulse line.

The two-chamber vessels are used in level meters with a base 630 mm. The vessel consists of

chambers of constant and variable level. The constant level chamber is designated to keep water

at temperature that is maximum close to saturation temperature in SG secondary side. For this

purpose it accumulates vapor condensate trapped from SG steam dome. The two-chamber vessels

allow eliminating a temperature deviation; but resulting in delay of measurement due to design

and long pulsing line.

Uncertainties of the major parameters are given in the Table 2.10 [4].

20
Tabe

IBund~e

To Mz~aca

Fig. 2.8 Arrangement of SG level-meter vessels

Table 2.10 Uncertainties of measurement

rararexer-value of uncertainty

Reactor power (thermal), % 2+3

Primary circuit pressure, % ± 1.0

Pressurizer water level, % ±1.5

Secondary side pressure, % ± 1.5

Steam generator water level, % ± 1.0

Coolant temperature, K ± 2.4

21
3 TRANSIENT DESCRIPTION

This description is prepared on the base of the archive data collected by DAS and In-Vessel

Monitoring Systems Kalinin NPP on July 07, 1996 [1].

In this chapter there are given the initial data for plant status prior to the transient changes of the

major thermal-hydraulic parameters during ten minutes after transient beginning.

3.1 Initial Plant State

Prior to the transient reactor unit was operated in the steady state at 97% of nominal power. A

statibnary mode of the RU has been supported by the operations of the two main power

regulators: ARM had operated in the mode "T" (maintaining the reactor power), and EGSR had

operated in the mode "RDI" (maintaining the pressure in the main steam header). The plant

status prior to the transient is shown in Table 3.1.

Table 3.1 Plant status prior to transient

S, Parameter , - - Measured value

Reactor power (thermal/electric), MW 2917/966

Boron acid concentration, g/kg 0.93

Position of the 10" control rods group, % 88

Fuel cycle, effective days 194

Primary circuit pressure (above the core), k/cm 2 160

Reactor vessel pressure drop, kg/m 3.33

Pressurizer levelk m &77

~ L-0 pariuneres.

Primarop~ -C Iru

_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _2 3 4

Main circulation pump pressure drop, kg/cm2 5.8 5.7 5.9 6.0

Coolant temperature at reactor vessel Inlet, C 286.0 286.5 2873 286.3

Coolant temperature at reactor vessel outl C 315.9 313.1 314.4 315.1

Reactor vessel coolant mass flowrate, m&/h 20289 22925 23410 21599

SG pressure drop, kcg/cmi. 1.49 1.54 1.50 1.59

Secon, dary.. Side ____ Loop No _....

1 2 3 4

Feedwater temperature, C 164.1 163.1 163.5 163.9

Feedwater flowrate A/h 1244 1242 1296 1276

SG steam pressuur, kgt/cm 60.1 59.8 60.1 59.8

SG collapsed water level, mm 2224 2206 2273 2297

3.2 Sequence of Events

22
L

The sharp decreasing of the feedwater flowrate to the SG-4 was caused by the failure of the

feedwater pipeline check valve. This moment is assumed to be the start of the transient.

A transient has been defined by the operation of the following regulators: ARM, EGSR, ROM.

After check valve failure a sharp decreasing of the feedwater flowrate to the SG-4 occurred.

Eight seconds later the water level in the SG-4 begins to decrease and at ' = 45 sec, the set point

for MCP-4 switch-off was reached.

ARM stops its management of the reactor power after switching-off MCP-4. ROM was moving

the

l0 control rods group with the working speed 20 mm/s during 8 s (of position 88% to position

83.5% counted from the core bottom). After that an activation of the 1"a kind emergency

protection has happened.

Due to the failure of the interlocking that was not activated after MCP-4 switching-off, the water

level in the SG-4 decreased to 1600 mm and AZ-1 was activated.

Timing of events during the transient is presented in the Table 3.2 [1].

Table 3.2 Sequence of events

%Event

SG-4 feedwater pipelines check valve failure 0.0

Sharp decreasing SG-4 water level 8.00

Main SG-4 feed water regulator Is transmitted to the remote control mode and Is full (100%) 32.00

opened

MCP-4 switching-off due to the signal "A decrease of the water level in the SG-4" 45.00

Activation of the ROM due to the signal "Switch-offMCP-4" 46.00

Activation of the AZ-M due to the signal" The water level In the SG-4 reached 1600 mm" 54.00

Switching-on emergency feedwater pump 68.00

Trip turbine of the Unit-i. W., - 0.0 MW 76.00

Switching-off turbo-feedwater pumps 132.00

Remark: Devices consisted in the protection had shown that SG-4 water level became lower than

1750 mm the 45 seconds beginning of transient. The I's kind emergency protection had been

activated the 54 seconds by the signal "A decrease of the SG-4 water level lower than 1600 mm".

Signal for the AZ-I activation is formed in conformity with principle "2 of 3". A signal about SG

23
water level changing is given by the detectors. located in the different points of the steam

generator. Steam generator water level measured data, using in this report are taken from DAS

archive. DAS data are not used as initial signals for emergency protection system.

The KaNPP Data Acquisition System monitors parameters every 4 seconds. A registration of any

parameters is performed by the DAS only if a parameter's deviation exceeds the established set

point.

4 INPUT MODEL DESCRIPTION

The code used in analyses was RELAP5/MOD312.

The input deck developed for analyses is presented in Appendix D. The features of noding

scheme are described herein.

The general philosophy is a compromise between precision and economy of the resources (CPU

time). For the primary system, a minimum transport time (i.e. ratio of a component length to

coolant velocity) of 0.0334 s was obtained for a steady state regime, when the SG hot collector is

represented by six control volumes. Modeling SG is principally based on common (owner (5] and

international) experience of modeling horizontal steam generators of NPP with VVER-type

reactors. All external solid components were specified in the input model to account for heat

release to the containment.

Kalinin NPP-1 nodalization scheme represents four loops scheme and includes the following

basic components of the primary and secondary circuits:

- reactor vessel,

- four loops,

- PRZ,

- four SGs,

- steam lines,

- main steam header,

- SG safety and relief valves.

The final nodalization scheme (Figures 4.1+4.2) comprises 562 volumes, 701 junctions and 494

heat structures (with 1944 mesh points).

24
The noding schemes of RU basic elements, rendering the greatest influence to the transient are

presented below.

Reactor vessel nodalization scheme is shown in Figure 4.1.

Reactor vessel inlet chamber (inlet nozzles included) is simulated by four identical volumes -

components 5+8. Each of these components is connected to the cold leg of the related loop. All

components are connected by crossflow junctions and will create a closed loop.

The upper points of each volume are connected to the components simulating reactor vessel

inlet/outlet bypass (components - 1 .-4).

The lower points of each volume are connected to the upper points of first sub-volumes of

components simulating downcomer.

Downcomer (components 9+12) are connected in cross direction; they are similar to the RV inlet

volumes. Each element consists of six vertical sub-volumes. The lower point of 67d sub-volume is

connected to the element simulating lower plenum.

Lower part of the reactor vessel (bellow bottom of the baffle) is simulated by the components

9+12. Components 18+25, simulated the part of the lower plenum from the baffle bottom to core

the heated part inlet.

Heated part of the core is divided into four parallel channel (components 26+40), each of which

includes 10 sub-volumes. Components 26+28 simulated 41 fuel assemblies, and components

29+40-40 fuel assemblies each.

Core bypass between core barrel and baffle is represented by component No 34; the control rod

guide tubes and core rim are simulated by the components No 35.01 +35%' 36.

Upper plenum is simulated by the elements 45+64. The segment located above elements 41-44 is

divided on 12 parallel channels. The components 45"-48 simulate the volume inside PTU, the

components 49+52 - the volume between PTU and baffle; and elements 61+64 - simulate the

coolant outlet zone between the baffle and reactor vessel, including outlet nozzles.

Volume of PTU lower plate up to the bottom of the reactor cover is simulated by the component

No 54. The reactor vessel upper head is simulated by an element No 56.

25
The nodalization schemes of two primary circulation loops (loop No 1 and No 4) are shown at the

Figure 4.1. The loops No 2 and No 3 have a similar configuration, apart from pressurizer surge

and spray lines.

The nodalization schemes of the steam generators secondary side and steam lines are shown in

the Figure 4.2.

Heat exchange tubes with the primary coolant inside are distributed into five groups:

- first layer (lower) correspond to 1018 tubes with average length 10.61 m;

- second layer corresponds to 1798 tubes with average length 10.76 m;

- third layer corresponds to 2884 tubes with average length 11.04 m;

- fourth layer corresponds to 2932 tubes with average length 11.25 m;

- fifth layer corresponds to 2368 tubes with average length 11.25 m.

As heat flux significantly changes along the length of tubes due to the coolant temperature

change, the tubes are divided into five nodes in longitudinal direction.

Steam generator secondary side is divided into the following main zones:

- area involving heat exchanges tube (between the elevations 0.0 and 2190 mm);

- layer between the upper tubes and SPS;

- layer of two-phase mixture above SPS;

- steam space above the mixture level;

- gap between vessel walls and SPS rim and between the tube bundles.

Secondary side of the tube bundles was simulated by the stack of five vertical volumes (for SGl

components No 161+165. Feedwater is supplied in the element 165 on the part of the hot

collector.

Area between tube bundles; gaps between SQ vessel wall and tube bundles were simulated by the

components No 171+175 (SG No 1).

SPS is represented by reduced flow area in junctions, that connected the volumes 166 and 168 in

exact accordance to the actual perforation rate. Loss coefficient of holes on SPS is derived from

pressure drop 0.6+1.1 kPa [5],

The steam layer between the upper tube rows and SPS is simulated by the component No 166.

Layer of the two-phase mixture above SPS is simulated by component No 168; its height is

26
L,

chosen so that a nominal position of mixture level corresponds to the elevation height of the

volume center. SG steam dome and corresponding steam pipelines are simulated by the

components No 169+182.

Pressurizer is connected to the hot leg of the loop No 4 (Figure 4.1). Pressurizer is simulated by

the component No 504 and divided in to 10 sub-volumes. In the top of pressurizer are located 3

safety valves. Pressurizer surge line is simulated by element No 504. Pressurizer spray line,

which connected pressurizer steam dome to the cold leg of loop No 3, is simulated by the

component No 349.

For obtaining KaNPP-1 initial steady-state condition some additional controllers were used.

During steady-state calculation pressurizer and steam generator pressure and water levels are

maintained.

Initial conditions were obtained by using RELAP5 steady state option and subsequent nulltransient run of 1000 s duration. The measured and calculated values of the main parameters for

steady state conditions are presented in the Table 4.1.

27
Table 4.1 Plant status prior to transient

- ParameterO KaPP-I ]RIELAP5

1. Reactor power (thermal), MW 2917.0 2917.0

2. Coolant flowrate, kg/s 18471 18471.1

Loop No 1 4253.6 4253.6

Loop No 2 4800A 4800.1

Loop No 3 4892.4 4892.4

Loop No*4 4524.9 4525.0

3. PrImary side Pressure, MPa 15.68 15.674

4. Reactor vessel inlet/outlet pressure drop, kPa 326 328.86

5. Coolant temperature RV inlet/outlet, K

Loop No 1 559/589 559.31589.6

Loop No 2 559/586 559.2/586.4

Loop No 3 560/587 560.3/588.0

Loop No 4 559/588 559.4/588.7

6. Pressurizer water level. mm 8770 8770

7. MCP head, kPa

MCP No 1 568.4 568.48

MCP No 2 558.6 560.45

MCP No 3 578.2 578.58

MCP No 4 588.0 588.09

8. Feedwater temperature, K

SGNo 1 437.3 437.3

SGNo2 436.3 436.3

SGNo3 436.7 436.7

SG No 4 437.1 437.1

9. Feedwater flowrate, kg/s

SGNo 1 345.6 345.6

SG No 2 345.0 345.0

SG No 3 360.0 360.0

SG No 4 354.4 354.4

10. Steam generator pressure, MPa

SGNo 1 5.89 5.883

SGNo2 5.86 5.855

SG No 3 5.89 5.881

SG No 4 5.86 5.856

11. Steam generator water level, mm

SGNo 1 2224 2223

SGNo2 2206 2199

SG No 3 2273 2274

SG No 4 2297 2297

Remark: In the RELAP calculation feedwater flow rate and feedwater temperature were applied

as boundary conditions.

28
L,

0

EUCCCU

a- UE

cf~ 0C

0z00

29
SG SF SG SF

SG No I SG No 4

CA)

CD

Fig. 4.2 VVER-1000N338. Secondary side nodalizatlon scheme
5 RESULTS OF SIMULATION

The transient considered in this report can be referred to a category of incidents caused by the

plant equipment failure. Stop of feedwater supply to the steam generator No 4 of the KaNPP-1

occurred by the failure of the feedwater pipeline check valve. In the given analysis as beginning

of transient (c = 0.0 s) the time of sharp decrease of the feedwater flowrate to the SG-4 was

assumed.

Calculated results and plant-recorded parameters are presented in Appendix-A. The sequence of

events in simulation is presented in Table 5.1 compared to the chronology recorded at the plant

Table 5.1 Sequence of events In the RELAPS simulation

Event .................. .- .......... '.......nle•s

SG-4 feedwater pipelines check valve failure 0.0 0.0

MCP-4 switching-off due to the signal "A decrease of the water level 45.0 47.45

in the SG-4". (SG collapsed level < 1750 mm)

Activation of the ROM due to the signal "Switch-off MCP-4" 46.0 48.47

Activation of the AZ-I (SG collapsed level < 1600 mm) 54.0 56.85

Trip turbine of the Unit-i 76.0 72.03

Reversed loop-4 coolant flow 71.0 73.0

End of Simulation - 600.0

The feedwater pipeline check valve failure leads to a sharp decrease of the feedwater flowrate to

the SG-4 (Figure A-27) and as a consequence, to decrease of SG-4 collapsed water level and

increase of SG-4 pressure (Figures A-23, A-19).

At r = 32 s SG-4 main feedwater controller was transferred to the position "Distance", however it

has not stopped the decrease of water level and at - = 46 s, SG-4 water level became lower than

1750 mm (set point for MCP switching-off).

31
Due to MCP-4 switching-off (r = 46 s, Figure A-11) ROM actuated insertion of the IOh control

rods group with the speed of 20 mm/s (Figure A-i). At r - 56 s SG-4 water level reached the set

point of AZ-1 activation (level < 1600 mnm, Figure A-23). At the moment of the AZ-1 activation

reactor power was - 94.5 % of nominal (Wz 2836 MW, Figure A-i). After SCRAM (AZ-1 full

insertion time - 3.5 s) reactor was shutdown, and at t - 100 s, reactor power became less then 5%

of nominal.

After emergency feedwater pump activation steam generators water level started to be restored

and at r - 10 min after transient start has reached values in the range of 2851+3090 mm

(SGl+SG3) and of 1623 mm in the SG-4 (Figure A-20-÷A-23).

Switch-off of turbine at c - 76 s has caused some increase of. secondary side pressure, however

transition of EGSR to the mode "RDI" kept the secondary side pressure level at

5.77-6.0 MPa (Figures A-16-A-19).

Figures A-4+A-7 show the coolant temperature at the inlet and outlet of the reactor vessel. After

switch-off of MCP-4 the coolant temperature increased (-1+2 K), however, after ROM and AZ-I

activation reactor vessel inlet/outlet coolant temperature was stabilized at the level T- 548/555 K.

Increase of the coolant temperature in the inlet of the loop No 4 (hot leg) at r - 65 - 85 s (Figure

A-7) may be explained as follows:

Decreasing primary side pressure after SCRAM (Figure A-2) lead to release of the water from

pressurizer to the loop No 4 (hot leg, Figure A-3); as result, the coolant temperature rised

(Figure A-7).

At c - 73 s the reverse of the coolant flow rate in the loop No 4 occurred. Hot water of PRZ

began to penetrate into the RV outlet nozzle.

Comparing the calculated results of the main parameters of the primary and secondary circuits

with plant data, good agreement is found. The deviation of the calculated and measured data did

not exceed the limits of the measurement channel accuracy at KaNPP (Table 2.16).

Finally, analysis of the transient proved that the RELAP5/MOD3.2 code describes satisfactorily

the thermal hydraulic processes in both primary and secondary side of the NPP with VVER-1000

reactor.

32
L

6 SENSITIVITY STUDY

The objectives of additional runs were to estimate differences in simulating heat transfer by two

code options: default option 101 for pipes and option 134 for horizontal tube bundles.

In base case, outer boundary of the SG tubes was specified with the option 101. In additional runs

the RELAP5 option 134 was set. The results of two calculations are summarized in Tables 6.1

and 6.2 and also shown in Figures B-I÷B-14.

Table 6.1 shows heat transfer coefficients at steady state for heat structures related to the SG-4

heat exchange tubes. As seen, heat transfer coefficient at outer surfaces of SG tubes in the base

case (option 101) in 1.54+2.52 times less than in the additional run (with option 134). Difference

is larger for lower layers of tubes.

Table 6.1 Heat transfer coefficient for option 101 and 134 onr - 0.0 s

SG-4 0ptio*1l OptionI34.

Heat Structures BliK(M lWmK M

Layer 1 17011 67A8 42898 69.86

Layer 2 18274 119.73 40654 121.78

Layer 3 19323 189.73 29758 186.09

Layer 4 19233 190.96 34362 194.95

Layer 5 17941 161.27 33727 162.05

Table 6.2 shows the key parameters of the

models.

reactor unit at steady state for two heat transfer

33
Table 6.2 Steady-state parameters for option 101 and 134

ameter:... .. .. " ,, Opti Option134,

1. Coolant flowrate, kg/s 18471.1 18415.8

Loop No 1 4253.6 4257.3

Loop No 2 4800.1 4800.9

4892.4 4832.6

Loop No 3 4525.0 4525.0

Loop No 4

2. Primary side pressure, MPa 15.674 15.678

3. Reactor vessel Inlet/outlet pressure drop, kPa 328.86 326.83

4. Coolant temperature RV inlet/outlet, K

Loop No 1 559.29/589.57 558.68/587.3

559.24/586.44 556.63/584.21

Loop No 2 560.25/587.96 557.52/585.57

Loop No 3 559.41/588.69 556.72/588.28

Loop No 4

5. Pressurizer water level, mm 8770.3 8728.2

6. MCP head, kPa

MCP No 1 568.48 564.58 MC~2560.45 556.54

MCP No 2 578.58 574.50

MCP No 3 588.09 584.03

MCP No 4

7. SG pressure drop, kPa SG No 1 145.93 145.07 SGNo 152.83 151.32 SGNo2 146.97 146.02

SG No 3 155.80 154.80

SG No 4

8. Steam generator pressure, MPa

SG No 1 5.89 5.89

SGNo2 5.90 5.89

SG No3 5.87 5.86

SG No 4

9. Steam generator water level, mm

SG No 1 2225 2151

SGNo2 2199 2154 SG No 3 2274 2206

SG No3 2297 2206

SQGNo 4__ _ _ __ _ _ _

34
V

The steady state of the examined regime, calculated with the RELAP5 option for horizontal tubes

bundle showed rising heat flux to the SG secondary side, decrease of the coolant temperature in

the primary circuit by -2 K and increasing steam generation by 0.8 %. As result, the SG water

collapsed levels decrease by - 4+.9 cm.

Figures B-1÷B-8 illustrate the behavior of the heat transfer coefficients at the outer surfaces of

SG-I and SG-4 tube bundles in the transient. As seen, the ratio of the heat transfer coefficients

for the option 101 and 134 remains practically invariant for the lower part of the tubes bundle

(layers 1+4) during transient. The heat transfer coefficients for both models are practically the

same for the part of the tubes bundle which is not covered by water (layer 5, T > 50 s).

Figures B-9-B-10 show the behavior of the primary side pressure, PRZ water level and loops

coolant temperatures. Some discrepancies of the primary side parameters at the beginning of the

transient (t <250÷300 s), may be explained by increase of the SG tube bundles heat transfer

coefficients (Figures B-I÷B-8).

For the last stage of the transient (T > 300 s) coolant temperatures for the option 101 and 134 are

practically identical, but primary side pressure and PRZ collapsed level for the option 134 are

greater than for the option 101 (1%, 4% respectively, Figures B-1 l+B-12).

The steam generators water level is shown in Figures B-13÷B-14. As seen, the choice of option

134 gives some overestimation of SG collapsed level at the last stage of transient

The sensitivity studies show that in spite of using two different heat transfer models (option 101

and option 134) for the for horizontal tube bundles, the main parameters (primary and secondary

pressure, coolant temperature, PRZ and SG collapsed levels etc.) remain within the uncertainty

limits of the plant data.

35
7 RESULTS OF RELAP5/MOD3.2.2BETA CALCULATIONS

This section provides a brief description of the calculation results by two RELAP5 code versions:

MOD3.2.2Beta and MOD3.2.

The input deck and run procedures for the MOD3.2.2Beta calculations are the same as for

MOD3.2.

For obtained KaNPP-1 initial conditions, null-transient run of 1000 s duration and subsequent run

with using RELAP5 steady state option were performed. The results of steady state calculations

for both code versions are presented in the Table 7.1. As seen, the steady state parameters

obtained by two code versions are practically identical. Maximum deviation of the parameters for

the both codes does not exceed -0.4 % for primary side parameters and -0.9 % for secondary

side parameters.

RELAP5/MOD3.2.2Beta calculation results of the transient are presented in Appendix-C. The

sequence of events in simulation is presented in Table 7.2 compared to the MOD3.2 version and

to the chronology recorded at the plant.

Comparing the RELAPS/MOD3.2.2Beta calculated results with MOD3.2 results and plantrecorded data, good agreement is found. Some oscillations of the SG-2 steam dome pressure and

loop No 2 cold leg coolant temperature (Figure C-6, C-17) could be referred to a different

numerical treatment of the pressure controller model (EGSR mode "RDI" simulation) by the

version MOD3.2.2Beta.

Finally, analysis of the transient proved that the MOD3.2 and MOD3.2.2Beta versions of

RELAP5 code describe satisfactorily the thermal hydraulic processes in both primary and

secondary side of the NPP with VVER- 1000 reactor.

36
Table 7.1 RELAP5/MOD3.2.2Beta Steady State Parameters

.aamte ..MMOD3=

Primary Side

1. Coolant flowrate, kg/s 18471 18471.1 18471.1

Core - 17886.3 17890.5

Loop No 1 4253.6 4253.6 4253.6

Loop No 2 4800A 4800.1 4800.1

Loop No 3 4892.4 4892A 4892.4

Loop No 4 4524.9 4525.0 4525.0

2. Pressure, MPa 15.68 15.674 15.676

3. Coolant temperature RV inlet/outlet, K

Loop No 1 559/589 559.290/589.567 559.2191589.501

Loop No 2 559/586 559.235/586.443 559.8181586.577

Loop No 3 560587 560.2501587.955 560.178/587.902

Loop No 4 559/588 559A12/588.636 559.3061588.504

4. Pressurizer water level, mm 8770 8770.38 8761.98

5. MCP head, kPa

MCP No 1 568.4 568.486 569.061

MCP No 2 558.6 560.450 561.626

MCP No 3 578.2 578.575 579.385

MCP No 4 588.0 588.088 588.789

6. Reactor vessel pressure drop, kPa 326 328.863 329.242

7. Steam generator pressure drop, kPa

SG No 1 146.06 145.557 146.142

SG No 2 152.52 152.830 153.324

SG No 3 147.00 146.973 147.217

SG No 4 155.82 155.802 155.953

Secondary Side

8. Steam generator pressure, MWa

SG No 1 5.89 5.894 5.896

SG No 2 5.86 5.871 5.926

SG No 3 5.89 5.898 5.892

SG No 4 5.86 5.866 5.867

9. Steam generator water level, mm

SG No 1 2224 2224.61 2223.91

SG No 2 2206 2199.80 2206.00

SG No 3 2273 2273.89 2273.01

SG No 4 2297 2297.09 2297.22

37
Table 7.2 Sequence of events in the RELAP5/MOD3.2.2Beta simulation

KaNP MOD3.2Beta:.

SG-4 feedwater pipelines check valve failure 0.0 0.0 0.0

MCP-4 switching-off due to the signal "A decrease of the 45.0 47.45 46.13

water level In the SG-4".

(SG collapsed level < 1750 mm)

Activation of the ROM due to the signal 46.0 48.47 47.157

"Switch-off MCP-4"

Activation of the AZ-1 54.0 56.815 57.057

(SG collapsed level < 1600 mm)

Reversed loop-4 coolant flow 71.0 73.03 74.0

PRZ Heaters On

Group No 1 (W = 270 kW) - 60.106 59.728

Group No 2 (W = 270 kW) - 60.507 60.100

- 61.031 60.575

Group No 3 (W = 720 kW)

- 61.580 61.250

Group No 4 (W = 1260 kW)

Trip turbine of the Unit-1 76.0 72.03 75.057

End of Simulation - 600.00 600.0

38
8 RUN STATISTICS

Calculations carried out on Workstation HP-9000 Model 715/100

The computation model used in a base case was done with 562 volumes, 701 junctions and 494

heat structures (with 1944 mesh points). Among there are 11 time-dependent volumes, 5 timedependent junctions. 55 control variables are used.

Plots of computer statistics for a transient run are given in Figures A-28-A-3 1; C-22÷25. The

requested time step (AT = 0.025 s) was chosen below material Courant limit (AT = 0.035 s) and

was not affected by the RELAP5/MOD3.2 code (Figure A-30). MOD3.2.2Beta version was made

some first iterations with a small time step (AT -10.9 s, Figure C-24). The CPU time versus

problem time was approximately 1:19.3 for MOD3.2 and 1:19.7 for MOD3.2.2Beta as seen in

Figures A-28; C-22.

Run statistics information for both code versions are summarized in the Table 8.1.

Table 8.1 Run Statistics

. .rameter - , . Code.Version

MOD3.2 MOD3.2.2Beta

Problem Time, s

Steady-State 1018.68 1022A

Transient 600.0 600.0

Number of Hydrodynamic Volumes 562 562

Advancement Count Number

Steady-State 40934 41218

Transient 24000 24168

CPU Time, s

Steady-State 19803.27 19939.8

Transient 11606.6 11848.0

Grind Time', s

Steady-State s.60S 104 8.608104

Transient 8.605 104 8.723 104

')The code efficiency factor ("Grind Time") as stated in [6] is obtained from: T = CPU/(C*AT),

where: C- total number of volumes; AT- advanced count number; CPU -CPU time.

39
9 CONCLUSION

The codes RELAP5/MOD3.2 and RELAP5/MOD3.2.2Beta were assessed using plant data" Stop

of feedwater supply to the steam generator No 4 at KaNPP Unit-i". A base case was calculated

with a RELAP5/MOD312 default heat transfer model for pipe (option 101). The additional run

was done with a model of heat transfer for horizontal tube bundles (option 134). The calculations

with the RELAP5/MOD3.2.2Beta were done to estimate the differences between two code

versions. The calculation results for both code versions were compared against plant data to

identify code capabilities. The following conclusion can be drawn:

1. The thermal-hydraulic parameters of the primary circuit (pressure, pressure drops,

coolant temperature, pressurizer water level) and of secondary side (steam generators

pressure and water level) are well predicted by the two RELAP5 code versions.

2. Divergence of the calculated and measured data does not exceed the range of KaNPP

measurement channels accuracy.

3. The sensitivity study shows that a choice between option 101 and 134 of the heat

transfer model in simulation of SG tubes practically does not influence the behavior of

the considered parameters.

40
L,

REFERENCES

1. Description of the Transient "Activation of the 1' Kind Emergency Protection Caused

by Decreasing of the Steam Generator No 4 Water Level During Unit Operation with

11-6 Fuel Load ". Technical Information about Kalinin NPP Unit 1&2 Transients.

Nuclear Power Ministry of RF Concern "ROSENERGOATOM", Kalinin NPP,

Udomly, 1997.

2. 0. Prasolov, A. Achtjamov, Technologic Handbook, PTO, Kalinin NPP, Udomly,1992.

3. VVER-1000, Primary Circuit Scheme, CRDI NVV NPP, No 01.PU.YA.

4. L. Bogachek, "Accuracy of the main measurement channels Kalinin NPP", E-mail of

28.06.98.

5. S. Pylev, V. Roginskaja, "Assessment of RELAP5/MOD3.2 on Experimental Data of

Void Fraction and Velocity Distributions in Secondary Side of Steam Generator PGV1000". Report No 90-12/1-97, NSI RRC KI, Moscow, Russia, 1997.

6. Protocol for performing CAMP Development Assessment, Rev. 8/10/95, page 6.

41

i,L

APPENDIX-A

BASE CASE RESULTS

i

3000

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

250LO

k-Z

2000O

15001- -

10001

57

7

II

-4 - - - -P- -

MZ=uarn Enor7 ,

L - -- * 1.

* I

t

I I

0 20 40 60 6o 100 120 140 160 10 201

Time, s

4i 100

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

- f -- - -. - - - ,

I -- P_ pý

W

Vol

, 9 

60

20 L

- ~I -

- ~I -

T

--- I-

-- I-

-4-- -I-- - 4

I I

Ii

.11- - -

III I

-- 4--

I I

I I

I I

r -r - -i

I I

Al,

-0 1 . . . . I , [ . . , . I . . . . I . . . . I

0 10 20 so 40 so

Time, s

60 70 80 so

Fig. A- 1 Reactor Power and Control Rod Group 10 Position

A-1
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

IxI.I_ _I - -F~ - --- - - - I - - - - -

•' I II

14.01 .1.__

_ _ _ _ _ I I" _ I

iI I I II

x 0 so 100 150 200 250 300 350 400 450 500 550 60

Time, s

Fig. A- 2 Primary Side Pressure

Kailnin NPP-1: Stop Feed Water Suply to SG No 4

3 7.S1f

I i I

.~ * i i I I I I i

0 5o 100 15 200 M 3 4o 40 W 5 I• 

Time, s

Fig. A- 3 Pressurizer Collapsed Level

A-2
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

-I "- CPe•ap

590L - - - - - - - - -

------------. -- * - PD2 Il

•Y i I I I I

i,. I i I I i Ii

& .•. _ I_ II, - ., , _, _- , _ I_,,, ' . _ I _ _r ,

I I I ] ; I I

0 50 100 150 200 25 500 550 400 450 500 550 6oC

Time, s

Fig. A- 4 Loop No 1: Coolant Temperature

6 600 Kalinin - NPP-1: I Stop Feed Water Suply to SG No 4

Iq] I __ [] __ aReap i

- - --- .. - - - - - -Dai -

$- - - -- -- .- -ljp- --- I . , MeasurcamtFrroriK x

_ - -, -

__' I _ I I _ 

-f ;I 1 j I I III

• i . . . I . . .• . . I . . . . .I.... _ I _ _ I

.4:' . .. . ., ... , ,

0 50 100 150 200 2505 005 S 400 45500 S M0

Time, s

Fig. A- 5 Loop No 2: Coolant Temperature

A-3
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

600 .I I cLi lap

590 I I I,,i.D &:mp

Mesurear~ v rrorzx 1 I

I I T

Ii. . . .I, , . .t . . I ... .. i . . . . .! I . . .. . .. .

, 350 400

* Time, s

Fig. A- 6 Loop No 3: Coolant Temperature

9 Kalinin NPP-1: Stop Feed Water Suply to SG No 4

1 °°• - I I I I- ,,-- _,. ,-- -- _ eiaJ•pz

6. 1- - -- -- -I- -- -- - - - - --

I I f I

j, --------- _ --- _=-_--'-- •-'-'-,- -- =.Z

0 50 100 150 200 250 300 350 400 450 500 550

Time, s

Fig. A- 7 Loop No 4: Coolant Temperature

A-4
L

Kalinln NPP-1: Stop Feed Water Suply to SG No 4

I I

-!O~• - - - - - -_ - - . -" - - -

o - - I i ;

-- 0 -, --- -

uoL

•]Ii I I

44Q.

0 100 200 3oo 400 50o 0

Time, s

Fig. A- 8 MCP No 1 Head

6 Kalinln NPP-1: Stop Feed Water Suply to SG No 4

" I

i bi p

-d III i

6001 ,

46o.2._ _ I_ _I I --I ,

0 45 i I I I

I T8Q I ----------- - ---

440!e

0 100 200 300 400 5006

Time, s

Fig.A- 9MCP No 2Head

A-5
600 Kalinin NPP-1: Stop Feed Water Suply to SG No 4

580 I 4 - Ia 

----------- - - -- -

,2L, - - -- - -I

44q- * Q..~ . _. I I

* I I II

_ . !- - --

! I .... !

0 100 200 300 400 500

Time, s

Fig. A- 10 MCP No 3 Head

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

500 IRZ AIEP

4, 00

30 ee

Ft I

-I- S200! _ _ __ __

100 I

a -i I I . .

0110 t 0 "100 200 30 400 500 6

i Time, s

Fig. A- 11 MCP No 4 Head

A-6
Kalnin NPP-1: Stop Feed Water Suply to SG No 4

I I Ada

--- - - I\Mea - ---- mremet E:rror 1 9. '

sOOKj I I

s .I I ; I

2601q__ _ _

"240L - - I

& 'r I

4i I

220.! . I i

no _ Av -- - - -----

0 10 20 40 50 ; C

Time, s

Fig. A- 12 Reactor Vessel Pressure Drop

A Kalnin NPP-1: Stop Feed Water Suply to SG No 4

ý1 180 _ _____________

'- - 4 -- I -- Iem 175 7Measrcrgt Error i j'R N

170

160.] _

- - - - - - - - - - - - -

I I

1 -- - - - - - - - -

i I I 0

e ao l I I I I

.1•01.. . , , .I

0 .100 200 30 400 500 6

Time, $

Fig. A- 13 SG No 1 (Primary Side) Pressure Drop

A-7
4-

Kalinin

190

170J_ _

-ii

1601 -

- I"

150-

1401

NPP-1: Stop Feed Water Suply to SG No 4

I _ _ _I . .srr t r elap J

I - -- ------ - --

"I .I -.

I I- I

I, I I

- - - - . -. -.. -I . . . .

- - - Z -i

I I

I I

I

I

0 100 200 300 400 500 60

Time, s

Fig. A- 14 SG No 3 (Primary Side) Pressure Drop

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

- I- - - - I-

-I~

Reap

ý-Mze 4 7-. pP D,!)

tu

a...

Co

a.-

I-, I I I

- I I I

31 _ _ I_ I I

I" I

. . . I '

Ut I . I

-30 ' I_ _ ] I I

-" I I ! I

*1L I • I . . I

0 100 200 300 400 50060 t

Time, s

Fig. A- 15 SG No 4 (Primary Side) Pressure Drop

A-8
0~

I654

5.90_

-I

£75 __

&701

Fn NPP-1: Stop, Feed Water Suply to SG No 4

------------ --- -, MArmt gError

7 7

II -f vi Ii

'I I

I

0 

200 800 400 I 

I

0 100 200

Time, s

So0 601

Fig. A- 16 SG No 1: Steam Dome Pressure

Kalinin NPP-1: Stop Feed Water Suply to SG No 4 6.15

I"I

I II 6.10iZ --- "

4.

-j I I - _ _ I _ _ 1I

£-1 _ - ---- -- -- -- --- --------

~ £02 -------------------------------I I

I I I I--

£9 JI i I

• I." I

o0 .100 n00 500 400 500

Time, S

Fig. A- 17 SG No 2: Steam Dome Pressure

A-9
5 Kalinin NPP-1: Stop Feed Water Suply to SG No 4

L- - -- - -

- - - - - - - --- er --•--rrri -

S--

la5.00- - -..-

&7V.

0 100 200 300 400 500 60ý

Time, s

Fig. A- 18 SG No 3: Steam Dome Pressure

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

- - - ---- 0-------

9. I MeI rJ n~nIu

-I I I

--- - - ---

I I

£7 .. I i I I _ _ _ _

SI I I I

................ !..... ! , g

O100 200 30 400 0

Time, s

Fig. A- 19 SG No 4: Steam Dome Pressure

A-1O
L

& Kalinin NPP-1: Stop Feed Water Suply to SG No 4

10 - - -Mesrnnrou,

2.6 -I~- -" 

-i_-- - - - - -!

3 I

3 A.2 -- - -- -. . ..-

2-2, ---

- - - -

-

0 100 200 300 400 500 60X

Time, s

Fig. A- 20 SG No 1: Collapsed Level

Q

S.

S.

0

Kailnin NPP-1: Stop Feed Water Suply to SG No 4

I 

I

- - 4- - - I- - - - - - - - - -

III

II

- -"-- - - - ---

|i

1.9

0 .100 200 Sa0

Time, s

4 . . 5.0. 

604

Fig. A- 21 SG No 2: Collapsed Level

A-11
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

- - - - - - - --- -.-.-

.-- - - - --- -- -------------- - - -

~I I

1J+i . . i 3 40i ,, +

0 100 200w 3W 40 S&

Time, s

Fig. A- 22 SG No 3: Collapsed Level

Kalnin NPP-1: Stop Feed Water Suply to SG No 4

1 I 2-I M r I

i •t"I I LI

I _ _ _ ,I_ I•• . . .I. . I

. JO 'I, I ' '

F --- "--- - - -

4 I I I I

-.. I I I --------------------------------------- - --

1.4i 1 . ..

0 .100 200 300 400 500 60m

Time, s

Fig. A- 23 SG No 4: Collapsed Level

A-12
I

s__Kalinin 0 NPP-1: Stop Feed Water Suply to SG No 4

400 :

I. ,

4|I I I = = = 100

0 100 20 300 4oo 500 601

tTime, s

Fig. A- 24 SG No 1: Feed Water Flow Rate

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

400 6 

-c I Ri ap

I I"I

- -- -- - -- -4- - - N-P- -

300+- -------------------------

I II

I . I

- I - . - .- -a " - -

----- ----- -- w •

0 .1fO0 200 s0 400 Soo 600 .Time, s

Fig. A- 25 SG No 2: Feed Water Flow Rate

A-13
!

,NI. Kalinin NPP-1: Stop Feed Water Suply to SG No 4

500

4O00

- - - - elap

Mnsuumntzro

40-- -- -- I--

~300

~ I

a

~200

4

2

I I

I I

_ _ I _ -I

I I I

I i I

I i I

I I

100_

A

0

0 100 200 3T0

Time, s

400 500 601

Fig. A- 26 SG No 3: Feed Water Flow Rate

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

a

'U

400

I ~ I

I

300

I I

3 -0 - -- -- t- - - -- - l-- --- 

20I I

-I I

1001

I.

-J

MeaszLntEror, ~

- - -I

A A I l L . . • .

. 100 200 300 • 4,0,0, ,0,

Time, s

60M

Fig. A- 27 SG No 4: Feed Water Flow Rate

A-14
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

ICL - - - I

I I

.

o0-

0 100 200 00 400 s0 60C

Time, s

Fig. A- 28 Run Statistics: CPU Time

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

~25AW0

j i I I

Iooo I-I - . . I 

I II

,0, 0L -J- -- - - I-- --- -I-. . . .

II

0 -. -- 200 - Soo 40 Soo 6M

Time, s

Fig. A- 29 Run Statistics: Advancement Count Number

A-15
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

I i

- I I I I

SI I.'

1~0.0260

1

I I I

ii i

0.0255

0 100 200 300 400 00

Time, s

Fig. A- 30 Run Statistics: Time Step

a . Kalinin NPP-1: Stop Feed Water Suply to SG No 4

0.0017-5 -- I------ -- --------------- -- -- -- ---

I I

01 I

0 0

i:o.omio I

II I I

*II

oIooI

* I Io I

I I I

0 • 100 200 300 400 500 S5

Time, s

Fig. A- 31 Run Statistics: GRIND Time

A-16
APPENDIX-B

SENSITIVITY STUDY RESULTS

B-1
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

-I Ii i

q--- --1 -- - - - - - - - - ------- - - - I

, -_ _ _ L _. . . i . . . i

T_.C ..•- - -- --- - -i. i .

011 tz .4 . I} "Io, . I . _

0 100 200 300 400 500 60M

rime, S

Fig. B- 1 SG No 1: Tube Bundles (Layer 5) Heat Transfer Coefficient

4 Kalinin NPP-1: Stop Feed Water Suply to SG No 4

30-

•• I i • , IMod. 10•

- - -- - - - - - - -- - Mode- 34_

-- I I

4 -5 -- - - - - - - - - - I

I '

dI

,I Il

°7 -- -- - - - I . . . . I

_ti ,.,. , --------. f I - - -,,-_

0 1 2 3 300 4. I. S. .

Time, s

Fig. B- 2 SG No 1: Tube Bundles (Layer 4) Heat Transfer Coefficient

B-2
II...

VS

Kalinin NPP-1: Stop Feed Water Suply to SG No 4 4 0

35 -•1-4--- Mode)34

I

25ý 1

0- I

20-I - - _ li- -- , I 

-J

- -

-4-

0 100 200 300 400 S. 60C

Time, s

Fig. B- 3 SG No 1: Tube Bundles (Layer 3) Heat Transfer Coefficient

to

to

I-.

to

VS

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

45

- l 1--4 I - e 134

25I L

_0

T-- 5 44--- -- - --- - -~ - - -_ -_ - - -

.44.

-J

I LV _ I "o -. o I

20 I , I I'

I

0

I I ., , I I

100 200 00o

Time, s

: . I . . I . . . I

400 Sw 6%

Fig. B- 4 SG No 1: Tube Bundles (Layer 1) Heat Transfer Coefficient

B-3
a Kalinin NPP-1: Stop Feed Water Suply to SG No 4

Mafde 10

35L.,1 I [--4-- MAb 134

30tI

I '

s- I-- - -- - - -

120 0; IL

I, 0 100 200 300 400 500 601

ITime7, 8

Fig. B- 5 SG No 4: Tube Bundles (Layer 5) Heat Transfer Coefficient

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

40 I

i! •'I I

,30 ' I

-. --- -,- - - -

~ 1-- -

°• -I • . ' I ' • , , I I' . . .

LR ------- --------------- -- --------

- - -I - - - - - - -

0 .100 200 300 400 500 60O , • Time, s

Fig. B- 6 SG No 4: Tube Bundles (Layer 4) Heat Transfer Coefficient

BA
0Kalinin 4Spl NPP-1: Stop Feed Water Suply to ttoSG No 4

25-

IbI

I I

- - -

I' I

10

0 100 200 300 400 s M

Time, s

Fig. B- 7 SG No 4: Tube Bundles (layer 3) Heat Transfer Coefficient

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

t

2:-X

10I L,_0

k 01--~--- --

0 .100 200 Sao 4O0 •0 60€

Time, s

Fig. B- 8 SG No 4: Tube Bundles (Layer 1) Heat Transfer Coefficient

B-5
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

1 & O5 i I I , . __ . _ ..

-- - - - "- - - " -- -- -

I i -I

15.54!~ I _ I Ti e I I

Mg B- 9I Pia Presur I I 

"1 I I II . " i

S Ii I I ' I I A

Time, s

Fig. ]B- 9 Primary Side Pressure

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

M - - - - -I - - - - -od 13-4

.0 " I I I I I I I I I

-" - - - - - ---- -.- - -- - -, -•

I_ I I I I

! _ 10 I 200I 20 M I I 4- SW -0

IT I i I I I IS

t I I I I I I

8 J j]_ __ .. _ ' . I I _ _ I I I , _

1 gx I . . . I-I- - -

e 50 - 00 150 Time,5 300 350 400 450 500 550 601

i

Fig. B- 10 Pressurizer Level

B-6
Kalinin NPP.I: Stop Feed -I - Water - - -Suply to SG No 4 -- - -, -I - -I

CL Mode 101)

IZ _Mode 1O4'-' -& Modc 134j

,- - - -L- - '-- -i-d-1-4- - I

LTIIA I . _ 141 1 I ' 5 M 60I

L.

i . . . I . . .t . . I . . . . . " , +i . . . . .I . . .I.. . + . .

0 50 100 150 200 250 300 350 400 450 500

Fig. B- 11 Loop No, 1: Coolant Temperature

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

S610

- I 1I I I ! I• _ _ _ _ "_

60 - - - - - --- --- --- I- -_.+-- __

" I I I I I• .M -

54001 ;• I I I I- ,

_ II t Ii II

101

L134

II

0 -- I-•L -- I-- ------------ -------- ---- -- -----------

• l iI I I I

I IIII I I

54 0 4 I I I I

0 50 1 01 •0 200 250 S00 0400 45 5005 5 60C

Time, s

Fig. B- 12 Loop No 4: Coolant Temperature

B-7
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

i-g- - -- -- - - - -oel

I II

IILI

. I

I I

0 100 200 300 400 5o0 601

Time, s

Fig. B- 13 SG No 1: Collapsed Level

A Kalinin NPP-1: Stop Feed Water Suply to SG No 4

, , -- •2_ , fModolO

2- - - - -...---- -= - -- ----- e 

£Tim s

F B- 1 Sl

•--

•, -rime, S

Fig. B-. 14 SG No2_olpe ee

B-8
APPENDIX-C

RELAP5/MOD3.2.2Beta RESULTS

C-1
tI

L

i.

a 300WU Kalinin NPP-1: Stop Feed Water Suply to SG No 4

1

*-...... NPP Dae r,

II I 2500

T

~200k L

ISM

S1000 L

500 L

ho 01

I

_I

I I I I

I I I _ I

I I I I

I I

I I _ _

I I I

I I I

I I I _ I

I I I I

I I

I _ _

I I

-- I

I • m m •

I-_

I 0 20 40

; ' ý • . I . . I , I , : . I

60 80 1W0 120 140 160 180 20(

Time, s

100

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

-- I--,--------------

V22B' I

a

a

a

a

2.~

I

80

60-'

1 9 -I1

~ 4-

L

Al

-- I-

- I -

-- 4 -- , NPPDaraj

L~1

I I

I I

I I

I I

-i

I . , I . . . . . . . . . . . . . . . . . . . . . . I i . . . . . . . .

0 10 20 30 40 50

Time, s

70 80 90 10i

Fig. C- 1 Reactor Power and Control Rod Group 10 Position

C-2
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

I i ----- -- Mode 3.2.2B

1 I I

15.5 I I I I I _ _ _

~ 

141 ,1 _ _ ,_ _ ,__,_ _

14 .0

i 3 .:, .. .. . . .I. L . ... I..L .. , , ' ... I . . . .... I .,

0 50 100 150 200 250 So0 350 400 450 So0 s5 5 01

Time, s

Fig. C- 2 Primary Side Pressure

Kalinin NPP-1: Stop Feed Water Suply to SG No 4 S 9.0 _ _

I II I I I ,II . i ' AMode3.2

i I.0 

I I

I I I i I

- -

-. . . . . . I .. .. .1. .. .. ., .... ..

0 5o .100 15 200 25 300 SSO 400 45 5o0 SM60

Time, s

Fig. C- 3 Pressurizer Level

C-3
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

5M4

I I t I I Iv 3dC3.2

I I I I I. * I

I I I I I III I

_ I_ I I

0 M 100 10 200 20 300 350 400 450 500 55 60;

Time, s

Fig. C- 4 Loop No 1: Cold Leg Coolant Temperature

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

' i II I I _ I _ _ _ _ _ _ _

580._ I .3d 

3.0

SI I I I I..e.... Mde..B

Ir . I . I I I

58. so I I I II ,II

I I~ I "I ! I I I I

I. I i i I I I

:1 0 5 .100 150 200 2SO 300 350 400 45 500 550 M0

4Time, s

Fig. C- 5 Loop No 1: Hot Leg Coolant Temperature

C-4
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

II I• I i____._____.,_]

i i . I .. I - i- -I -- - I- -- -- . --I. . - -l-

•'! 4I" , i I I ___

5eI I I i I

I i I iJ i iI I I I

•. .4-------------- ----- i--- -- i . .!--

I l,, I I I I I j'- - i --i- "- - "- - "- -- - -- - - - - - -- !- -;, -I-

|j I I I I I* I I I

55 I

5441 I I I I

... ! , , .., . , ! ., .I. , ... ...I ... ..... .... ..... i

0 50 100 150 200 250 $00 350 400 450 0 S 50 60C

Time, s

Fig. C- 6 Loop No 2: Cold Leg Coolant Temperature

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

5600

5501" TI I I I I

590 1 I I _ _.p_ p _ II

T - I I I -- I I _ ;4 I i I I I T

_ j . -I ., _ _ _ . _ _ _ _ _

-I ! I i i I I I I I I

50 .150 150 Doo 2580 SO 50 4M0 40 s500 Ms l

Time, s

Fig. C- 7 Loop No 2: Hot Leg Coolant Temperature

C-5
Aa Kalinin NPP-1: Stop Feed Water Suply to SG No 4

5604- - 55I I I -I I -- ------- _ -_-_-_ - -

I I

_ _ IS I I Ii

II I I II 1 , 

4 J ~ ]~ iI I I I iI I

SI I iI i I

0 50 100 150 200 2503 00 350 400 4505 0 50 M

Time, s

Fig. C- 8 Loop No 3: Cold Leg Coolant Temperature

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

6 0 I I . . . . . . .

Mode 32

590 I I a

_i _ I_ I I I ' 2i~ ,,r

I I I I t

_ I _ _ I I I I i i I

I II II I

OjI _ _ i I I

g , I I i ! i I I I I I

0 .00 5 • 00 5•300 350 400 450 500 550 0

50 .10 150Time, s

Fig. C- 9 Loop No 3: Hot Leg Coolant Temperature

C-6
Kalinin NPP-1: Stop Feed Water Suply to SG No 4 i3.

II l

--------- -- - - ---- ---- - - - -- ---

541

. I II

. . .. I"I

I I I I

I. III

ii I II

! iI I

0 50 100 150 200 250 30 350 400 450 s5o 550

Time, s

Fig. C- 10 Loop No 4: Cold Leg Coolant Temperature

KalininNPP-1: Stop Feed Water Suply to SG No 4

610

I i i I I _ _ __-_ -• -- _ - M d

I I M•e 3 2

I I I

i I I I i ! ii 9I 

I I I E

I£ 5O._ _L• I- - - -I- -I--- I-- --I ..-- - - - - ---- --

i I !

)f

0 50 .10015020M3 0 W.

Time, s

Fig. C- 11 Loop No 4: Hot Leg Coolant Temperature

C-7
Kalinin NPP-I: Stop Feed Water Suply to SG No 4

320 - - -__r --.-.... •ppL,

3 I

2001

IIi I

2404.... I

0 100 2ýo 300 4ý0o 500 o

Time, s

Fig. C- 12 Reactor Vessel Pressure Drop

CKalinin NPP-1: Stop Feed Water Suply to SG No 4

185

10 - - --- I I - -, -- - d- 3-2 -

T - - ------- ----- - P-DI I

Is_

' I 

1401 I I

)

o .100 200 300

Time, s

400

50 : I .

Fig. C- 13 SG No 1 (Primary Side) Pressure Drop

C-8
L

U.

aII~

a.

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

190

1 I _ _ _ Mode 3.2,Z 18--5L-- - - - - - -ae22

-F4 -

160 _

I I

0 100 2w

! I I I I I . I I I I . I

Soo 400 Sw 601

Time, s

Fig. C- 14 SG No 3 (Primary Side) Pressure Drop

x Kalinin NPP-1: Stop Feed Water Suply to SG No 4

a.

I2.

180

T1601 _- - --

1 I I

140 _ - -

2 -- I -- I

SI

d___

220-- I

.I I

.40 - _ I I I

Mode 3.2 ' I

- -- Mode 3.2.2B I

I ---

-_I

.0100 200 SO0 400 S0o 60(

Time, s

Fig. C- 15 SG No 4 (Primary Side) Pressure Drop

C-9
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

Moda 32

S a- - - - - - - --- 3 B

I I

- I

j-----------------------I

0 100 200 30 400 Soo

Time, s

Fig. C- 16 SG No 1: Steam Dome Pressure

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

£15_

I I i ~ PP D a ta .05 I - -

- --- - - ' -. -. . . -. -. .

• --- - ' -. -. . . -. -. .

IMi I

•1_ _I__ I -- , _ ,

0 100 200 300 400 0

Time, s

Fig. C- 17 SG No 2: Steam Dome Pressure

C-10
. Kallnin NPP-1: Stop Feed Water Suply to SG No 4

&.10 --I i - - - - - - - - - - - - -

6. I

6.5 .j' I_ _

IFI

II _ I_ I_ _ _ I

&0.ý

0 100 200 S00 40 50 6&

Time, s

Fig. C- 18 SG No 3: Steam Dome Pressure

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

-- - - - - - - - - I I i ,di •.2

I I I I I

I I

I I I

- I, I _ _ _

0 .0 2-0 Sao 4o 500

Time, s

Fig. C- 19 SG No 4: Steam Dome Pressure

C-11
Kalinin NPP-1: Stop Feed Water Suply to SG No 4

Modb 3-22B . i I

I"I I I+

. .. P±4m - - -- - -

0'• , , Time, s

FIg. C- 20 SG No 1: Collapsed level Kainin NPP-1: Stop Feed Water Suply to SQ No 4

"I I+ I

I i K .. I I

.-_ _ L _ -.- _ I__ , _ ,_ _ , . . . , _

2 - I I I I 

1e i i I

1 1 I -9 I

0 100 20 0 50M

Time, s

Fig. C- 21 SG No 2: Collapsed level

C-12
12.000

Kalinin NPP-1: Stop Feed Water Suply to SG No 4

I.

I'

- -j

W~e 3.2B

-It

0,OW - -

I - - -

'• PJ . . . . I . .. . ..

0

I I . . . . I . I I I I ,

100 200 3oo

Time, s

40 . . . . 5

Fig. C- 22 Run Statistics: CPU Time

Kalinin NPP-1: Stop Feed Water Suply to SG No 4 • 25,00

E) M - 2

-I -I I- 

'SAW00{- - -e-- -~e1.2 - I

Si I I I ,. r i

,T m I I

0.. .1 200 30040 50

Fig. C- 23 Run Statistics: Advancement Count Number

C-13
I

0.030

0.02S

I.-.

0.02_

0.01o

0.m0

0.00

Kallnin NPP-I: Stop Feed Water Suply to SG No 4

-4 '

rII

I I

I : I I

-i I I

IC e 100 24 0 300

TIme. s

400 5w 6A

Fig. C- 24 Run Statistics: Time Step

l-I Kalinin NPP-1: Stop Feed Water Suply to SG No 4

[

Mode3.2

Mode 3~2~2 2~ I

-I -

I I

I i I I

I I I

I _ _ _ _ _

- - -I

i

I- - - - IT

- - -I

0 .100

. . 1,

200 3Xe

Time, S

400 500 . M. 

Fig. C- 25 Run Statistics: GRIND Time

C-14
APPENDIX-D

STEADY STATE INPUT DECK

D-1
,WWERIOOOI0 eanP Unk I. Stop ofFeedwear Supply to MG.

4.

" This •pt deck prepar by S. Py•v " (NSI RRC XI. Moscow. Russia)

" oa the bes ofthe archived dam couetrd by Kalinin NPP

" Data Aqauisbion and la-Vsasel Mouitoring Systens an

07.07.96

* Iwoa Moda Inclue: 0 4 -prximaryooM•

0 4- Steamnenecrasoa * 4 -Steam LiMn

0 Reacmor Vesase

' InlkVWUaIaNozicsDC, LP AdUP aespalittdon4

Dea-aip of •te Tratsiem

* Activasio offth I-an "a Emergecncy Protechion

* caused by Decrease of the SO No 4 Water Level

* during WOi NPp.l Operation with I 1-tb Feal LmIniniial dam for a Reactor Steady stra mofde

* T'ehazllReactor Power .2917MW

* Loopl: - 0.245632

* Loop2-0.246615

SLoop3: -05606

* Lp4- 0.251698

LO 1.0000

Company D•ration - 194 cf. days

SBoron Concutatims .0.939 a/kg

*Posattom (o axe bottom)

of 10.h OR SUZ woulp -133%

SPrimay Sidte

* Press= above Core 15.6S MP&

• Loop Coolant Flow Rae:

" Loop No I - 4253.S9 kt/s

* LoopNo2 - 400.43kg1: " Loop No 3 - 4392.43 kgh/

" L.opNo4 4524.M951•S

* Reactor inletioutls Pressue Drop. 326.34 kP&

• SO (Piutay side) Pressure Drop:

•SON N - 146.&2kP•

S No2 - 152.92kPA

* SONo3 . 147.0kPa

S SNoo4- 155.82kra

" MCP proanae DoP:

• LoopNol - M&4 kPa

" LoopNo2 - 5 6 kPa

" LoopNo3 - 5752kPa

" LoopNo4 -.5SLOV

* Reactor letCoolant Tempieraue:

L oopNoI - 559.15K

*Loop No 2- 359.65 X

SLoopNo3 - S451X

SLoop N4 - 59.45

* Remor Outil Coolant Tempe'raom

L.opNol -599.05 K

* LoopNo 2 - 3"2 .

" LoopNo3 - 587..55X

" LoopNo4 - U.S25K

" Pre'uriz.rLevel 8.77 i.

*Secondary Sid,~.

" SNol-437.,5K

" SGN2*42-436.25M

" SONoo3 - 436.65K

" 4.- 437.05

* Pcedwater flowrave: SSO No I - 345.6 kas S0 No 2 - 345.0Okg/

" SONo.3 - 360.0ki/s

SSONo4- 354.4 kgf

" Fcdwater Presure a the SO nlet:

" SONoN - 7.056MPh " SONo2 - 7.0S6 M1s

" SONo.3 - 7.056 UP&

" SONo4 - 7.056MPa

* Stamooencrator Prasate:

SGNol -5.89MP&

* SONo2 - 5.86 MP

SNo 3 - 5.3914a

SO No4 - 5.86MP

" StCim Geta-Co Want LewVe

" SONoI - 2.224 t

• SO No2- 2.2D6m

* SONo3-2.273m

* SONo4 - 2297m • Tra•sienDenriptiom

" t- Oe. - StarafTranaaen

" t - ac - Beginning of the dtcruaa offth 50-4 water level

"t -45 wce - MCPA Swatdai-off by thesignal

St-46 an - Activation offt ROMW due to swisth- off MCP4

" twS4 se - Activaion ofth AZ-i

• t - 69c - Swihc of•he FWP pump

"t=76 s - Atrip nft Uni I Truine-gecracr

t -241 an - SwicoffshsTPN No I&2

Scrduo pr.Pe prxot-ip

100 War osomn

1. Elevat€ionecds

•cdno voL.o. dev fluid mme

121 I1010002 26.9 h2o•Pi•ary

122 182010002 35.9 h2. Second

*IL TVnA step Cads

Crdn• Vot. mI-n2 070& sa/ko man0 r ID 100

201500.0 L.-9M.5-2 00003 2000020000 20000

202 1000.0 1IA 2.5 -2 00003 20000 20000 20000

0,

BL Trips

* 3.1 AuxliawyTrips

• dnoo var code rd v3r code mcon Li tineof

401time 0p cul 0 -1.10.0

402 done 0 nl 0 -1.1 -1.0

3.2 Accident Trips

* 3.2.1 Stop Feedwaerzsuppty

crdno, var ~ode rdt va code cn Litiziaof

403 time 0 Itull 0.-1.1.-1.0

3.. True Befre Accident

trdn trip rel trip Li Ijineof

601 -403 and -403 n0.0

* 32.2 Accident

*crdnoouip rel trip Li timeof

602 403 and 403 a-l.0

33 Stem LineeTrips

* 3.3.1 BRU-A

*crdoo var code rd var code coonst toinof

404 p 169010000 p aull 07.15+6 n -1.0 S* 1BRU-A

Ope

405 p 169010000kl null 06.2746 a .1.0 *SGt BRJJ-A

Close

406 p 269010000go ull 07.16 a -1.0 S2BRU-A

Open

407 p 269010000k etull 06.27463a -1.0 SG2 BR-A

Clowt

408 p 369010000 pcmll 0 7.15+6 n 4l0OSW3BRU-A

Open

409 p369010000k mnll 06.27+6 s -1.0 *S03 B A

410 p 4690100001 V ull 0 7.54 -1.0 S04 BRU-A

Close

crdnotip fllp et Lt UsoL

603 602and 4N4-1.0 *5SO BRU-AOpm

6'04602;d 405o-1.0 *5431 BIU-AClose

60M 602 and 406 om-1.0 * SG2 Bill-A Open

1606 60ad 407 o -1.0 * SO2 BRLLACloe

607 602aasd 408a-1.0 SG3 BRU-AOpen

608 6M and 409-.1.0 0SG3 BRU-AClose

609 602and 410 o-1.0 S04 BRJ-A Open

610 602 nd 411n-1.0 So4 BRU-AClose

* 3.3.2%GZ

. MIV Closed with 10-12 se delay aft SCRAM

*crdno vr code rL var code cons MLi tunof

501 time, 0 timed 617 10.01 -1.0 * Loop 140 1: v4187

502 time 0 Ztt aaeotdi7 10.01 -. 0 *OLoop No 2. vhv02

503 tim oat e617 10.01 -1.0 * Loop N 3: vMV

504 time 0 St timf617 18.01 -1.00 Loop No 4: vi4

*3.3.3 Presatw Regulatora

L PMWae Set Point

cdnovar code rdevar codeconat Li

413 pl16 90100 D ) null 05.88+6 a SO0 RV#ISS Cose

414 p 16910000 p mull 05.9046 n 'SGI RVI#IISOpen

415 p269010000 It mull 05.85+6 542 iRV#295 Close

416 p 26 9

010 000 p null 05.87+6 "SM 2 tV#M8SOpen

417 p369010000k macll 05.8846 n 'SOS XV0385 Cloft

418 p369010000 null 05.9046 a S03RV#385 Open

419 p469010000 It mall 05.8546 a SG4RV#4S Clone

420 p469010000 pe mul 0 5.8746 a S04 4RVN4 Open

* b. Steady Scm Presnse Coomnoiu

ordoe nrip rdtripo Li tiansof 701 601 audJ4IJ$1-.0 eS•! iV#I8SIo ae 702 601 and414a-l.0 *'SGI RV#1,5opse

703 601 and414a.1.0 *SOI RV185 Open 73601 aUd4171-1.O SG2 RVOM3CIMl 704 601 and 41 1..0 S021VM25 Opts

705 601 and417a.-.0 * SO) RV383 Close

706601 and41$n-l.0 *SG3 iV#385 Open

1707 601 andd419n.1.0 "SO4iV#415 Clofe

708 601 and420n-l.0 *SG4RVO45Open

.OEGSR Mode"RDI"

erdoo tri ret trip Li tmotof

711 403 and413a-1.0 'SGI RV#189Close

712 403 and 414 .1.0 'SGI RV#1890pen

713 403 and415o.1.0 SO•2 V#29Close

714 403 ,nd 416 a -l.0 0S02 i•ViOpen

715 403 and417a-1.0 0,3 RV389 Ciose

716 403 and4la-1.0 *S03 RV#3SPOpn

717 403 and4t92-l.0 *SO4RV94$9Clos

718 403 aad420a-1.0 ",S04RV#4IOpen

* 3.MCP Tris

"doodovarcoderd vat code coca LiUtimof

421 time O k nall 0 -1. 1 -1.0*MCPAI sepoun

422tdie 0t null 0 -1. 1 -1.0 *MCPiset point

423tim 0It mull 0 -1. 1 .1.0 0MCP•s3 point

424cinrfvar476 le cull 0 1.75 a .I.0MCP14sespoiu

*c+dno trip rl trip "Li timnof

612 602 and 4211 -1.0 -MCPI(141) switb off

613 602 ad 4221-1.0 MCPa2(241) ewitchoff

614 602 and 4231.1.0 MCP#3(341) switchoff

615 602 and 4241-..0 *MCP#(441) switchoff

* 3-5SCRAM

*tlno var code rt var code consM Liteof

425time 0 getheof615 1.01*-.0ROMsopoint

426 enrhw 476k InullO 1.6na-.0 AZ-I sepoint

*04d0.nip rel trip Li timeof

616 602 4251 -1.0 *ROMIwitchon

617 615 d4261 -1.0 'AZ-I switchon

03.6 Preassurizer Icaters

ctdeo var code rel var code o-- U timeof

427 cantvar$04h aull 0 4.2 1-.0*aHam uswitch off

'Al beates5 switch off- Level too low

adoo trip tel trip Li titnof

618 403 and 427 I -1.0

"PRZlIZHea CioupNo I (Wa270kW)

crdno var code rel var code con Li- tiofe 

428 p054010000k cull 0 15.5446 o -1.00On

429 p054010 00

0 moull 0 15.79.6 a -1.0 Off

"alno, rnp rel trip Li timeof

619 618or 429.a -1.0

620 428 or 621 -1.0

621 620 and.-618n -1.0 roup I SwitchOn

I PRZ Hm Group No 2 (W 270kW)

*ad" o var code rel var code coca Li timf

430 p054010000le nu 0 15.39+6 a -1.0 On

431 p0540100009, mull 0 15.6446 a -3.0* Off

=troo trip ret trip Li titiaof

622 618 cr431 n -1.0

623 430cr624 a3-1.0 624623 and .- 618 o -1.0 * Goup2SwitchOn

" PRZ Him op No 3 (W - 720 kW)

c"dnoo vat code ret vu code on Liumof

432 p054010000le mull 0 15.2046 a -l.0*On

433 pOS4010000 V mal 0 15.49*6n -1.0*Off

crdo trip rel tp U timeof

625 618or 433a -1.0

626 432cr 627 a -1.0

627 626 and-61a -.1.0 4 Group3 SwitchOn

$ PIZ Hasteero GewNo 4 (W - 260kWM

*crdo var code eel va code conan Li tmoof

434 p0$4010000k male 0 15.01+6 a -1.0*On

433 p054010000ge null 0 15.396 n -I.0*Off

adootcip rel trip Li tinteo

628 618or 435n -1.0

629 434 r 630a -1.0

M3 629 and -6180a -U. O roup 4Switch On

" IV. Steady State Adjustment coanpountn

* 4.1 NIC Comrollrs•

* ) opfl: MC•N141

"Controlvariable 140 " L•opill Mas fow set point

I2O140000lqsp conusant 4253.59

"Ccal -variable 141

*MCPWI controller

20514100rpm-141 pumpel 1.0 101.743 0 3 100.0 500.0

20514101 catv 140 nflowj 143000 10.0 10. 2.

b) h Loop#2: MCM#241

"Corl variable 240

Loop2 Mass flow stn pose

20524000 G2sp constant 4800.43

* Comot variable 241

" MCP# controlle 20524100 rpo.24! paapatl 1.0 101377 0 3 00.0500.0

20524101 cntvar 240 nAowj 243000000 10.0 10. 2.

I c) Loop#3: MCP#341

*Controil variable 340

*Loop#3 Mass flow set point

20534000 03sp consta 4M9.43

* Control variable 343

MCPS3 contriler

D-2
20534100 pm-341 •ujtcil 1.0 102.392 0 3 100.0500.0

20534101 cetrvar 340 maloi 343000=0 10.0 10. 2.

d 6) Loop#4: MC#441

*Control variable 440 * Loop4 Manss flow = point

20544000 04sp e•oom 4524.95

" Conl variable 441

" M(84 cotolkr

20544100 rpoa-441 pooanlt 1.0 102.7020 3 100.0500.0

205"44101 aortvar 440 mfowj 44300000 10.0 10. 2.

* 4.2 Pr Controlletr

* 4.2.1 PRZ Pressure Controlles

"Control variable 500

* PI2 Presmr Set Point

2055000 P2Z-P eo= 15.63+6

S42.2 P,2 Level Controllm

"Control variable 503

SPRZ Level Set Point

20550100 PRZ-L coasts 8.77

*etrivar N 509

" PRZ.-IvelDevistion

2055M00 prz-er sum 1.0 .-. 991723.4 0 3-10.0 30.0

2050901 0.0

20550902 1.0 n-tvar 501

2055093 -I.0 msrlvar5

* 4.3 Foedwaermooler

4.3.1 Level Set Point

"Coen•ol variable 160

* Sl Water Level set point

20516000 SGI.Lsp costnan 2.224

* Control vriablk 260

" S02 Water Level in poi

20526000 SG2-L.p wosnt 2.206

" Camol variable 360

* S03 Water Level snt point

20536000 SG3-Lsp comac 2.273

*Contro variable 460

*S03 Wae Level set point 20546000 S04-Lap cons 2.297

'4.3.2 Function SG Level v1 . WSaWe Vohna

20216100 suac-t

, Level lRe H = 0.0-0.96 

m

202161010.330 0.00

20216102 0.547 0.01

20216103 0.571 0M

20216104 0.603 0.03

20216105 0.642 0.04

202161060.6990.05

20216107 0.742 0.06

20216108 0.803 0.07

20216109 0.271 0.00

20216110 0.945 0.09

20216131 1.0260.10

202161121.1140.11

20216113 1208 0.12

2021611413090.13

20216115 IAI$ 0.14

20216116 1.52 04.15

202161171.6470.16

20216118 1.7720.17

20216119 .9020.18

20216120 2.038 0.19

202161212.180 0.20

20216122 2.327 0.21

20216123 2.479 0.22

20216124 2.637 0.23

20216125 2.799 0.24

202161262.9660.25

20216127 3.1370.26

20216128 3313 07

20216129 3.492 0.2

20216130 3.676029

20216131 3.8630.30

20216132 4.054 0.31

20216133 4.24j

20216134 4.416 0.33

20216135 4.646 0.34

20216136 4.849 0.35

202161375.OSS 0.36

20216138 .263 0.37

20216139 5.473 0.38

20216140 5.636 0.39

20216141 5.900 0.40

20216142 6.116 0.41

20216143 6334 0.42

20216144 6.54 0.43

20216145 6.776 0.44

20216146 7.0O0 0.45

20216147 7.227 0.46

20216148 7.456 0.47

20216149 7.69 0.48

202161507.9240.49

2021615118.163 0.50

202161528.4040.51

20216153 8.650 02

202161548.8990M3

202161559.1520.54

20216156 9.409 035

20216157 9.670 0.56

20216158 9.936 0.57

20216159 10.2060.58

20216160 10.4800.59

20216161 10.7600.60

20216162 11.0440.61

20216163 31.3330.62

20216164 11.6240.63

20216165 113.9160.64

20216166 12.208 0.65

20216167 12.5000.66

2021613 12.7890.67

20216169 13.075 0.68

20216170 13.3560.69

20216171 13.6320.70

20216172 13.9000.71

20216173 14.1600.72

20216174 14.4110.73

20216175 14.6531 0.74

20216176 14.8790.75

20216177 15.0940.76

20216178 S.29 0.77

20216179 15.481 0.78

20216180 15.6490.79

20216181 5.81000.80

20216182 15.9320.81

20216133 16.048 0.2

202161•4 16.151 0.83

20216185 16.2420.84

20216186 163260.85

20216117 16.4040.86

20216188 16.4800.87

20216189 16.356 0.88

20216190 16.635 0.89

20216191 1•.20 0.90

20216192 16.8140.91

20216193 16.9190.92

20216194 37.03 0.93

20216195 17.1740.94

20216396 373290.95

20216197 17.508 0.96

20216139 17080001 0.0

20216199 127.0000.0

20236200 O 

4

* L.evelange H 0.96 

- 1.9 

m 20216201 0.000 0.0

20216202 17.pft 0.0

20216203 I750 I003 0.96

20216204 17.7110.97

20216205 17.9420.98

2=21626 38..2040.99

20216207 38.$O 1.00

2021620M I38.8 1.01

20216209 19.195 1.02

20216210 19390 1.03

20216211 20.0121.04

20216212 20.458 1.05

20216213 20.925 1.06

20216214 21A10 1.07

20216215 21.9111 .08

20216216 2•.423 1.09

20216217 22.945 1.10

20216218 23.4731.11

20216219 24.004 1.12

20216220 24.535 1.13

20216221 25.063 .14

20216222 25365 1.15

20216223 26.098 3.16

20216224 26.599 1.17

2021622 27.085 1.18

20216226 27.353 1.19

221622728.000 1.20

2021622 28.424 1.21

20216229 28.825 1.22

20216230•29.206 .23

20216231 2936 1.24

20216232 29.914 .25

20216233 30246 1.26

20216234 30.564 1.27

20216235 30.72 1.28

20216236 31.1701.29

20216237 31.462 1.30

20638 31.748 1.31

20216239 32.031 132

20216240 323121.33

20216241 32.594 1.34

20216242 32.878!.35

20216243 33.167 1.36

20216244 33.4611.37

20216245 33.764 1.38

20216246 34.076 1.39

20216247 34.400 1.40

20216248 34.7371.41

20216249 35.087 1.42

20216250 35.447 1.43

20216251 35.811.44

202162S2 36.196 1.45

20216253 36.582 1.46

20216254 36.974 1.47

20216255 37.370 1.48

20216256 37.769 1.49

20216257 38.170 1.50

20262=58 38.572 .51

20216259 38.973 I.52

20216260 39.373 3.53

20216261 39.76U 3.54

20216262 40.159 1.55

20216263 40.545 3.56

20216264 40.9231.57

20216265 41.292 1.58

20216266 41.652 1.59

20216267 42.0001.60

20216268 42.336 1.61

20216269 42.661 1.62

20216270 42.9761.63

20216271 43.281 1.64

20216272 43579 1.65

20216273 43.369 1.66

20216274 44.153 167

20216275 44.433 1.66

20216276 44.708 1369

20216277 44.9811.70

20216278 45353 3.71

20216279 45.523 13.72

20216280 45.795 1.73

20216281 46.0681.74

20216282 46.343 1.75

20216283 46.623 1.76

20216284 46.907 1.77

20216285 47.1971.78

20216286 47.495 1.79

20216287 47.800 1.80

20216280 48.114 1.83

20216269 48.437 3.82

20216290 48.769 1.83

20216291 49.108 1.84

20216292 49.454 1.35

20216293 49.807 .36

20216294 50.166 1.87

20216295 50.5301.86

20216296 50.900 .89

20216297 51.274 1.90

20216298 51.2740001 0.00

20216299 127.000 0.00

20216300 nmao4

I Level Fajge H = 1.9.2.84 

m

20216301 0.000 0.0

20216302 51.2740.0

20216303 $1.2740001 M.90

20216304 51.6531 .91

20216305 52.035 1.92

20216306 52.420 1.93

20216307 52.808 1.94

20216308 53.1971.95

20216309 53.3891.96

20216310 53.9911.97

20216311 54.3741.96

20216312 54.7671.99

20216313 55.160 2.00

20216314 553.522.01

20216315 55.943 2.02

20216316 56.334 203

20216317 56.7242.04

20216318 •7.1152.05

20216319 $7.3072.06

20216320 $7.9002.07

20216321 58.2932.08

20216322 S3.69 2.09

20216323 59.0962.10

20216324 59.4962.11

20216325 59.88 2.12

20216326 60.2932.13

20216327 60.7012.14

20216328 61.1122.15

20216329 6328 2.16

20216330 61.9472.17

20216331 62.3712.18

20216332 62.8002.19

20216333 633342.20

20216334 63.6722.21

20216335 64.1162.22

20216336 6435632.23

20216337 65.0162.24

20216338 65.4722.25

20216339 65.932 2.26

20216340 66.3962.27

20216341 66.863 2.28

20216342 67.3342.29

D-3
20216343 67.8072.30

20216344 684,,2.31

20216345 68.7632.32

20216346 692452.33

20216347 69.7292.34

2021634 70.2162-35

20216349 70.7042.36

20216350 71.1942.37

20216351 71.6152.38

20216352 72.1782.39

20216353 72.6722.40

202163$4 73.1672.41

20216355 73.6622.42

20216356 74.1592.43

202163$7 74.65 2.44

20216338 7S.1522.45

20216359 75.6482.46

20216360 76.1452.47

20216361 76.6402.48

20216362 77.1362.49

20216363 77.630 2.50

20216364 78.123 231

20216365 78.616 2.52

20216366 79.1062.53

20216367 79.5962.54

20216368 80.084 2.55

20216369 80.5712.56

20216370 81.0562-57

20216371 81.5392.58

20216372 82.021 29

20216373 82.5002.60

20216374 8..9772.61

20216375 83.453 2.62

20216376 83.9262.63

20216377 84.398 264

20216378 84.868 265

20216379 85.336 266

20216380 85.8022.67

20216381 86.2662.68

20216382 86.7292.69

20216383 87.1982.70

.20216334 87.6502.71

20216385 81.1082.72

20216386 85 62.73

20216387 89.0202.74

20216388 89.4742.75

20216389 89.9262.76

20216390 903772.77

20216391 90.$27 178

20216392 91.2762.79

20216393 91.7232.80

20216394 92.1702.81

20216395 92.6152.82

20216396 93.059 .83

20216397 93.303 284

20216398 93.5030001 0.00

20216399 127.000 0.00

20216400 reao4

0 Level Rampn 2.41- .40 

m

20216401 0.0000.0

20216402 93.503 0.0

20216403 93.5030001 2.84

20216404 93.945 2.85

20216405 94.3862.86

20216406 94.827 2.87

20216407 95.2672.88

2021640895.706 2.9

20216409 96.144 2.90

20216410 96.382 2.91

20216411 97.0192.92

20216412 97.45652.93

20216413 97.8922.94

20216414 98.328 2.95

20216415 98.763 2.96

20216416 99.1972.97

20216417 99.632 2.98

20216418 100.0662.99

20216419 100.500 3.00

20216420 100.934 3.01

20216421 101.3673.02

20216422 101.800 3.03

20216423 102.233 3.04

20216424 102.665 3.05

20216425 103.096 3.06

20216426 1033263.07

20216427 103.956 3.08

20216428 104.3, 3.09

20216429104.8123.10

20216430 10238 3.11

20216431 105.663 3.12

20216432 106.087 3.13

20216433 106.5093.14

20216434 106.930 3.15

20216435 107.3493.16

20216436 107.7663.17

20216437 108.181 3.18

2021643810.5995 3.19

20216439 109.006 3.20

20216440 109.415 3.21

20216441 109.822 3.22

20216442 10.227 3.23

20216443 110.6293.24

20216444 111.028 3.25

2021644S 111.425 3.26

20216446 111.8193.27

20216447 112.211 3.28

20216448 112.399 329

20216449 112.94 3.30

20216450 113.366331

20216451 113.745 3.32

20216452 114.1213.33

20216453 114.493 3.34

20216454 114.862 335

20216455 115.227 3.36

2021646115.588U3.37

20216457 115.94 3.38

20216458 116.299 339

20216459 116.648 3.40

20216460 116.994 3.41

20216461117.335 3.42

20216462 117.672 3.43

20216463 118.0043.44

20216464 118332 3.45

2021646118.655 3.46

20216466 118.974 3.47

20216467 119.2873.48

20216468 119.596 3.49

20216469 119.900 3.50

20216470 127.000 4.00

oV. Control Vuiables

* .1 Presurier Level

* zzuivar N 504

P* P- level

205400 pcz-levsum 1.0 8.771 30.011.62

20550401 0.0

20550402 0.900 voidf 50010000

205403 1.200 voidf $04020000

20550404 1.227 vo 50403000

20550405 1.227 voidf 504040

20550406 1227 void 504050000

20550407 1.227 voidf 504060000

20550408 1.227 void! 5470000

20550409 1227 voidf 54080000

20550410 1.200 voidf 504090000

20550411 0.900 voidf 504100000

5* .2 Steam Generemr Level

* 5.2.1So Level

Cannot variable 170

* SGI Water Vohnxm

20517000 SGI.W szm 1.0 66.7276 

1

20517001 0.0 3.0voidf 161010000

20517002 3.99 voidf 171010000

20517003 S.94 voidf 162010000

205170044.1 void! 172010000

2051700 8.97 voidf 163010000

205170066.38 voidf 173010000

20517007 9A voidf 164010000

20S17006 23 voidf 174010000

205170093.75 voidf 17•010000

205170109.93 voidf 165010000

205170113.18 voidf 175010000

20517012 4.72 voidf 179010000

20517013 10.71 void! 166010000

20517014 1.0 voidf 176010000

20517015 28.353voidf 167010000

20517016 10.09 voidf 168010000

20517017 10.21 voidf 169010000

20517018 0.072 voidf 177010000

* Control variable 171

* S0l Water Level (tane of 0.0- 0.96)

20ý17100 0GI-LI Inctieon 1.0 0.01

20517101 coutvar 170 161

* Cotml variable 172

* SOl WaterLevel (Rap of0.96 

- 1.9)

20517200 SGI-L2 litnaio 1.0 0.01

20517201 ctlvar 170 162

Control variable 173

* Sol WeterLevelM (Ra of 1.9-2.84)

20517300S01.43 finiuion 1.0 2.2771 

1

20517301 coutv 170 163

Control variable 174

" S0I Water Level(Range o2.34-4.0)

20517400 S-I.MA fAuctioe 1.0 0.0 

I

20517401 cnulva 170 164

SCotrol variable 175

" S00 CollapsedLevel (Rp0.0-4.0)

20517500 SGI-L sum 1.0 2.2771 

1

205175010.0 1.0 culvar 171

20517502 1.0 cnrvar 172

20517503 1.0 cautlvmr 173

20517504 1.0 cutrivar 174

D-4

* Control vriable 176

* S00 Correte Level

20517600 SG.-.Lsuml.0 22241

20517601-0.0531

20517602 1.0 Cnva 17S

*52.2 SG2Level

SControl variable 270

* S02 Water Volunee

20527000 SC2-W sm 1.0 65.6616 

1

205270010.0 3.0 voidf 261010000

205270023.99 voidf 271010000

20527003 5.94 voidf 262010000

205270044.1 voidf 272010000

20527005 8.97 voidf 263010000

20527006 6.38 voidf 273010000

20527007 9.4 voldf 264010000

20527008 2.3 voidf 274010D00

20527009 3.75 voidf 278010000

205270109.93 void! 265010000

20527011 3.M8 voidf 275010000

205270124.72 voidf 279010000

20527013 10.71 void! 266010000

20527014 1.0 voidf 276010000

20527015 28.558 voidf 267010000

20527016 10.09 voidf 268010000

20527017 10.21 voidf 269010000

20527018 0.072 voidf 277010000

" Control variable 271

" S02 Water Level (Uae of0.0 

- 0.96)

205271005G2-LI f8muoi 1.0 0.0 

1

20527101 crw 270 161

• Control variable 272

" SG2 Water 1vl (Ruane of0.96 

- 1.9)

20527200 S02-1.2 function 1.0 0.0 

1

20527201 cmrlva 270 162

"Control variable 273 • SG2 Water Level (Range of 1.9 

- 2.34)

20527300SG2-13 fimctim 1.0 2.25412 

I

20527301 courivar 270 163

* Conrol variable 274

* S02 Water Level (Range of2.84 

- 4.0)

20527400 Sa2-L4 fuction 1.0 0.0 

I

20527401 cntvw 270 164

s Control variable 275

" S02 Collapscd Level (Ruge 0.0 

- 4.0)

20527500 S02-L sm 1.02.25412 

1

205275010.0 1.0 cntvar 271

20527502 1.0 clatvar 272

20527503 1.0 cwhlar273

20527504 1.0 azuia 274

"Control variable 276

S 002 Corrected level

20527600 SG2-I sum 1.0 2.206 

1

20527601 -0.04812

20527602 1.0 cattvar 273

5.2.3S03 Level

• Control varial 370

* SG3 Water Vohune

20537000 S03-W sum 1.0 65.6344 

1

20537001 0.0 3.0 void! 361010000

20537002 3.99 void! 371010000

20537003 5.94 voidf 362010000

20537004 4.1 voidf 372010000

20537005 8.97 void! 363010000

20537006 6.38 void! 373010000

20537007 9.4 void! 364010000

20537008•2.3 voidf 374010000

20537009 3.75 void! 378010000

20537010 9.93 void! 365010000

20537011 3.•8 voidf 375010000

20537012 4.72 voidf 379010000

20537013 10.71 voidf 366010000

20537014 1.0 void! 376010000

20537015 28358 voidf 367010000

20537016 10.09 void! 368010000

20537017 10.21 voidf 369010000

20537018 0.072 voidf 377010000

" Cocnol variable 371

* SG3 Water Level (Range o!0.0 

- 0.96)

20537100 SG3-LI fimction 1.0 0.0 

1

20537101 cativar 370 161

" Control variable 372

" SO0 WaterLevel(Ranseo!0.96- 1.9)

20537200 S03-1.2 fuactiim 1.0 0.0 

1

20537201 catrlvar 370 162

* Control variable M3

" SG3 Waer Level (Rae of 1.9 

-2.34)
20537300 S03-.3 fScstioe 1.0 2.25353 I

20537301 am'lvar 370 163

SControl variable 374 • S3 Water Level (Rawg of2.84 - 4.0)

20537400 S03-LA finti•e 1.0 0.0 I

20537401 €ouvar 370 164

" Coctrol variable 375

" S03 Collapsed Level (Ralge 0.0.4.0)

20S37500 SG3-L mm 1.0 2.25353 1

20537501 0.0 1.0 emorvar 371

20537502 1.0 - lva 372

20537503 1.0 emmlvar 373

20537504 1.0 cocivar 374

" Cootrol variable 376

" SO Corrected Level

20537600 S03-Le sum 1.0 2273 1

20537601 0.01947

20537602 1.0 onulvar 375

" 5.2.4 SG4 Level

" Coer-ol variable 470

" S04 Water Volume

20547000 SG4.W &u= 1.0 66.1983 I

20547001 0.0 3.0 voidf 461010M00

20547002 3.99 voidf 471010000

20547003 5.94 voidf 462010000

205470044.1 voidf 472010000

20547005 8.97 voidf 463010000

20547006 6.38 voidf 473010000

20547007 9.4 voidf 464010000

2047008 2.3 voidf 474010000

20547009 3.75 voidf 47810O000

20547010 9.93 voidf 465010000

20547011 3.8 void! 475010000

20547012 4.72 voidf 479010000

20547013 10.71 voidf 466010000

20547014 1.0 voidf 476010000

20547015 28.558 voidf 467010000

20547016 10.09 void! 468010000

20547017 10.21 voidf 469010000

20547018 0.072 voidf 477010000

• Control variable 471

* S04 Water Level (Range ofO.0 - 0.6)

20547100 SG4-LI Sancion 1.0 0.0 1

20547101 entrlvar 470 161

" Control variable 472

" S04 Water Level (Range of+0.9 - 1.9)

205472O0 S,4-,2 ioctmio 1.0 0.0 1

20547201 eanrhvar 470 162

• Control variable 473 • SG4 Water Level (Rang• of 1.9.2.94)

2054T308 .o4-1. fitntion 1.0 2.26574 I

20547301 cmlvar 470 163

SControl variable 474

S £04 Water level (Rapne o'2.84 -4.0)

20547400 S04-IA fi0nction 1.0 0.0 I

20547401 estr 470 164

• •Cool variable 475 • S4 Collapsed Level (Range 0.0 -4.0)

20547500 SC4-L sum 1.0 2.26574 I

20547501 0.0 1.0 eerva 471

20547502 1.0 enuvar 472

20547503 1.0 contlvar 473

20475U04 1.0 ntuivar 474

* Control variable 476

SS04 Coereted Level

20547600 S4-Lc sum 1.0 2.297 1

2047601 0.03126

20547602 1.0 Itvar 475

*5.3 breamu Drop

* ocrivar N 800

* Ractor Vesscl Presure drop. kPa

20580000 RV-DP msm 1-3 326.34 1

2058=1 0.0

20580002 0.25 p 005010000

20580003 -0.25 p 061010000

2058 40.26p 06010000

2080005w 0.25 062010000

2050006 0.25 p 007010000

205807-0.25 p 063010000

20580008 0.25p 008010000

2058009 -0.25 p 064010000

• Convar N 801 • SGI Pressure drop. kla

20580100 SGI.DP sum I-3 146.02 1

20580101 0.0

20580102 1.0 p 102030000

20580103-1.0 p 130010000

eoeatrv N 802

• S2 Promw drop, kP

20580200 SG2-DP mm I..W 152.92 1

20580201 0.0

205202 1.0 p 202030000

20580203-1.0 p 230010000

" eotmrl N 803

* S03 PVesre dop. Its

20580300 S3.DP aum I.-3 147.0 1

20580301 0.0

20580302 1.0 p 302030000

20580303.1.0 p 330010000

"cotrtvar N 804

SS04 Pim e drop. kP&

20580400 SC4-DP am IA.3 155.02 1

20580401 0.0

20580402 1.0 p 4020300¢0

20580403-1.0 p 430010000

c amutvar N 8 11

* MPI Pressmre drop, kbP

20581100 MCPI-DP ma I..-3 568.4 I

20581101 0.0

20581102 1.0 pMhead 141

" ont~as N 812

" MCP2 Pressure drp. kPa

205812D0 MCP24DP am 1.-3 558.6 1

20581201 0.0

205•8122 1.OpMbead 241

ocnulvarNl13

"MCP3 Prmmeu drop, kh

20581300 MCP3.-DPsm .3 578.2 1

205813010.0

20581302 1.0pMhead 341

* r"tv N 814

SMCP4 Pessmu drop, bPs

20581400 MCP4-DPm 1.-3 538.0 I

20581401 0.0

2OS1402 1.0 pvbead 441

*VI. Reactor Vessel

6.1Downcwo•.

Volumes above Inlet Nozzle

SCompeotn No I • Dowcommer Volume above imlet Nozzle o*fLoop No I

0010000 dc-opl I c

0010001 3 1

0010101 0.0 0.458 0.15=1 0.0 90.0 0.458 1.0.5 0.358

0000000

0010200013 16.00736 359.2640.939-3

0011101 0010100030020100040.099524 1.01.0 0001100

0012101 0010100020610100010.003375 1.0 1.0 0001000

0013101 005010001 001010001 0.340M 20.0 0.0 0001000

0011110 0.358 0.01.0 1.0

0012110 0.006 0.0 1.0 1.0

0013110 0.35 0.0 1.0 1.0

001120167.067 0.0 0.0

0012201 74.959 0.0 0.0

0013201 94.986 0.0 0.0

Scapone, No 2

*Downcommer.

" Volume above Inlet Nozzle of Loop No 2

00o200 doop2 bemwb

0020001 3 1

0020101 0.0 0.458 0.150023 0.0 90.0 0.458 .0.5 0358

0000000

0020200 013 16.0069+6 559.552 0.939-3

0021101 002010003 0030100040.099524 1.0 1.0 0001100

0022101 002010002 062010001 0.003375 1.0 1.0 0001000

0023101 0060100010020100010.534072 0.0 0.0 0001000

0021110 0.35 0.0 1.0 1.0

0022110 0.006 0.0 1.0 1.0

0023110 0.358 0.0 1.0 1.0

0021201 -63.6400.0 0.0

0022201 73.0980.0 0.0

0023201 -57.609 0.0 0.0

* Cmssooe No 3 * Dowucoaner

- Volume above Inlet Nozzle ofLoop No 3

0030000 dc-rp) 1 nd

0030001 3 1

0030101 0.00.45 0.150023 0.0 90.0 0.458 1.0-S 0.358

00•0000

0030200013 16.072M6 $59.8330.939-3

0031101 003010003 004010004 0.099524 1.0 1.0 0001100

0032101 003010002 063010001 0.003375 1.0 1.0 0001000

0033101007010001 00"010010 5S40 0.00.0 0001000

0031110 0.358 0.0 1.0 1.0

D-5

0032110 0.006 0.0 1.0 1.0

0033110 0.358 0.0 1.0 1.0

0031201-51.5170.0 0.0

0032201 73.129 0.0 0.0

0033201 85.2520.0 0.0

*CarepooentNo 4

*Downeesoar

• Volmne above inlet Nozzle ofLoop No 4

040000 d&400 ranbh

0040001 3 I

0040101 0.0 0.458 0.10023 0.0 90.0 0.458 10.5 0358

0000DO

0040200013 16.007546 5593540.9393

0041101004010003 001010004 0.0¢924 1.0 1.0 0001100

0042101 004010002 06401000I 0.003375 1.0 1.0 0001000

0043101 008010001 004010001 0.33408n 0.0 0.0 0010¢0

0041110 0.358 0.0 1.0 1.0

0042110 0.006 0.0 1.0 1.0

0043110 0.358 0.01.0 1.0

0041201 47.040 0.0 0.0

0042201 73.218 0.0 0.0

0043201171.78 0.0 0.0

a6.2 Dowwcoarnr

• Cold Lae Inlet Volumes

* Caoa~moem No 5

• Downcmer Inlet Volum br Loop I

0035O001o1l brandh

0<OM0¢ 3 1

0050101 0.5340872 1.4440.00.0-90.0-1.444 1.0-50358 00000O

0050200013 16.0149+6 559.1990.939-3

0051101 1441100020050100030.367450 0.73 0.730001000

0.521010050100030060100040.516952 1.0 1.0 0001000

0053101 005010002 0090100010.5340872 1.09 1.090001000

0051110 0.358 0.0 1.0 1.0

0052110 0.358 0.0 1.0 1.0

0053110 0.358 0.0 1.0 1.0

0051201 4253.60.0 0.0

0052201-302.150.0 0.0

0053201 4546.80.0 0.0

C oponenm No 6

* Dowamo cr Inlet Volume for Leap 2

0060000 d klach

0060001 3 1

0060101 0.5340872 1.444 0.00.0-90.0.1.444 1.0.5 0.358

00DM

0060200 013 16.0136.6 559.2590.939-3

0061101 244110002 006010003 0.567450 0.73 0.73 0001000

0062101 006010003 007010004 0.516952 1.0 1.0 0001000

0063101 006010002010010001 0.O340872 1.09 1.090001000

0061110 0.358 0.01.0 1.0

0062110 0.358 0.01.0 1.0

0063110 0358 0.01.0 1.0

0061201 48003 0.0 0.0

0062201 19.270 0.0 0.0

006320! 4536.5 0.0 0.0

SComponent No?7 • Dowmncoer lain Volume for Loop 3

0070000 d-isa13 blrac

0070001 3 1

0070101 0J34087 1.444 0.00.0.90.0-.1444 M.0S 0358

0070200 013 16.014746 560.098 0.939.3

0071101 344110002007010003 0.567450 0.73 0.73 0001000

0072101 0M7010003 00S0100040.516952 1.0 1.0 0001000

0073101 007010002 011010001 0.5340M72 1.09 1.090001000

0071110 0.3" 0.01.0 1.0

0072110 0.358 0.0 1.0 1.0

0073110 0"35 0.0 1.0 1.0

0071201 4892.4 0.0 0.0

0072201 296.20 0.0 0.0

0073201 454.2 0.0 0.0

- Component No 8

*Dowscoensser Inlet Vokimme 11or Loop 4

0080000 dc.inl4 amanh

0080001 3 1

00801010o534072 1.44 0.0U0-9o.0.1.444 1.0-50.358

000¢0

0080200 013 16.0156.6 5593440.939.3

0081101 444110002 008010003 0.567450 0.73 0.73 0001000

082101 008010003 005010004 0.516952 1.0 1.0 00010O0

0083101 008010002012010001 0.340$721.00 1.090001000

0081110 0358 0.0 1.0 1.0

002110 0.358 0 1.0 1.0

0083110 0.358 0.0 1.0 1.0

00812014525.0 0.0 0.0

0082201 6056 0.0 0.0

0083201 45533 0.0 0.0

*6.3 Downcomor. * Middle Past Volumes

SCotmponeat No 9

* mnro Middle Pani for Lop I
0090000 d4c-l -

OO9000 6

0090101 O.O000 2

0090102 0.782562 5

0090103 0.00000 6

0090201 0.650762 1

0090202 0.73262 5

0090301 0.9010 1

0090302 0.7445 2

0090303 1.0S0 4

00903041.0050 S

0090303 0.825 6

0090401 0.4970M97 I

0090402 0`.529797 2

0090403 0O000OO 5

0090404 0.7012277 6

0090601 -90.06

O0D09 1.0-50.0 6

0090901 0.0 0.0 3

009100100000006

0091101 00010003

0091201 013 15.92504 559.167 0.00.00.0 I

0091202013 15.951W"6 559.177 0.00.00.0 2

0091203013 15.9599+6 559.179 0.00.00.0 3

0091204013 13.967546 559.181 0.00.00.0 4

0091203 013 13.9749"6 559.15 0.0 0.00.0 5

0091206013 15.9M8+6 539.192 0.0 0.0 6

00913001

0091301 4541A0.0 0.0 I

0091302 4550.40.0 0.0 2

0091303 4547.1 0.0 0.0 3

0091304 455930.0 0.0 4

091230 4522.5 0.0 0.0 5

0091401 0.432 0.0 1.0 1.0 1

0091402 0.14 0.0 1.0 1.05

W092001 0.939-3 6

* Coupoou No 10 •Downco•.

Middk Partr Loop 2

010000 dcm.-12 anmmbm

01000016

0100101 0.000000 2

0100102 0.782562 5

0100103 0.00OOO 6

0100201 O.650762 1

0100202 0.782562 5

0100301 0.9010 1

01OO302O.7445 2

0100303 1.0550 4

01003041.0050 5

01003M 0.s3 6

0100401 0.4970897 1

0100402 0.5629797 2

0100403 0.0000003

0100404 0.7012277 6

0100601 -90.06

0100801 .0-.5 00 6

0100901 0.0 " 5

01010010000000 6

0101101 00010005

0101201013 13.925006359.22=0.00.0 0.01

0101202013 15.951W'. SS9.2370.00.0 0.02

0101203 013 1S.95996559 .240 0.0 0.0 U 3

0101204 013 13.967546 559.240 0.0 0.0 0.0 4

0101203 013 13.974946559.2520.00.0 0.05

0101206013 IS.916 S59.2355 0U00.0 0.06

01013001

0101301 4525.50.0 0.0 1

0101302 4518.30.0 0.0 2

0101303 4533.1 0.0 0.0 3

0101304 4436.50.0 0.0 4

0101303 4641.20.0 0"0 S

0101401 0.432 0.01.01.01

0101402 0-514 0.0 1.0 1.05

01020010.939.3 6

" Component No I1

• Middle PMai ftr Loop 3

0110000 4cm-Il am"ulia

01100016

0110101 0.000000 2

0110102 0.7M2562 5

0110103 0.000000 6

0110201 0.650762 I

0110202 0.732562 5

01103010.9010 I

0110302 0.7445 2

0110303 1.0550 4

0110304.1.0050 5

01103050.8325 6

0110401 0.4970397 1

0110402 0.5629797 2

0110403 0.00M 000

0110404 0.7012277 6

0110601 -90.06

0110801 1.0.50.06

0110901 0.0 0.0 5

0111001 0000000 6

01111010001000 $

0111201 013 15.9"; 560.0•067 0.0 0.0 1

0111202013 15.95134.560.076 0.00.".02

0111203 013 15.959944560.077 0.0 0.0 0.0 3

0111204013 15.967546560.075 0.00.00.04

0111205 013 15.9749•650.066 0.00.00.03

0111206013 15.93496 $60.032 0.00.00.06

01113001

0111301 453320.0 0.0 1

0111302 4537.00.0 0.0 2

0111303 4535.90.0 0.0 3

0111304 4534.60.0 0.0 4

0111305 4535.90.0 0.0 3

0111401 0.432 0.01.01.01

0111402 0C514 0.01.01.05

01120010.939-3 6

*Coa~onew No 12

*Dovwnconw

*Midle Put fo Loop 4

0120000 dcm-14 -k

0120001 6

0120101 0.000000 2

0120102 0.712562 3

0120103 0.000000 6

0120201 0.650762 1

0120202 0.732562 5

0120301 0.90!0 1

0120302 07443 2

0120303 1.0550 4

0120304 1,0050 5

0120303 0.3235 6

0120401 0.4970897 1

012D402 0.5629797 2

0120403 0.00M005

0120404 0.7012277 6

0120601 -90.0 6

0120601 1.0-5 0.06

0120901 0.0 0.0 5

012100100000006

0121101 00 01000

0121201013 15.9250+6 559.314 0.0 . 0.0 1

0121202013 15.9"136 559,324 0,00.00.0 2

0121203013 15.959936559.326 0.00.00.0 3

0121204013 15.96756 559331 0.00.00.0 4

0121205 013 15.9749* 559333 0.0 0.0 5

0121206013 15.943436559.366 0.00.00.0 6

0121300 1

0121301 4564.380.0 0.0 1

0121302 4571.20. 0.0 2

0121303 455U. 0.0 0.0 3

0121304 4596.5.0.0 0.0 4

0121303 44773.3 0.0 " 5

0121401 0.432 0.0 1.0 1.0 I

0121402 0.514 0.0 1.0 1.03

0122001 0.9393 6

* Coapouen No 13

*"DODDor TrAmDMISmDewtio

0130000 DwC-uj mqipm

0130001 241

0130011 00901003 010010004 0.430394 1.0 1.0 0001000

0130021009020003 01002D00040.370496 1.0 1.0 00O00

0130031 009030003 010030004 0-42270 1.0 1.0 0001000

0130041 009040003 0100400040.542270 1.0 1.0 O001000

0130031 009050003 010050004 0.16570 1.0 1.0 0001000

0130061 009060003 010060004 0.491040 1.0 1.0 0001000

0130071 012010003 009010004 0.4303941.0 1.0 0001000

0130001 012020003 00902000410.370496 1.0 1.0 0001000

0130091 0120300030090300040.542270 1.0 1.0 0001000

0130101 01204M003009040004 o..22M 1.0 1.0 0001000

0130111012050003 10900040.416570 1.0 1.0 0001000

0130121012060003 0090600040.481040 1.0 1.0 0001000

01300121,01.0 1.0 1000000 100000003

0130022 1.0 1.0 1.0 1000000100000006

0130032 1.0 1.0 1.0 1000000100000009

01300421.01.0 1.0 1000M00100000 12

0130032 1.0 1.0 1.0 100000 10000000 15

0130062 1.0 1.0 1.0 100000010000M00 18

0130072 1.0 1.0 1.0000 19

01302 1.0 1.0 1.000 0 20

01300921.01.0 1.000 021

0130102 1.01.0 1.000 0 22

0130112 1.0 1.0 1.000023

0130122 1.0 1.0 1.000 0 24

0131011 0.0 0.0 3

0131021 0.0 0.0 6

0131031 0.0 0.0 9

0131041 0" 0.0 12

01310310.0 0.0 I1

01310610.0 0"0 I

01310710. 0.0 19

01310310.0 0.020

01310910.0 0.021

01311010.0 0.022

01311110.0 0,023

01311210.0 0.024

0132011 0.47 0.0 1.01.03

0132021 0.494 0.0 1.01.0 6

0132031 0.14 0 1.0 1.0 9

0132041 0.514 0.0 1.0 1.0 12

0132051 0.514 0.0 1.01.015

0132061 0-53 0.0 1.01.015

0132071 0.478 o.0 1.01.0 19

0132091 0.498 0.0 1.01.020

0132091 0.514 0.0 1.0 1.021

0132101 0.514 0.0 1.01.022

0132111 0.514 0.0 1.01.023

0132121 0.583 0.0 1.01.024

:6.4 Down== Bott Volmzes

*Compoocut No 14

*Downconursi.

"Bo omVozmo for Loop I

0140000 dc.bdl blrnch

0140001 3 1

0140101 0.0 0.712 0.701544 0.0 -90.0-0.712 1.05 0.125

0000000

0140200013 16.00646 359.2040.939-3

0141101 009060002 014010001 1.0635600. 0,0 0`00IO0

0142101014010003 015010004 0.000000 1.0 1.0 O0010OO

0143101 014010001 013010001 0.430241 1. 1.5 0001000

0141110 0.753 0.0 1.0 1.0

0142110 0.738 0"0 1.0 1.0

0143110 0.040 0,01.0 1.0

0141201 4672.2 0.0 0.0

0142201 237.35 0.0 0.0

01432014543.7 0.0 0.0

Compionent No is

Bottom Volme for Loop 2

0150000 d€-1btl branch

0130001 3 1

01501010.0 0.7120.701344 0.0 -90.0.0.7121.0-50.125

0=00000

0150200013 16.008546 3592870.939-3

0151101010060002 01010001 1.063 00 0001000

0152101 015010003 016010004 0.000000 1.0 1.0 0001000

0153101015010001 019010001 0.430241 1.5 1.3 0001000

0151110 0.756 ".0 1.0 1.0

0152110 0.756 0.01.0 1.0

0153110 0.040 0.0 1.0 1.0

0151201 4131.80.0 0.0

0152201 -173.30 . 0.0

0153201 4544.5 0.0 0.0

* Coou•oo No 16

* Dowocl~tw.

- Boumr Vohme. lbr Loop 3

0160000 do-bt banch

0160001 3 I

0160101 0.0 0.712 0.701544 0.0 -90.0-0.712 1.05 0.125

0000000

0160200013 16.00U46 $60.0130.939-3

0161101 011060002 016010001 1.0635600.0 0.0 0001000

0162101 016010003 017010004 0.000000 1.0 1.0 W0000

0163101 016010001 020010001 0.430241 1.3 1.5 0001000

0161110 0.753 0.0 1.0 1.0

0162110 0.7S0.0 1.0 1.0

0163110 0.040 0.0 1.0 1.0

0161201 4521.1 0.0 0.0

0162201 -194.21 0.0 0.0

0163201 4540.00.0 0.0

* COpooew No 17

* Downeommw.

Bottom Volume for .•op 4

017000 D W4 branch

0170001 3 1

01701010.0 0.712 0.701544 0.0 -.90.0-0.712 1.0-5 0.125 0000000

0170200 013 16.0086# 359.374 0.939-3

0171101 012060002 017010001 1.063560 0.0 0.0 0001000

0172101 017010003 014010004 0.000000 1.0 1.0 0001000

0173101 017010001 021010001 0.4302411.5 1.5 0001000

0171110 0.756 0.0 1.0 1.0

0172110 0.758 0.01.0 1.0

0173110 0.040 0.01.0 1.0

01712014331.7 0.0 0.0

0172201 110.80 0.0 0.0

0173201 4546.7 0.0 0.0

' 6.5 Lowor Plemic Bottom Voabiwt

* Coqcout No is * LoworPlemuE:

* Bonom Vomom for Loop I

0180000 do-lpbl brant•h

013000 3 1

0130101 0.0 0.3253 1.962399730`0 90.0 0.8255 1.0-5 0.236 000000

0160200013 15.98444 559.1610.93M-3

0111101 018010003 01901004 3.677077 1.0 1.0 0001000

0182101018010002022010001 0.91926925 0.0 0.0 0001100

0163101 018010002034010001 0.00157373 3.5 3.S 0001100

0181110 0.236 00 1.0

0132110 0.170 001.0 1.0

0183110 0.008 001.0 1.0

0181201 9.3717 0.0 0.0

0182201 4525.5 00 0.0

0133201 13M33 0.0 0.0

D-6
* Compooem No 19

*LowerPaftnur

B Bornm Volukaicr Loop 2

0190000 dc4pb2 Wa

0190001 3 1

0190101 0.0 0.255 1.96239975 0.0 90.0 0.2551.0.S 0.236.

00000

0190200 013 15.0S84+6 559.242 0.939-3

0191101 019010003 0200100043.677077 1.0 1.0 0001000

0192101019010002 023010001 0.91926925 0.0 0.0 0001200

0193101019010002 0340100010.00157875 3.535 0001100

0191110 0.236 0.0 1.0 1.0

0192110 0.170 0.0 1.0 1.0

0193110 0.008 0.0 1.0 1.0

0191201 2.1099 0.0 0.0

0192202 4538.9 0.0 0.0

0193201 13387 0.0 0.0

" Conpocat No 20

" Lower PIem

" Domm VOhme for Loop 3

0200000 kdpll I

020000 3 1

0200101 0.0 0.8255 1.96239975 0.0 90.0 0.8255 1.0-5 0-236

0000000

0200200013 15.88"46 559.9700.939.3

0201101 020010003 021010004 3.A770771.0 1.0 000100

0202101 020010002024010001 0.919269250.00.0 0001100

0203101 020010002034010001 0.001578753. 3.5 0001100

0201110 0.236 0.0 1.0 1.0

02110 0.170 0.0 1.0 1.0

0203110 0.008 0.0 2.0 2.0

020120140.737140.0 0.0

0202202 4529.5 0.0 0.0

0203201133760.0 0.0

* Component No 21

* Lower Peium

Swomrn Vokume for Loop 4

0210000 dc-Ipb4 tincb

0210001 3 I

0210101 0.0 0.8255 1.96239975 0.0 90.0 0.8255 1.0.5 0236

O0OOOO

0210200103 15.8884.+6 5593310.939-3

"0211101 0210100030180100043.677077 1.0 1.0 0001000

0212101 021010002025020001 0.91926M25 0.00.0 0002200

0213101 021010002 034010001 0.00157875 3.5 35 000100

0211110 0.236 0.01.0 1.0

0212110 0.170 0.0 1.0 1.0

0213110 0.008 0.01.0 1.0

02112013.0234 0.0 0.0

0212201 4529.6 0.0 0.0

0213201 13396 0.0 0.0

*6.6 Lower Piebirm Top Vobumes

* Camoporct No 22

* Lower Pecmu

* Top Voloen for Loop I

0220000 &4pt.l kambr

0220001 3 1

0220101 0.0 03295 0.4455035 0.0 90.0 0.3295 1.0-50.170

0000M

0220200 013 15.8667+6 559.1540.939.3

0221101 022010002 026010001 1.04933625 0.2 02 0001000

02220102 2010002 035010001 0.00684255 1.0 1.0 0001100

0223101 02201000203600001 0.002375 1.0 1.0 0001100

0221120 0.170 0.0 1.0 1.0

0222110 0.002 0.01.0 1.0

0223110 0.002 0.0 1.0 1.0

0221201 4466A 0.0 0.0

022220150311 0.0 0.0

0223201 8.7707 0.0 0.0

" Coupncet No 23

" Lower Pammo

• Top Volune lbr Loop 2

0230000 dc-Ipt2 bme

0230001 3 1

02301010.0 03295 0.4455035 0.0 90.0 0329 1.0-50.170

000000

0230200 013 15.2665 559.234 0.939-3

0231101023010002 027010001 1.04933625 0.202 0001000

0232101023010002035010001 0.00684255 1.0 1.0 0001100

0233101023010002 03600010.002375 1.0 1.0 0001100

0231110 0.170 0.01.0 1.0

0232110 0.002 0.0 1.0 1.0

0233110 0.002 0.0 1.0 LO

0232201 4479.8 0.0 0.0

0232201 50.286 0.0 0.0

023320118.7556 0.0 0.0

" ComponenNo24

" Lower Plemum

" Top Volume for Loop 3

0240000 dc1-Ipt3 brach

024000D 3 1

0240101 0.0 03295 0.4455035 0.0 901 03295 1.0-50.170

0000

0240200 013 15.8666+6 559.963 0.939-3

0241101 024020002028020001 1.0433625 0.20.2 0002000

0242101 024010002035020001 0.00634255 1.0 1.0 0001100

0243101024010002036010001 0.002375 1.0 1.0 0001100

0241110 0.170 0.0 1.0 1.0

0242110 0.002 0.0 1.0 1.0

0243110 0.002 0.0 1.0 1.0

0241201 4470.5 0.0 0.0

0242201 50.252 0.0 0.0

0243201 8.7554 0.0 0.0

" Conpooem No 25 " Lower Plemmr

* Top Volume for Loop 4

050000 dc.I.4 breah 0250001 3 2

0250101 0.0 0.329 0.44550350.0 90.0 03295 1.0-50.170

0250200 013 15.8666.6 5593240.939-3

0251101 025010002 029010001 1.04933625 0.2 0.2 0001000

0M52101 025010002 035010001 0.0063425 1.0 1.0 0001100

0253101 02500002036010001 0.002375 1.0 1.0 0001100

0251110 0.170 0.01.0 2.0

0252110 0.002 0.0 1.0 1.0

0253110 0.002 0.010 1.0

02512014470.5 0.0 0.0

0252201 50294 0.0 0.0

0253201 8.7645 0.0 0.

6.7 Core

*ComponentNo 26 Cow

• I/pan (40.75 FA) ofLoop 1

0260000 core-Il pipe

0260001 10

0260101 1.0500465 10

0260201 1.0500465 9

0260301 0.353 10

0260401 0.0 10

0260601 90.0 10

0260801 1.0-5 0.0106 10

0260902 0.02 0.02 9

0261001 0000100 10

0261101 0002000 9

0261201 013 151531+6 562S.25 0.00.00.0 1

0261202013 15.1421+6 566.949 0.0 0.0 0.02

0261203 013 I0309.6 571.962 0.0 0.0 0.0 3

0261204 013 15196.1 576.681 0.00.00.04

0261205 013 15.80826 580.946 0.0 0.0 0.0 5

0261206 013 15.7968.6584347 0.00.00.06

0261207 013 15.7853+6 S56.988 0.00.00.07

0261200013 15.7739+6 58.935 0.00.00.08

0261209013 15.762446 50.120 0.00.00.09

0261210 013 15.7509.6 590.59 0.00.0 0.0 10

02613001

0261301 4466.40.0 0.0 9

0261401 0.01060.0 1.0 1.09

0262001 0.939-3 10

* Cceqpoocat No 27 *Core

* 1/4 pm (40.75 FA) of Loop 2

0270000 core-12 V"p

0270001 10

0270101 1.0500465 10

02702011.0 004659

0270301 0.353 10

0270401 0.0 10

0270601 90.010

02701 1.0-. 0.0106 10

0270901 0.020.029

0271001 0000100 10

0271101 00020009

0271201 013 152.529+6561.778 0.00.0 0.0 1

0271202013 I15.841946 56.140 0.00.0 0.0 2

0271203013 15.830746 S70.628 0.00.0 0.0 3

0271204013 251194+. 574.810 0.00.0 0.0 4

0271205013 15.=08046578.635 0.00.0 0.0 5

0271206013 15.7966.6581.718 0.00.0 0.0 6

0271207 013 15.7852+4 584.060 0.0 0.0 0.0 7

0271208 013 15.7737.6585.716 0.00.0 0.0 8

0271209 013 15.762346 5W.841 0.0 0.0 0.0 9

0271210 013 15.7500+6 587.284 0.0 0.0 0.0 10

0271300 1

0271301 4479.90.0 0.0 9

0271401 0.01060.0 11.0 9

0272001 0.939-3 10

• Coqmoem No 2

* Core:

• 14•'n (40.75 FA) of.oop 3

0280000 core-D pk

02800012 0

0280101 1.05 6 10

0280201 1.0500465 9

0280301 0.353 10

0280401 0.0 20

02806 90.0 10

0280801 1.0-5 0.0106 10

028M090 0.02009

02810010000100 10

02811010001000 9

0281201013 15.8530+6 52528 0.00.00.0 I

0281202013 1514206566.9A8 0.0 0.00.0 2

0281203 013 21308.306 571.5000.0 00.0 3

021204 013 15.8195+65 75.755 0.0.0 0.0 4

081205 013 5.802+6 579.648 0.0 0.0 0.0 5

0281206 013 15.7968+6 58.733 0.0 0.0 0.0 6

0281207 013 15.753+6 M85.116 0.0 0.0 0.0 7

0281208 013 15.7739.6 586.172 0.0 0.0 0.0 8

0281209 013 15.7625+6 5•7.946 0.0 0.00.0 9

O281210 013 15.75114658,.39 0.0 0.0 0.0 10

081300 I

0281301 447030.0 0.0 9

0281401 0.01060.0 1.0 1.019

02001 0.939-3 20

*Coaipooem No 29

*Core:

* 1/4 pan (40.75 FA) of Loop 4

0290000 core4 pipe

0290001 10

02901011.050046 10

0290201 .0500465 9

0290301 0353 10

0290401 0.0 10

0290601 90.0 10

0290802 1.0-5 0.0106 10

0290901 0.020.029

02910010000100 10

0291101 0001000 9

0291201 013 15.8530+6562.079 0.00.00.0 1

0291202 013 15.842056566.8 I 10.0 0.0 0.0 2

0291203013 15.8308+6 571.640 0.0 0.00.0 3

0291204 013 15.81956 576.175 0.0 0.0 0.0 4

0291205 013 15.80•2+6 803070.0 0.00.0 5

0291206013 15.7967+6 583.576 0.00.00.0 6

0291207013 15.7853+65 56.1150.00.00.0 7

0291208 013 15.7738+6 587.987 0.00.00.0 8

0291209013 15.7623+6 589.1320.0 0.00.0 9

0291210 013 15.7509.6 589.611 0.0 0.0 0.0 10

02913001

0291301 4470.50.0 0.0 9

0291401 0.01060.0 1.0 1.09

0292001 0.939.3 10

62 Core Uhabed Top VohMi

• Compooe No 30

* Core Top: • Volume for Loop I

0300000 oore-t1l branch

0300001 2 2

03001010.0 0.469 0.68085 0.0 90.0 0.469 1.0-5 0.0106

0000100

0300200 013 15.7405+6 590.591 0.939-3

0301101026100002 030010001 1.50045 0.5 0.5 0002000

0302101030010002 037010001 0.0 0.9 0.9 0002000

0301110 0.01060.0 1.0 1.0

0302110 0.01060.0 1.0 1.0

03012014466.4 0.0 0.0

0302201 4466.4 0.0 0.0

SCoampooen No 31

SCore Top:

* Voluhm for Loop 2

0310000 mcr.f2 t~ach

0310001 2 2 0310101 0.0 0.469 066808 0.0 90.0 0.469 .0-5 0.0106

0000100

0310200013 15.7405.6 587.2800.939-3

0311:01 027100002031010001 1.05004650-50.5 0001000

0312101 031010002 0380100010.0 0.9 0.9 0001000

0311110 0.01060.0 1.0 1.0

0312110 0.01060.0 1.0 1.0

0311201 4479.9 0.0 0.0

0312201 4479.9 0.0 0.0

Comonem No 32

• Core Top Vokume for Loop 3

020000 c00 D bmacb

0320001 2 1 0320101 0.0 0.469 0.686805 0.0 90.0 0.469 1.0-5 0.0106

0000100

0320200013 15.7407+6 588392 0.939-3

0321101 0291000M 032010001 IM0 0.5 0.5 0001000

0322101 032010002 039010001 0.0 0.9 0.9 0001000

0321110 0.01060.0 1.0 1.0

0322110 0.0106 0.0 1.0 1.0

03212014470.5 0.0 0.0

0322201 470.50 0.0

* Coaponeat No 33

• C4e TOP:

* Volume for Loop 4

0330000 core-d licb

0330001 2 1

0330101 0.0 0.469 0.686808 0.0 90.0 0.469 1.0.5 0.0106

0000100

0330200013 15.7405+6 599.6070.939-3

0331101 029100002033010001 1.054650.50-5 0001000

03321010330100020400100010.00.90.9 0001000

D-7
0331110 0.01060.0 1.0 1.0

0332110 0.01060.0 1.0 1.0 0331201 44703 0.0 0.0

0332201 44"70.3 0.0 0.0

° 6.9 Core BypasE * Inside Baft and Betwee Bfle and Bared

0-

- Cornponeet No 34

*Baffd bypm

0340M c*-bybafpipe 0340001 4

0340101 0.04

0340201 0.249642 3

0340301 1.005 1

0340302 1.055 3

0340304 1.21354

0340401 0.406876 1

0340402 0.484764 3

0340403 0.484054 4

0340601 90.0 4

0340801 1.065 0.070 4

0340901 1.0 1.0 3

034100100000004

03411010001100 3

0341201 013 15.760646 59.383 0.0 0.00.0 1

0341202 013 15.7529,6 S559.32 0.00.00.0 2

0341203 013 15.74516 559.380 0.0 0.0 0.0 3

0341204013 15.7368+6 58.5770.00.00.0 4

03413001

0341301 53.5370.0 0.0 3

0341401 0.070 0.0 1.0 1.03

0342001 0.939-34

*6.10 Cwr Bypa

Inside 121 FA (Guide Tubes)

*cornoameo No 35 C aom Bypass inside 121 FA

0350000 co-by121 pipe

0350001 8

0350101 0.206982 5

0350102 0.08

0350201 0.091962 4

035020 0.07

0350301 0.706 5

0350302 0.901 6

0350304 3W75 7

0350305 1.592 8

0350401 0.0 5

0350402 0.558709 6

0350403 6.997912 7

0350404 0.219073 8

0350601 90.0 3

03503 01 1.0.5 0.011 5

0350802 1.0-5 0.00286

0350803 1.0-5 0.120 7

0350804 1.0-5 0.013 8

0350901 0.250.254

0350902 1.0 1.0 5

0350903 0.0 0.0 7

0351001 000000 8

0351101 000100 7

.0351201013 15.7800+ 559.387 0.0 0.0 0.0 1

0351202013 15.7700+6 559.340.0 0.00.0 2

0351203 013 15.7600+6 559.381 0.00.00.0 3

0351204 013 15.7500+6 559.378 0.00.0 0.0 4

035I205 013 15.7400+6 559.376 0.00.0 0.0 3

0351206 013 15.732846 560.844 0.0 0.00.0 6

0351207"013 15.716546 30.23 0.0 0.0 0.0 7

0351201 013 15.697S46 503.25 0.0 0.00.0 8

03513001

0351301 201.140.0 0.0 S

0351302 0.0 0.0 0.0 7

0351401 0.00280.0 1.0 1.04

0351402 0.070 0.0 1.0 1.07

0352001 0.939-3 8

6.11 Core Bypam: Inside 42 FA

SCoupooet No 36

Core Bypass inside 42 FA

0360000 o-by42 pip

0360001 6

0360101 0.06

03602010.022351 5

0360301 0.706 5

0360302 0.901 6

0360401 0.0160966 5

0360402 0.09954 6

0360601 90.0 6

0360801 1.0-S 0.00187 6

0360901 0.2 0.2 S

0361001000000 6

03611010001000 0

0361201013 15.045544 559.413 0.0 0.00.0 I

0361202 013 15.•200+6 559.409 0.0 00.0.0 2

0361203 013 15.7945+6 559.405 0.0 0.0 0.0 3

0361204013 15.7689+6 559.4020.000.0.0 4

0361205 013 15.7434+ 559.3980.0 .00.0 5

0361206 013 15.72806 55914 0.0 00.0.0 6

03613001

0361301 35.0460.0 0.05

0361401 0.001870.0 1.0 1.05

0362001 0.93903 6

0 6.12 Upper Pk=nu inletVchnms

* Compone No37 * Upp" plcmm

m lVoltne forLoop 1

0370000 UP-Ial brandl

0370001 4 1

0370101 0.0 0.432 0.4929 0.0 00.00.432 1.0.5 0.091 DODOOOO

0370200 013 15.719946 590.131"0.939-3

0371101 0304000 037010001 0.0676387S 1.0 1.0 0001000

0372101 037010003 0380100040.0 1.0 1.0 0001000

0373101 03506000 0370100020.0 1.0 1.0 0001000

0374101 03701002 0410100010.77943425 0.20.20001000

0371110 0.07000.01.0 1.0

0372110 0.091 0.01.0 1.0

0373110 0.01060.01.0 1.0

0374110 0.091 0.01.0 1.0

0371201 23.689 0.0 0.0

0372201 3.7547 0.0 0.0

0373201 57.703 0.0 0.0

0374201 4.23A 0.0 0.0

SCooaoam No 38

* Upppkiln

•nlet Volum for Loop 2

0380000 U-h-n brand

0380001 4 1

0380101 0.0 0.432 0.492 0.0 90.0 0.432 1.0-5 0.091

0000000

0380200013 15.7199.6 586.701 0.93-3

0381101 034040002 038010001 0.06763875 1.0 1.0 0001000.

0382101 030100003 00900040.0 1.0 1.0 0001000

0383101 035060002 03801000 0.0 1.0 1.0 0001000

0384101038010002 0420100010.77943425 0.2 0.2 0001000

0381110 0.07000.01.0 1.0

0382110 0.091 0.0 1.0 1.0

0303110 0.01060.01.0 1.0

0384110 0.091 0.0 1.0 1.0

0381201 27.708 0.0 0.0

03•2201 66.605 0.0 0.0

0383201 4-535 0.0 0.0

0384201 4529.3 0.0 0.0

" ComponentNo 39

" Upper plmnu

" Inlet Volume f•"Lmp 3

0390000 UP-113 branch

0390001 4 1

0390101 0.0 0.432 0.49299 0.0 90.00.432 1.05 0.091

9000<0

03090200013 15.7199+6 588.3660.939.3

0391101 034040002 0309010001 0.06763875 1.0 1.0 0001000

0392101 039010003 0400100040.0 1.0 1.0 0001000

0393101 03506000203901000 0.0 1.0 1.0 0001000

0394101 03090100= 043010001 0.77943425 0.2 0.2 0001000

0391110 0.07000.01.0 1.0

0392110 0.091 0.0 1.0 1.0

0393110 0.01060.0 1.0 1.0

0394110 0.091 0.01.0 1.0

0391201-23.781 0.0 0.0

0392201 -62.784 0.0 0.0

0393201-10.1100.0 0.0

0394201 4566.00.0 0.0

• Componen No 40 • Upperpweem

SInlet Volume fo Loop 4

0400000 UP-IJM branh

0400001 4 1

0400101 0.0 0.4320.492998 0.0 00.00.432 1.0-5 0.091

OD00D00

0400200013 15.7199M 589.071 0.93M-3

0401101 034040002 040020001 0.06763975 1.0 1.0 0001000

0402101040010003 0370100040.0 1.0 1.0 0001000

0403101 035060002 040020002 0.0 1.0 1.0 0001000

0404101 040010002 044010001 0.7794342S 0.2 0.2 0001000

0401110 0.07000.0 1.0 1.0

0402110 0.091 0.0 1.0 1.0

0403120 0.01060.0 1.0 1.0

0404110 0.091 0.0 1.0 1.0

0401201 25.921 0 0.0

0402201 .20.6160.0 0.0

0403201 69.011 0 0.0

0404201 4523.3 0.0 0.0

6.13 Upper Plen SIoweVokume3

* Conpoom No 41

SUppcrpleknum

SLower Volume for Loop 1

0410000 UP-Loal branch

0410001 4 I

0410101 0.0 1.469 2.2191995 0.0 90.0 1.469 1.0.5 0.343

D0000•

0410200013 15.7125+6 $90.0620.939,-3 0411101 036060002 041010001 0.014754 1.0 2.0 0001100

0412101 041010003 0420100040.0 1.0 1.0 0001000

0413101 041010002045010001 0.823 0.20.2 000100

0414101041010002 0490100010.2605 0.2 0.2 0001000

0411110 0.032 0.01 .0

0412110 0.343 0.0 1.0 1.0

0413110 0.193 0.0 1.0 1.0 0414110 0.040 0.01.0 1.0

0411201 8.8820.0 0.0

0412201-11.1070.0 0.0

0413201 2395.60.0 0.0

0414201 2149.20.0 0.0

SComaponent No42

" Uppo•Lrpuu " LowerVome for Loop 2

0420000 UP-LoI2 banch

0420001 4 1

0420201 0.0 1.4692.21919930.0 90.0 1.469 1.0-50343

0000000

0420200 013 15.7125•6 56.645 0.93-3

0421101036060002 0420100010.014754 1.0 1.0 0D01100

0422101 042010003 043010004 0.0 1.0 1.0 0001000

0423101042010002 0460100010.825 0.2 0.2 0001000

0424101042010002 03001000 0.260 0.2 0.2 0001000

0421110 0.032 0.0 1.0 1.0

0422110 0.343 0.01.0 1.0

0423110 0.193 0.0 1.0 1.0

0424110 0.040 0.0 1.0 1.0

0421201 9.0203 0.0 0.0

0422201.0.15013 0.0 0.0

04232012379.0 0.0 0.0

0424201 2148.3 0.0 0.0

* Compone No 43

SUpper plonuen

* Lower Volume for Loop 3

04300D0 UP-Lo branch

0430001 4 2

0430101 0.0 1.469 2.2191M 0.0 90.0 1.469 1.0-S 0-.43 000000

0430200013 15.7125465 8311 0.939-3

0431101036060002 0430100010.014754 1.0 1.0 0001100

0432101 043010003 044010004 0.0 1.0 1.0 0001000

0433101043010002 047010001 0.8. 0.20.2 0001000

0434101 043010002 051010001 0.260 0.20.2 0001000

0431110 0.032 0.0 1.0 1.0

0432110 0.343 0.0 1.0 1.0

0433110 0.193 0.0 2.0 1.0

0434110 0.040 0.0 .0 2.0

0431201 8.1993 0.0 0.0

043220110.596 0.00.0

0433201 24063 0.0 0.0

0434201 2156.9 0.0 0.0

" Coaqoanoe No 44

* Upper plkmn * Lower Volume far Loop 4

0440000 1WNoM branch

0440001 4 1

0440101 0.0 1.469 .2191995 0.0 90.0 1.469 1.0-5 0.343

00000

0440200 013 15.712546 589.008 0.93m-3

0441101 036060002 04401000 0.014754 1.0 1.0 0001100

0442101 044010003 0410100040.0 1.0 1.0 0001000

0443101 044010002 048010001 0.825 0.20.2 0001000

044410 04401000 0520100010.26030,20.2 0001000

0441110 0.032 0.01.0 1.0

04421100.343 0.0 1.0 1.0

0443110 0.193 0.0 1.0 1.0

0444110 0.040 0.0 1.0 1.0

044120111.9440 0.0 0.0

04422011.3771 0.0 0.0

0443201 2391.28 0.0 0.0

0444201 2149.6 0.0 0.0

6.14 Upper Plenu

NO MideVolume

SComoneu No 45

* Upper pum

* Middle Volume fbr Loop I

0450000 UP-MdII branch

0450001 3 1 0450101 0.01.06 1.81735125 0.0 90.0 2.106 1.0-5 0.193

00000

0450200013 15.701046 519.98 0.939-3

0451101 045010003 0460100040.0 2.0 1.0 0001000

0452101045010003 0490100040.6268103 1.0 1.0 0902000

0453101045010002054010001 0.23707475 1.0 1.0 0001000

0451110 0.193 0.01.0 1.0

0452110 0.055 0.01.0 1.0

0453110 0.040 0.01.0 1.0

0431201 -51.465 0.0 0.0

0452201 2359.60" 0.0

0453201 93.7260.0 0.0

0 Component No 46

Upperpleom , o *middle vottune far Loop 2

D-8
0460000 UP-Md12 banch

0460001 3 1 04601010.0 2.106 121.7351250.0 90.02.106 1.0-5 .193

0000000

0460200 013 15.701146 596.745 0.939-3

0461101046010003 0470100040.0 O 1.01.0 0001000

"62101046010003 0501004 0.6 103 1.0 1.0 0001000

0463101 046010002 054010001 0.23707475 1.0 1.0 0001000

0461110 0.193 0.01.0 1.0

0462110 0.055 0.0 1.0 1.0

0463110 0.040 0.01.0 1.0

0461201 47.2n 0.0 0.0

0462201 2373.40.0 0.0

0463201 .100.15 0.0 0.0

* Componen No 47

*Upeplevalm

* Middle Vohume for Loop 3

0470000 UP.M143 1eaac 0470001 3 1

04701010.0 2.106 1.81735125 0.0 90.0 2.106 1.0.5 0.193

O00000

0470200 013 15.7010+6 UMS27 0.939-3

0471101 047010003 048010004 0.0 1.0 1.0 0001000

0472101 047010003 051010004 0.6269105 1.0 1.0 0001000

0473101 047010002054010001 0.23707475 1.0 1.00001000

0471110 0.193 0.01.0 1.0

0472110 0.055 0.0 1.0 1.0

0473110 0.040 0.0 1.0 1.0

0471201 21.774 0.0 0.0

0472201 2367.0 0.0 0.0

0473201 65.076 0.0 0.0

*Coaipooewt No 48 • Upp• p1em.

* Middle Volumfor Loop 4 0480000 UP-MdS brand

0480001 3 1

04801010.0 2.106 1.81735125 0.0 90.0 2.106 1.0.5 0.193

0000000

0480200013 13.701006 M3.9960.939-3

0481101048010003 0450100040.0 1.0 1.0 0001000

0482101 048010003 052010004 0.6268105 1.0 1.0 0001000

0483101 043010002 054010001 0.23707475 1.0 1.0 0001000

0481110 0.193 0.01.0 1.0

0482110 0.055 0.01.0 1.0

0483110 0.040 0.01.0 1.0

0481201-0.679390.0 0.0

0482201 2363.8 0.0 0.0

0483201 50.463 0.0 0.0

* 6.15 Upper Plem-

* Ouwer Vohmnes

SComponent No 4

* Upper pleumu OtOer Voume fr Loop I 0490000 UP-Oull branch

0490001 3 1

04901010.0 2.106 13263620.0 90.02.106 1.0-50.55 000000

0490200013 I2A90746 590.007"0.939-3

0491101049010003 00010004 0.0 1.0 1.0 0001000

0492101049010002 054010001 0.0079922 1.0 1.0 0001000

0493101 049010004 061010004 1.7605595 0.2 0.2 0001000

0491110 0.550 0.01.0 1.0

0492110 0.006 0.021.0 1.0

0493110 0.180 0.01.0 1.0

0491201 31.391 0.0 0.0

0492201-27.1490.0 0.0

0493201 4497.8 0.0 0.0

" Component No 50

" Upperplecum:

" Outr Volume for Loop 2

0500000 UP.OuM2 branch

050000 3 1

0500102 0.0 2.106 1.6362 0.0 90.02.106 1.0.50.55

00D000

0500200013 15.690746 586.7290.939-3

05011010500100030510100040.01.01.0 0001000

0502101 050010002 054010001 0.0079922 1.0 1.0 0001000

0503101 050010004062010004 1.7685595 0.2 0.2 0001000

0501110 0.550 0.01.0 1.0

0502110 0.006 0.0 1.0 1.0

0503110 0.180 0.0 1.0 1.0

0501201-3.76440.0 0.0

0502201.27A40 0.0 0.0

0503201 4584.3 0.0 0.0

* Component No 31 * Upper plenum

*Otter Volume: lnrLoop 3

0510000 UP-OuDl branch 0510001 3 1

05101010.0 2.106 1.5263620.0 90.02.106 1.0.50.55

0000000

0510200 013 15.690746 588.2940.939-3

05111010510100030520100040.01.01.0 0001000

0512101051010002 050100010.0079M2 1.0 1.0 0001000

0513101051010004 063010004 1.7685595 0.2 0.2 0001000

0511110 0.550 0.0 1.0 1.0

0512110 0.006 0.0 1.0 1.0

0513110 0.180 0.0 1.0 1.0

0511201-33.90400 0.0

0512201-27.2600.0 0.0

0513201 4581.3 0.0 0.0

• Comonent No 52

" upper pi-=

" Otter Volume Ibr Loop 4 0520000 UP.,O14 branch

0520001 3 2 05201010.0 2.106 1.526362 0.0 90.02.106 1.0.5 0.55

0000000

0520200 013 13.6907+6 588.995 0.939-3

0521101052010003 049010004 0.0 1.0 1.0 0001000

0522101 052010002 054010001 0.0079922 1.0 1.0 0002000

0523101052010004 064010004 1.7685595 0.20.2 0001000

0521110 0.550 0.0 1.0 1.0

0522110 0.006 0.0 1.0 1.0

0523110 0.180 0.0 1.0 1.0

0521201-6.78M20.0 0.0

0522201 -27.254 0.0

0523201 4513.50.0 0.0

& 616 Upper Hefat

*Lowm VOlum

*CnomonentNo 54 * Upper Head Loa Volume

0540000 UHK-ow bran

0540002I1

054101 0.0 1.592 11.25261 0.0 90.0 1.592 1.0-5 2.30

0540200 013 15.69M+6 589.2• 0.939-3

054110105,010002 056010001D21571224 1.0 1.0 0001000

0541110 0.140 0.0 1.0 1.0

05412010.00.0 0.0

' 6.17 Upper Iu&d:

* Top Volume

SCaimpon No 56

• Upper Head Top Vohime

0540000 Ma~p anglvot 05601010.0 1.0756.338612 0.0 90.0 1.075 1.0.53.3 0000000

0560200013 15.683846 5U.2490.939-3

• 6.18 Ial•otor Vensel Outle

• CoyoeocNo 6f

• RV Oute t Loop 1

0610000 RV-O•II branch

0610001 2 1

06101010.0 1.240 0.93954175 0.0 90.0 1.24 1.0.50.348 0000M0

0610200013 15.74446 589.5280.939-3

0611101 061010003 0620200040.0 1.0 1.0 0001000

0612101061010003 1000100010.5674500.61 0.610001000

0611110 0.348 0.01.0 1.0

0612110 0.1500.01.0 1.0

0611201203.86 0.0 0.0

0612201 4253.6 0.0 0.0

* Component No 62 •V Oulet o Loop 2 0620000 RV-OuM2 brancd

0620001 2 1

0620101 0.0 2•240 0.93954173 0.0 90.0 1.24 1.0.50.348

0000M

0620200013 25.08974'6 $86.458 0.939-3

0621102 062010003 063010004 0.0 1.0 1.0 0001000

0622101 062010004 200010002 0.567450 0.61 0.61 0001000

0621110 0.348 0.01.0 1.0

0622110 0.850 0.0 1.0 1.0

0621202 60.874 0.0 0.0

06222014800.4 0.0 0.0

SComponent No 63

RV Outlet Io Loop 3

O6300 V-Ou brand 0630001 2 1 0630101 0.0 1.240 0.93954175 0.0 90.0 1.24 1.05 0.348

00000

0630200013 15.6897+6 587.8760.939-3

0631101 0630100030640100040.0 1.0 1.0 0001000

0632101063010004 300010001 0.567450 0.61 0.61 0001000

0631110 0.34" 0.0.0 1.0

0632110 0.150 0.0 1.0 1.0

0631201-177.180.0 0.0

0632201 425 0.0 0.0

C o.mnponent No 64

•V Outit so Loop 4 0640000 RV-OuI4 branch

0640001 2 1 06401010.0 1.240 0.939541750.0 90.0 1.24 1.0-50.348

00¢00<

0640200013 15.689746 588.5680939-3

0641101064010003 061010004 0.0 1.0 1.0 0001000

0642101064010004400010001 0.567450 0.61 0.61 0001000

0641110 0.34 0.0 1.0 1.0

0642110 0.850 0.0 1.0 1.0 0641201-1 25.2 0.0 0.0

0642201 4524.8 0.0 0.0

VI. Loops (14ima-M Side)

* 7.1.1 Loop 1: Ht Icg

Somponent No 100

* Hot Leg of loopt of RV outlet to 0ite valve

10001000 h1-¥1 pipe 20000014

1000101 0.56745 4

1000201 0.56745 3

1000301 1.49 1

1000302 1.8 4

1000401 0.0 4

1000601 0.0 4

2000801 1.0-5 0.804

1000901 0.0 0.0 3

10010010000000 4

20012010001000 3

1001201013 15.623946 S9.490 0.0 0.0 0.0 I

1001202 013 15.623246 S89.487 0.0 0.0 0.0 2

1001203 013 13.6225+6 S89.497 0.00.00.0 3

1001204013 15.6217+6 S89.446 0.0 0.00.0 4

1001300 2

1001301 4253.60.0 0.0 3

1001401 0.50 0.0 1.0 1.03

1002001 0.939-3 4

* Compoent No 101

* Loop 1: HoRt le Cre Valve

1010000 hbll-va &lun

1020101 100040002 102010001 0.3117 0.10.10001000

1010201 14253.6 0.0 0.

* Component No 102

-HotLcgoftoopl ofMGVt*SGI hlmt

2020000 hI2-1pi pipe 1020001 3

1020101 0.56745 3

1020201 0.56745 2

1020301 1.282

1020302 1.052 2

1020303 1.252 3

1020401 0.0 3

1020601 0.0 1

1020602 45.0 2

1020603 45.0 3

1020701 0.0 1

1020702 0.67 2

1020703 0.87 3

1020801 1.0-6 0.8503

1020901 0.0 0.0 1

1020902 0.07 0.07 2

102100100000003

102110100010002

1021201013 15.6077+6 589.478 0.0 0.0 0.0 1

1021202 013 15.60506 589.476 0.0 0.0 0.0 2

1021203 013 15.5966+6 589.471 0.0 0.0 0.0 3

1021300 1

1021301 4253.60.0 0.0 2

1021401 0.850 0.0 1.0 1.02

10220010.939-33

*7.1.2 SOL: He Collector

* ComonentNo I10

* F0l Har Collector Inlet Volume

2100000 SOI-Hcin randh

1100001 2 i

1100101 0.54 0.670 0.0 0.0 90.0 0.670 1.0-5 0.834 000000

1100200013 15-5426+6 589.4420.939-3

1101101 i02030002 1100100010.0 .02521.02520001000

1102101 110010002 1110100010.00.000 0.00000001000

1101110 0.850 0.01.0 1.0

1102110 0.834 0.0 1.0 1.0

1101201 4253.6 0.0 0.0

1102201 423.6 0.0 0.0

" Componen No I I1

" 5G2 Hot CollectorTube conection Lvel I

2I 10000 SO1-Hell brn

2220001 2 1

2220201 0.5460.445 0.00.090.0 0.445 . 0.5.34 0000000

1110200013 15.5407+6 589.4410.939-3

2111101 1110100021120100010.0 0.00.0 0001000

11121012111010003 1210100010.0 0.00.0 0001100

1112110 0.8,34 0.01.0 1.0

1112110 0.013 0.0 1.0 1.0

1111201 3848.7 0.0 0.0

1112201 404.94 0.0 0.0

o Comiponen No 112

* Sal Hot CollectorTubeeonocaion level2

I220000 SGI-HcI2 brandh

2120001 2 1

1120101 0.460.446 0.00.090.0 0.446 2.0.50.8 30000000

1120200013 25.546746 589.4440.939-3

D-9
1121101 112010002 113010001 0.0 0.0 0.0 0001000

1122101 112010003 1220100010.0 0.0 0.0 0001100

1121110 0.334 0.01.0 1.0

1122110 0.013 0.0 .0 1.0

1121201 31413 0.0 0.0

1122201 707.19 0.0 0.0

. Componem No 113

SSGI Ho Collector Tube cooection level 3

1130000SO1..Uc hmanod,.

1130001 2 I

1130101 0.546 0.446 0.00.090.0 0.446 1.050.334 0000000

1130200013 1"564#6 589.4490.939-3

1131101 11301000 114010001 0.0 0.00.0 0001000

1132101 113010003 1230100010.0 0.00.0 0001100

1131110 0.834 0.0 1.0 1.0

1132110 0.013 0.0 1.0 1.0

1131201 2060.4 0.0 0.0

11322011081.1 0.0 0.0

" Coimponent No 114

" SGI Hoe CollectorTube conectioc leveld4

1140000 SG.IHcl4 brandc

1140001 2 1

1140101 0.5460.464 0.00.0 90.0 0.464 1.05 0.834 000000

1140200013 15.5046 59•.4530.939-3

1141101 114010002 1150100010.0 0.00.00001000

1142101 114010003 124010001 0.0 0.0 0.0 0001100

1141110 0.834 0.01.0 1.0

1142110 0.013 0.01.0 1.0 1141201 942.55 0.0 0.0

1142201 1117.9 0.0 0.0

• Component mNo 1S

* SOl Hot ColzlorTube con:ecton level

150000 SGI-HIcLS branch

1150001 2 1

1150101 0.5460.464 0.00.090.0 0.464 1.0-.50.834 0000000

1150200013 15.5690.6 519.4540.939-3

1151101 11501002 1160100010.0 0.00.0 0001000

1152101 115010003 1250100010.0 000.0 0001100

1151110 0.834 0.01.0 1.0

1152110 0.013 0.0 1.0 1.0

1151201 0.0 0.0 0.0

1152201 942.54 0.0 0.0

: Component No 116

* Sol Hoto Collector Top

1160000 SGI.Hct pipe

11600012

11601010.546 1

11601020.0 2

1160201 0.546 1

1160301 0.485 1

1160302 1.552

1160401 0.0 1

1160402 0.50 2

1160601 90.02

1160801 1.0.5 0.334 I

11608M 1.0.5 0.02

1160901 0.0 0.0 1

1161001 00000002

1161101 0001000 1

1161201 013 15.5668.5 3-533. 0.00 0.0 1

1161202 013 15.359846582.9590.00.0 0.02

1161300 I

1161301 0.0 0.0 0.0 I

1161401 0.34 0.01.01.01

1162001 0.939-3 2

• 7.1.3 SOl: Tube Bundles

* Componem No 121

0 SGI Tube Bunde Level I

* 10ISTubes;LIO.61 m

1210000 SGI.Ibil pipe

1210001 5

1210101 0.13:512 5

1210301 2.122 5

1210401 0.0 5

1210601 0.0 5

1210801 4.0.6 0.013 5

1210901 0.0 0.04

1211001000005O 3

1211101 00010004

1211201 013 1.5.234+6 50.4060.00.0 0.01

1211202 013 15"066.+65732300.00.0 0.02

1211203 013 15.4900#6 567.675 0.0 0.0 0.0 3

1211204 013 15.47366.563.- "0.00.0 0.04

1211205 013 15.45746 .560.022 0.0 0.0 0.0 5

12113001

1211301 404.94 0.0 0.04

1211401 0.013 0.01.01.04

12120010.939-3 5

SCoxnpoom No 122

SO[ Tube Bundle Level 2

1 "798TubaL- 10.76

1220000 SOi-Tbh2 pipe

12200015

1220101 0.23865 5

1220301 2.152 5

1220401 0.0 5

1220601 0.0 5

1220301 4.0-6 0.013 5

1220901 0.0 0.04

1221001000000 05

122110100010004

1221201 013 15.5311+6530.08700.0`0 0.0 1

1221202 013 15.514446572.7360.00.0 0.02

1221203 013 15.4930+6567.1170.00.0 0.03

1221204 013 15.48184562.3130.00.0 0.04

1221205 013 15.4657+6559.543"000.0 0.05

12213001

1221301 707.19 0.0 0.04

1221401 0.013 0.0 1.0 1.04

1222001 0.939-3 5

" Comiponent NO 12 * SG! Tube Bundle Level 3

S2U4 Tubes; L - 11.04 m 1230000 SOI-Th1 pipe

1230001.5

1230101 0.32 35

1230301 2.203 5

1230401 0.0 S

1230601 0.0 5

12308014.06 0013 5

1230901 0.0 0.04

12310010000000 5

123110100010004

1231201 013 15.5417+6579.4610.00.0 0.0 1

1231202 013 !5.526146 571.795 0.0 0.0 0.0 2

1231203 013 15.1034 M656030 0.0 0.0 0.03

1231204 013 15.4956"6561.7360.00.0 0.04

1231205 013 15.480646 50.514 0.00.0 0.05

12313001

1231301 101.1 0.0 0.04

1231401 0.013 0.0 1.0 1.04

1232001 0.939-3 5

" Componcet No 124

" Sal Tube Bundle Level 4 • 2932TubesL.11.M2m

1240000 SI-'bl4 pipe

1240001D5

1240101 0.31917 5

1240301 2.25 5

1240401 0.0

1240601 0.0 5

12408014.0-6 0.013 5

1240901 0.0 0.04

1241001 0000000 5

1241101 00010004

1241201 013 15.50446 579.409 0.0 0.0 0.0 1

1241202 013 15.5340+6.571.71600.0.0 0.02

1241203 013 15.51784M55.9330.00.0 0.03

1241204 013 15.5019466561.6440.00.0 0.04

1241205 013 15.4861+6 558.426 0.0 0.0 0.0 5

12413001

1241301 1117.90.0 0.04

1241401 0.013 001.0 1.04

1242001 0.939-3 5

SCoponentNo 123

S 501 Tube Bundle Level 5

S2368 Tubes; L - 1125 m 125 SOI-TbS pipe

1250001 5

12501010.31431 S

1250301 2.255

1250401 0.0 5

1250601 0.0 5

125001 4.0.6 0.013 5

1250901 0.0 0.04

125100100000005

1251101 00010004

1251201 013 15.552946 579.881 0.0 0.0 0.0 1

1251202 013 1.-5350466572.4180.00.0 0.02

1251203 013 15.517446 566.747 0.00.0 0.03

1251204 013 153000.562.4430.00.0 0.04

1251205 013 15.48n346559.1960.0.0 0.05

1251300 1

1251301 942354 0.0 0.04

1251401 0.013 0.01.01.04

1252001 0.939-3 5

7.1.4 Sal: Cold Collector

• Component No 130

* SGt Cold Collector Outlet Volume

1300000 SG1-Ccou branch

1300001 2 1

1300101 03460.670 0.00.0 -90.0-0.670 1.0-50.334 0000000

1300200 013 15.450646 558.945 0.939-3

1301101 131010002 130010001 0.0 0.0 0.0 0002000

1302101 13001000 140010001 0.0 0.0 0.00001100

1301110 0.14 0.0 1.0 1.0

1302110 0.50 0.0 1.0 1.0

1301201 4253.6 0.0 0.0

1302201 4253.6 0.0 0.0

D-1 0

" ComponenNo 131

" SGI Cold Collector Tube coccejon level I

1310000 Sal-CAll branch

1310001 2 I

1310101 0346 0.445 0.00.0 -90.0.0.445 1.0.5 0.34 0000000

1310200 013 15A52346 558.945 0.939-3

1311101 132010002 1310100010.0 0.0 0.00001000

1312101 121050002131010003 0.0 0.0 0.00001100

1311110 0.34 0.0 1.0 1.0

1312110 0.013 0.0 1.0 1.0

1311201343L. 0.0 0.0

1312201404.94 0.0 0.0

SCoponent No 132 • SOl Cold CollectorTUbe coneeuim level2

1320000 SOI-=C2 branch

1320001 2 I

1320101 046 0.446 0.0 0.0 .90.0.-0446 1.0-5 0.34 0000000

1320200 013 15.459446 5S333 0.939-3

1321101 133010002 132010001 0.0 0.0 0.00001000

1322201 12200002 132010003 0.000 0.0 0001100

1321110 0A4 0.01.0 1.0

1322110 0.013 0.0 1.0 .0

1321201 3141.3 0.0 0.0

1322201 707.18 0.0 0.0

• Compoenit No 133 • Sal ColdCollectorTubeconectin levd3

1330000 SGI-Cc.3 brand

1330001 2 i 1330101 0.546 0.446 0.00.0 -90.0-0.446 1.0-500.134 0000000

1330200013 15.4637+6 558.6790.939-3

1331101 134010002 133010001 0.0 0`0 0.00001000

1332101 123050002 133010003 0.0 0.0 0.00002100

1331110 0.334 0.0 1.0 1.0

1332110 0.013 0.0 1.0 1.0

13312012060.4 0.0 0.0

13322011031.1 0.0 0.0

• Component No 134 * Sal Cold Collector Tube conecetle level 4

1340OOOSOI.l4 branch

1340001 2 1

13401010.5460.464 0.00.0 .90.0-0.464 1.0.5 0.334 0000000

1340200013 15.474146 553.7700.939-3

1341101 135010002 134010001 0.0 0.0 0.0 0001000

1342101 12405000 134010003 0.0 0.0 0.0 0001100

1341110 0.834.001.0 1.0

1342110 0.013 0.01.0 1.0

1341201 942.54 0.0 0.0

13422011117.9 0.0 0.0

• Coone,•t No 135 • Sol Cowl Collector Tube conection level 5

1350000 SGI-.Cc$ branch

1350001 2 1 1350101 0.5460.464 0.00.0 -90.0-0.464 1.0-50.334 0000000

1350200013 15.4739%4 559.1280.939.3

1351101 136010001 135010001 0.0 0.0 0.0 0001000

1352101 1250500012135010003 0.0 0.0 0.0 0001100

1351110 0.334 0.01.0 1.0

1352110 0.013 0.0 1.0 1.0

1351201 0.0 0.00.0

1352201 942.540.0 0.0

• Compone•t No 136

SOI Cold Collector Top 1360000 SOI-Ce pipe

13600012

1360101 046 1

1360102 0.0 2 1360201 0346 1

1360301 0.485 I

1360302 1M52

1360401 0.0 1

1360402 05M 2

1360601 90.0 2

13608011.0.5 0.334 I

1360802 1.05 0.02

1360901 0.0 0.0 1

1361001 0000000 2

13611020001000 I 1361201 013 15.470446 557.475 0.0 0.0 0.0 1

1361202 013 15.462856557.2430.00.0 0.02

1361300 I

1361301 0.0 0.0 0.0 1

1361401 0.834 0.0 1.0 1.0 I

1362001 0.939-3 2

*7. 1.5 Loop I ColdLeS

* Compoocne No 140

Seal Loop ofSl ouold to l,•vl lat

1400000 sl-IpI pipe

1400001 9 1400101 0.56745 9

1400301 0.3 1

1400302 1.2 2 1400303 1.052 4

1400304 1.516

1400305 1.052 9
1400306 1.74 9

1400401 0.0 9

14006] .90.0 2

1400602-45.0 4

1400603 0.0 6

1400604 45.0 8

1400605 90.0 9

1400701.0.8 1

1400702 -1.22

1400703 -0.67 4

1400704 0.06

1400705 0.67 8

1400706 1.74 9

1400801 1.0-6 0.850 9

1400901 0.0 0.02

1400902 0.070.07 3 *R/d 1J8.90deg.2k0t26

1400903 0.0 0.06

1400904 0.070.07 7 0Rd I.58. 90 degs Ik-0.26

1400905 0. 0.0 8

1401001 0000000 9

1401101 OOO100 8

1401201 013 15.458746 558.9470.00.0 0.0 2

1401202 013 15.4658.65S8.9490.00.0 0.02

1401203 013 15.472446 5$8.950 0.00.0 0.03

1401204 013 15.474546558.95• 0.00.0 0.04

1401205 013 15A766'6 $58.950 0.0 0.0 0.05

1401206 013 15.476146 338.950 0.0 0.0 0.06

1401207 013 15.4733+6 558.948 0.00.0 0.07

1401208 013 15.46546 558.946 0.0 0.0 0.0 8

1401209 013 15.4561W6558.9420.00.0 0.09

14013001

1401301 4253.60.0 0.0 8

1401401 0.850 0.0 1.0 1.08

1402002 0.939-3 9

•7.1 A MWinCultioe Pomw I

• PUMP WWER 1000 (95M): * Volume - 3.0 cab.i

• RaiV Speed - 104.720 p/sec

Actual speed - 104.196 p/sec

* Flow =5.888m3/soe

SIead. 84.0O0m

* Torque = 47500.0 nhm

M Jdom.iL. = 7500.0 ks*mzm

SDenmsy - 747 kg/M3

* Celpoaee aNo 142 * MCPI

1410000 MP#I pump

1410101 0.0 5.287 3.0 0.0 0&00.0 0000000

2410108 140090002 0.0 0.0 0.0 00O0100

1410109 142010001 0.0 0.0 0.0 0000100

1410200013 15.7336*6 559.1040.93903

1410201 1 4253.6 0.0 0.0

1410202 1 4253.6 0.0 0.0

1410301 0 -1.3-106120

1410302 104.72 1.0 5.694 84.0 47511. 7500. 47.0 0.0 0.00.0

0.0 0.0

7.1.6.1 Table pump velociy

1416100 OCek'va" 141

1416101 0.0 0.0

1416102 500.0 500.0

• 7.1.6.2 Pump Homologous Curves

* Single fhase Head Curves

HeadCavefno I HAN (Normnl)

1411100 1 1

1411101 0.0 1.826

1411102 0.04 1.739

1411103 0.11 I.562

1411104 0.20 1.423

1411105 0.3 1.315

1411106 0.42 1.239

1411107 0.5 1.228

1411108 0.6 1.206

1411109 0.72 1.184

1411110 0.82 1.141

1411111 0.91 1.076

1411112 1.0 1.00

: Torque Curve so I BAN (Nomnl)

1411200 21

1411201 0.0 1.045

1411202 0.271 0.796

1411203 0.3 0.82

1412I04 . 0.816

1411205 0.5 0.82

1411206 0.82 0.95

1411207 1.001.00

0 Head Curve so 2 HVN (Pmp)

1411300 12

1411301 0.0-1.227

1411302 0.221-0.909

1411303 0.42 .0.5

1411304 0.620.0

1411305 0.84 0.5

1411306 0.904 0.658

1411307 1.0 1.00

* Torque Curve so 2 BVN (Pump)

1411400 22

1411401 0.0-1.148

14114020.5 0.0

1411403 1.0 1.0

* Head Caveao 3 lEAD (Ews

1411500 13

1411501 .1.0 419

1411502 MO.52.95

1411503 .0.39 2.695

1411504 .0.29 2.434

1411505 .0.1812.173

1411506 -0.12.0

1411507 0.000 1.826

* Torque Co bve 3 BAD (&oMy)

1411600 23

1411601 -.. 03.43

1411602 .0.89 2.978

1411603 40.79 2.609

1411604 .058 2.0

1411605 -0.51.826

1411606 .0.19 1.239

1411607 .0.11.13

1411608 0.00 1.045

* HWea Curve o 414VD (Dissipation)

1411700 14

1411701 -1.0 4.272

1411702 -0.769 3.272

1411703 -0.576 2-W

141704-0.384 2.0

1411705-0.192 1.458

1411706 0.0O0 1.272

* TOWqu Curve ao 4 BYD (Dissipation) 1411800 24

1411201 -.. 0 3.272

1411802 -0.769 2.453

1411803 -0.576 2.0

1411804 -0.34 1.636

1411805 40.192 1.272

14118060.OO 1.09

* Head Curve so 5 HAT (Noral)

1411900 15

1411901 0.0 0.42

1411902 0.0452 0.426

1411903 0.0905 0.420

14119040.181 0.444

1411905 0.271 0.480

1411906 0.362 0.504

14119070.4,52 0.52

141I908 0.543 0.600

1411909 0.633 0.696

14119100.724 0.828

1411911 0.814 0.984

1411912 0.905 1.188

1411913 1.000 1.360

* Torque Curve so 5 BAT (Normal)

1412000 25

1412001 0.0-0.704

14120020.0452 4.684

14120030.134-0.684

1412004 0.1814-0.612

1412005 0.271-0.449

1412006 0.362 -0.255

14120070.45240.122

1412008 0.543 40.0306

14120090.633 0.0816

14120100.724 0.224

14120110.814 0.388

1412012 0.905 0.592

1412013 0.995 0.776

1412014 1.00 0.790

* Read Cav no 6 IIVT (Turbine)

1412100 1 6

1412101 0.0 2.024

14121020.221 1.731

1412103 0.442 1.525

1412104 0.663 1.408

14121050.884 1.379

1412106 1.0 1.36

" Torque Cave no 6 BVT (Turbine)

141220O 2 6

1412201 0.0 1.547

1412202 0.221 2.397

1412203 0.442 1.197

1412204 0.663 1.048

1412205 0.884 0.848

1412206 1.000 0.790

* Head Camv so07 MA (Revrs) 1412300 1 7

1412301 -1.0 -3.12

1412302 -0.414 .2.016

1412303 -0.724 -I.608

1412304 -0.633 -1.296

1412305 -0.543 40.996

1412306 -0.452 4.672

1412307 4.362 4.360

1412308 .271 40.072

1412309 -0.181 0.216

1412310 -0.0905 0.360

1412311 -0.0452 0.408

1412312 0.0•0 0.420 * Torque Curve m 7 BAR (Revere)

1412400 27

1412401 -1.0 -4.34

1412402 40.814 .3.142

1412403 .0.724 -2.724

1412404 09.543 -2.286

1412405 ,0.452 -1.939

1412406 .0.362 -1-52

1412407 .0.271 .1.286

1412408 -0.181 -..000

1412409 -0.0905 -0.796

14124100.000 -0.704

* Head Curve no 8 H'VR (Pump)

1412500 1 8

141250D -1.0 -3.12

1412502 -. 8842.9A 2

1412503 0.663-2.757

1412504 40.442.2.435

141250• 0.221 ..053

1412506 0.000 -..584

* Torque Curve 3o8 BVI (Pump)

1412600'28

1412601 -1.0-4.34

1412602 -0.884 -3.941

1412603 -0.663 -.3.218

1412604 40.442-2.495

1412605 -0.221-1.821

1412606 0.000 -1.148

7.1.7 Loop I Cold LegofMCP toRV

* Componeat No 142

* Colm teg ofmC70i to Cold we MOV

1420000e1-ipl pipe

1420001 2

1420101 0.56745 2

1420301 2.1075 2

1420401 0.0 2

1420601 0.0 2

1420701 0.02

1420801 1.0-5 0.852

1420901 0.0 0.0 I

14210010000000 2

14211010001000•1

1421201 013 16.0174+6559.201 0.00.0 0.0 1

1412202 013 16.016663559.201 0.0 0.0 0.02

1421300 1

1421301 4253.60.0 0.0 2

1421401 0.850 0.0 1.0 1.0 1

1422002 0.939-3 2

C omponen No 143 * Loop 1: CoWd leg CAe Valve

1430o00 e1..m•p m1jun

1430101 142020002144010001 0.3117 0.1 0.1 0001000

1430201 1,4253.6 0.0 0.

• Componm No 144 • Cold Ikg f Cold leg MOV to RV

144000 eO.4. pipe 1440001 11 14401010.56745 11

1440301 1.5 I

1440302 1.052 2

1440303 2.252 4

1440304 1.052 S 1440305 1.52 6

1440306 2.5 7 1440307 4.5 8

1440308 3.5 9

1440309 IM 11

1440401 0.0 11

14406010.0 2

1440602.45.0 5

1440603 0.0 11

144070I 0.0 1

14407024.67 2

14407034.87 4

1440704-0.67 5

1440705 0.0 II

1440801 1.0-6 0.850 11

1440901 0.0 0.0 1

1440902 0.070.07 2

14409 0.00.03

1440904 0.07 0.07 4

1440905 0.0 0.0 10

14410010000000 11

1441101 0001000 10

1441201 013 16.0037-6559.1960.00.0 0.01

1441202 013 16.0058+6 559.196 0.0 0.0 0.02

1441203 013 16.0085+6 559.195 0.0 0.0 0.0 3

1441204 013 16.0146+6 559.198 0.0 0.0 0.04

1441205 013 16.017346 559.198 0.0 0.0 0.0 5

1441206 013 16.01946 559.198 0.0 0.0 0.0 6

1441207 013 16.028466559.1960.00.0 0.07

1441208 013 16.01789+6 59.193 0.0 0.0 0.08

1441209 013 16.0166+6559.191 0.0 0.0 0.09

1441210 013 16.015946559.1890.00.0 0.0 10

1441211 013 16.01%66 S59.189 0.0 0.0 0.0 11

14413001

D-11
1441301 4253.6 0.0 0.0 10

1441401 0.150 0 1.0 1.0 10

1442001 0.939-3 11

*7.2 Loop I: Hot leg

SComponnt No 200

*Hot Leg of loop2 ofRV nutlet to gate valve

2000000 h11.1p2 pipe

200001 4

2000101 0.56745 4

2000201 0.56745 3

2000301 1.491

2000302 1.8 4

2000401 0.0 4

2000601 0.0 4

20008011 .0-5 0.8504

2000901 0.0 0.0 3

2001001 0000000 4

2001103 00010003

2001201 013 15.606746586A.160.00.0 0.0

2001202 013 15.605946586.413 0.00.0 0.02

2001203 013 15.6049+6 586.4140.00.0 0.03

2001204 013 15.6040+6586.4140.00.0 0.04

20013001

2001301 4300.40.0 0.0 3

2001401 0.850 0.0 1.0 1.0 3

20020010.939-3 4

- Compont No 201

* Loop 2: Hot leg Gat Valve

2010000 hO.amv msjgu

2010101 200040002 202010001 0.3117 0.02 0.02 0001000

2010201 14800.3 0.0 0.

" Compooent No 202

" lHt Leg ofoop? ofMGV to SG2 Iola

200000 blo-p pe

20200013

2020101 0.56745 3

2020201 O.56745 2

2020301 1.28 1

2020302 1.052 2

2020303 1.252 3

2020401 0.0 3

202060 0.0 1

2020602 45.0 2

2020603 45.0 3

2020701 0.0 1

20207M 0.67 2

202003 0.873

2020801 1.0-6 0.850 3

2020901 0.0 0.0 1

20209020.0 0.0 2 0 R/d 1.58. 90 des - k 0.26

2021001 00000003

2=1101 00010002

2021201 013 15.59990.586.412 0.0 0.0 0.0 1

2021202 013 15.5972.65M6.411 0.00.0 0.02

2021203 013 15.59144.6584080.00.0 0.03

2021300 1

202331 4800.3 0.0 0.0 2

2021401 0.850 0.0 1.0 1.02

2022001 0.939-3 3

*71.2.2502 Hot Collecor

• CompooeoNo 210

SSO2 ot Collemor la Volum

2100000 S2-l-do bm4

2100001 2 I

2100101 0.5460.670 0.00.090.0 0.670 .0..5 0.134 0000000

2100200 013 15352+6586389 0.939-3

2101101 202030002210010O010.0 0.47640.47640001000

2102101 210010002211010001 0.0 0.00000.00000001000

2101110 0.850 0.0 1.0 1.0

2102110 0.834 0.0 1.0 1.0

2101201 48003 0.0 0.0

2102201 48003 0.0 0.0

SCoznpoouo No 211

* SG2 HM Collector Tube conteio, level I

2110000 SC241 brandb

211000D 21

2110101 0.546 0.445 0.0 0.0 90.0 0.445 1.0-5 0.834 0OOOOO

2110200013 15.537+6 586.3890.939-3

2111101 211010002212701000 0.0 0.0 0.00001000

2112101 21101000M 221010001 0.0 0.0 0.00001100

2111110 0.834 0.0 1.0 1.0

2112110 0.013 0.0 1.0 1.0

2111201 4342.1 0.0 0.0

2112201458.25 0.0 &0

C~* CoopcnmNo21W * SG2 Hot Cleac Tube concedom levd 2

2120000 SG2-H.c brncw

2120001 2 1

21201010.5460.446 0.00.090.0 0.446 1.0.50.834 O000OOO

2120200013 15.5621.5 6 930.939-3

2121101 212010002 213010001 0.0 0.0 0.0 0001000

2122101 212010003 222010001 0.0 0.0 0001100

2121110 0.134 0.0 1.0 1.0

2122110 0.013 0.0 1.0 1.0

2121201 3542.7 0.0 0.0

2122201 799.37 0.0 0.0

• Componem No 213

" S02 Hot Collector Tube coetlia leveld 3

2130000 S02.-1c1 kmwob

2130001 2 1

21301010.5+40.446 0.00,090.0 0.446 1.0-5 0.834 O00000

2130200013 15.575146 586.3990.939-3

2131101 213010002 214010001 0.0 0.0 0.00001000

2132103 2130100037223010001 0.0 0.0 0.00001100

2131110 0.A34 0.01.0 1.0

2132110 0.013 0.0 1.0 1.0

2131201 2322.A 0.0 0.0

2132201 1220.3 0.0 0.0

" Coozpaccat No 214 " S02 Hot Collctr Tube coneccton level 4

2140000 S0241c14 branch

2140001 2 1

2140101 0.5 0.464 0.00.090.0 0.464 1.0.5 0.834 00000OO

2140200103 15-W846 586.4050.939-3

2141101 214010002215010001 0.0 0.0 0.00001000

2142101 214010003 224010001 0.00.00.001100

2141110 0.834 0.0 1.0 1.0

2142110 0.013 0.0 1.0 1.0

2141201 1062.3 0.0 0,0

2142201 12602 0.0 0.0

• ComnpooetNo 21l

* S02 ot Collector Tube €ooooctm level 5

2150000 SO 2-1lf b h

2150001 2 1

21501010.5460.464 0.00.090.0 0.464 1.0-50.834 0000

2150200013 15.3924.6 596.4070.939-3

2151101 215010002216010001 0.0 0.0 0.0001000

2152101 215010003.225010001 0.0 0.0 0.00001100

21;1110 0A34 0.0 1.0 1.0

2152110 0.013 0.0 1.0 3.0

21351201 0.0 0 0.0

2352201 3062.2 0.0 0.0

• Compoone No 216

" S02 HSot ColiectorTop

21600OO 502-lct pipe

2160001 2

21601010.546 1

2160120.0 2

2160203 0.546 1

2160301 0.485 1

2160302 1.552

2160401 0.0 1

2160402 0.505 2

2160601 90.0 2

2160801 1.0.5 0.234 I

21608 1.0.5 0.02

2160901 0.0 0.0 1

2163001 00000002

21611010001000 1

2161201 013 15.5904•6•5309050.00.0 0.0 1

2161202 013 15.5134+6 80.953 0.0 0.0 0.0 2

21613001

2161301 0.0 0.0 0.0 I

2161401 0.834 0.0 1.0 1.0 1

2162001 0.939-3 2

*7.23 S02: Tube Bundles

* Compoem No 221

* SG2Tube Bundle Level I

S101 L8TubeLw 10.61 m

221000 ,02-Tbll pipe

22100015

2210101 0.13512 5

2210301 2.122 5

2210401 0.0 5

22106010.0 5

2210801 4.0.6 0.013 5

2210901 0.0 0.04

2211001 O000005

2211101 00010004

2211201 013 15.5320'6 578.603 0.0 0.0 0.01

2211202 013 15.510746 52313 0.0 0.0 0.02

2211203 013 15.489746567•324 0.0 0.0 0.03

2211204 013 15.4689.+6563640.00.0 0.04

2211205 013 15.44.04 560.260 0.0 0.0 0.05

22113003

2211301 45824 0.0 0.04

2211401 0.013 0.0 1.0 1.04

22120010.939-3 5

* Co nmo No 222

S 502 Tube Bundl Level 2

• 1798Tubes;L- 10.76

222OOOO S2-T.2 pipe

2220001 5

2220101 0.23865 5

2220301 2.152 S

2220401 0.0 5

2220601 0.0 5

22208014.0.6 0.03 5

22209031 0. 0.04

2221001 00000005

222110100010004

2221201 013 15.425+6 578.2810.00.0 0.0 I

2221202 013 15= +14 571.8190.00.0 0.02

2221203 013 1-5.00765666.741 0.00.0 0.03

2223204 013 15.4801,6562.7720.00.0 0.04

2221205 013 15A590+659.70300.0.0 0.05

22213001

2221301 799.34 0.0 0.04

2221401 0.013 0.0 1.0 1.04

2222001 0.939-3 5

• Coupowat No 223

S 502 TuWe Bundle Level 3

* 2884 Tbes; L = 11.04 in

223000 ST.2-Tb13 pipe

2230001 5

2230101 0.3828 5

2230301 2.20 5

2230401 0.0 S

2230603 0.0 S

2230801 4.0.6 0.013 35

2230901 0.0 0.04

2231001 0000005

223110100010004

2231201 013 15.5367+6577.5800.00.0 0.01

2231202 013 13.5371+6M570.T30.00.0 0.02

2231203 013 15.5177+6565.4500.00.0 0.03

2231204 013 15.4986"6561.4590.00.0 0.04

2231205 013 15.479746 558.4010.00.0 0.05

22313001

2231301 1220.3 0.0 0.04

2231401 0.013 0.0 1.0 1.04

2232001 0.939-3 5

• Compocot No 224

* •02 Tube Bundle Level 4

S2932 Tubes L - 1I1. m

2240000 SG2-Tb14 pipe

2240001 5

2240101 0.38917 5

2240301 2.25 5

2240401 0.0 5

2240601 0.0 5

2240801 4.0.6 0.013 5

2240901 0.0 0.04

2241001 000020O 5

2241101 00010004

2241201 013 15684+6577.7240.00.0 0.01

2241202 033 15.547896570.9640.00.0 0.02

2241203 013 15.5275+6565.7300.00.0 0.03

2241204 013 15.5074+6561.755 0.00.0 0.04

2241205 013 15.4875"6 558.702 0.0 0.0 0.03

2241300 1

22413011260.10.0 0.04

2241401 0.013 0.0 1.0 1.04

2242001 0.939-3 5

* Compoonm No 225

* S02 Tube Bundle Level 5 • 2368Tube:L- 1125m

2250000 .02-IbIO pipe

22500015

22501010.31431 5

2250301 2.35

2250401 0.05

2250603 0.0 5

2250801 4.0.6 0.013 5

2250901 0.0 0.04

22510010000000 5

2251101 3000I004

2251201 013 15.5723+6 577.970 0.00.0 0.0 t

2253202 013 15-499.6 $571.327 0.0 0.0 0.0 2

2251203 013 155278+6 566.146 0.00.0 0.03

2251204 013 35.506046562.1660.00.0 0.04

2251205 013 15.4843+6559.0960.00.0 0.05

22513300

2251301 1062.30.0 0.04

2251403 0.013 0.0 1.0 1.04

2252003 0.939-3 5

* 74.2:S Cold Collector

SComponent No 230

S 502 Cold Collector Outlet Volhum

2300000 SG2-Conu branch

2300001 2 1

2300101 0.46 0.670 0.0 0.0 -90.0 -0.670 MS0-5 0.834 0000000

2300200 013 15.4386+6 559.0120.939-3

2301101 231010002 230010001 0.00.0 0.00001000

2302101 2300000224003003 0.00.0 0.00001100

2301110 0.134U 0.01.0 1.0

2302110 0.850 0.0 1.0 1.0

23012014900.3 0.0 0.0

230220149.00.3 0.0 0.0

" Compoocne No 231

" SG2 Cold Collctor Tube cooctaio level I

D-1 2
2310000 SG2-C.. I

2310001 2 1 2310101 0.5460.445 0.00.0 -90.0.-0.445 1.0-50.834 0000000

2310200013 15.4419.6 559.0140.939.3

2311101 232010002231010001 0.0 0.0 0.0 0001000

2312101 22105002 231010003 0.0 0.0 0.0 0001100

2311110 0.834 0.0 1.0 1.0

2312110 0.013 0.0 1.0 1.0

2311201 4342.2 0.0 0.0

2312201 453.2 0.0 0.0

* Component No 232 * SG2 Cold Collector Tube oectinc leve 2

2320000 SG2-CcW2 branch

2320001 2 1

2320101 0.546 0.446 0.0 0.0 .90.0.446 1.0-5 O.3 0000000

2320200 013 15.4519+6 55.36 0.939.3

2321101 233010002232010001 0.0 0.0 0.00001000

2322101 22205000232010003 0.0 0.0 0.00001100

2321110 0.834 0.0 1.0 1.0

2322110 0.013 0.0 1.0 1.0

2321201 3542.8 0.0 0.0

2322201 799.37 0.0 0.0

* Coamoant No 233

S62 Cold CollectorTLThe cooction level 3

2330000 S02-C brand

2330001 2 1

2330101 0.546 0.446 0.00.0 .90.040.446 1.0M50.834 G00000

2330200013 15.4646+6 558.707 0.939-3

2331101 234010002233010001 0.0 0.0 0.00001000

2332101 223050002233010003 0.0 0.0 0.00001100

2331110 0.134 0.0 1.0 1.0

2332110 0.013 0.0 1.0 1.0

2331201 2322.5 0.0 0.0

2332201 1220.3 0.0 0.0

* Coipontm No 234 • 62 Cold Collector T"ibe coection level 4

2340000 6S,2.Cl4 btnb

2340001 2 1

23401010.5460.464 0.00.0 -90.00.464 1.0-. 0.934 0000000

2340200 013 15.4724+6 558.375 0.9393

2341101 233010002234010001 0.0 0.0 0.00001000"

2342101 224050002234010003 0.0 0.0 0.00001100

2341110 0.334 0.0 1.0 1.0

2342110 0.013 0.0 1.0 1.0

2341201 1062.4 0.0 0.0

2342201 1260.1 0.0 0.0

- Comm, nntNo 235 1 S02 Cold Collector Tube econecion level 5

2350000 S02-Cel branc

2350001 2 1

2350101 0.56 0.464 0.0 0.0 .90.0-0.464 1.0.-0.834 000000

2350200013 15.4730+6 559.0380.939-3

2351101 236010001 23500M0I 0.0 0.0 0.00001000

2352101 225050002 235010003 0.0 0.0 0.00001100

2351110 0.34 0.0 1.0 1.0

2352110 0.013 0.0 1.0 1.0

2351201 0.0 0.0 0.0

2352201 1062.4 0.0 0.0

* C, qponcn No 236 • SG2 Cold CollectorTop

2360000D S2-Ca pipe

23600012

2360101 0.546 1

23601020.0 2

2360201 0.546 1

2360301 0.485 1

2360302 1.552

2360401 0.0 1

2360402 0.505 2

2360601 90.0 2

2360901 1.0.5 0.834 1

2360802 1.0-. 0.02

2360901 0.0 0.0 1

2361001 00000 2

23611010001000 1

2361201 013 I1.4695+6 57.2300.00.0 0.0 I

2361202 013 15.46196 557.625 0.0 0.0 0.02

23613001

2361301 0.0 0.0 0.0 1

2361401 0.334 0.0 1.0 1.0 1

2362001 0.939-3 2

* 7.2.5 Loop 2 Cold Leg

SCoqmlot, No 240

*Seat Loop of 602 Outlet to MCP2 Inler

2400000 .-Ip2 pipe

24000019

2400101 0.56745 9

2400301 0.8 I

2400302 1.2 2

2400303 1.052 4

2400304 1I5 6

24M0305 1.052 8

2400306 1.74 9

2400401 0.0 9

2400601 -90.0 2

240602 .45.0 4

2400603 0.0 6

2400604 45.0 3

2400605 90.0 9

2400701.0. 1

2400702M1.2 2

2400703.0.67 4

2400704 0.06

2400705 0.67 8

2400706 1.74 9

2400301 1.0.6 0.59

2400901 0.0 0.02

2400902 0.0 0.03 R/d- U.& 90d k - 0.26

2400903 0.0 0.06

2400904 0.0 0.07 Rd- l.59,90deg-Ika0.26

2400905 0.0 0.08

2401001 0000000 9

24011010001000 8

2401201 013 15.4474+6 559.014 0.0 0.0 0.0

2401202 013 15.454563559.015S0.0 0.0 0.02

2401203 013 15.461036559.010.00.0 003

2401204 013 15.4655+6 559.016 0.0 0.0 0.04

2401205 013 13.467+6 $559.0140.00.0 0.0 3

2401206 013 1S.4670'6559.0130.00.0 0.06

2401207 013 15.4640+6.559.011 0.0 0.0 0.07

2401208 013 1.5137. 559.00 0.0 0.0 0.0 3

2401209 013 5.44926 559.004 0.0 0.0 0.09

24013001

2401301 4300.60.0 0.0 8

2401401 0.1150 0.0 1.0 1.03

24020010.939-3 9

* 7.2.6 Mmo Cvlaicia Ptn 2

*ComonoeintNo 241 MCPO2

2410000 MCP#2 pump

2410101 0.0 5.•27 3.0 0.0 0.0 0.0 0000000

2410108 240090002 0.00.0 0.0 0000100

2410109 242010001 0.00.0 0.0 0000100

2410200013 15.7226+6 559.1440.939-3

2410201 I 4800.6 0.0 0.0

2410202 1 4800.6 0.0 0.0

2410301 141.1 -3 -10 613 0

2410302 104.72 1.06.425 54.0 47511. 7500. 747.0 0.00.00.0

0.00.0

7.2.6.1 Table pump velocity

2416100 Omatvar 241

2416101 0.0 0.0

2416102 500.0500.0

* 7Z7 Loop 2 CoWl Leg ofMCP 10 ItV

* Cemtpocm No 242

*Cold leg of MCP#2 to Cold kgs MOY

2420000 eII.1p2 pipe

24200012

2420101 0.56745 2

2420301 2.1075 2

2420401 0.0 2

2420601 0.0 2

242D701 0.02

2420,011.0.5 0.1502

2420901 0.0 0.0 !

24210010000000 2

2421101 0001000 I

2421201 013 16.0023+6 559.242 0.0 0.0 0.0 !

2421202 013 16.00146 559.2440.0 0.0 0.02

2421300 2

2421301 4300.5 0.0 0.0 1

2421401 0.350 0.0 1.0 1.0 1

24220010.939-3 2

• Componemt No 243

*Loop 2. Cold kg Gale Valve 2430000 eU.iP m$1jun

2430101 242020002 244010001 0.3117 0.02 0.02 0001000

2430201 14800. 0.0 0.

• Componen No 244

* Coald ga ofMVtonIV

2440000 el2.1p2 pipe 2440001 11

2440101 0.56745 I1

2440301 1.5 I

2440302 1.052 2

2440303 1.252 4

2440304 1.052 5

2440305 1.523 6

24403062.57

2440307 4.5 8

2440308 359

2440309 1.2 I

2440401 0.011

24406010.0 1

2440602-45.0 5

2440603 0.0 I1

2440701 U I

2440702 .67 2

244070340.37 4

2440704.0.67 5

2"0705 0.0 If

2440801 1.0-6 0.850 11

2440901 0.0 0.0 I

2440902 0.0 0.02

2440903 0.0 0.03

2440904 0.0 0.04

2440905 0.0 0.0 10

2441001 0000000 11

2441101 0001000 10

2441201 013 16.9974#6S59.2440.00.0 0.0 1

2441202 013 16.995+66559.243 0.00.0 0.02

2441203 013 16.0047+6 559.2470.00.0 0.03

2441204 013 16.0107+6 559.2510.00.0 0.04

2441205 013 16.0160+6559.2540.00.0 0.05

2441206 013 16.0106 559.255 0.0 0.0 0.06

2441207 013 16.0172+6 559.257 0.00.0 0.07

2441203 013 16.0159.6559.5790.00.0 0.03

2441209 013 16.0145+6 1559.2%60.00.0 0.09

2441210 013 16.0136+6 559.254 0.0 0.0 10

2441211 013 16.0131+6 559.2540.00.0 0.0 11

244130 i

2441301 4800.5 0.0 0.0 10

2441401 0.50 0.0 1.0 1.0 10

2442001 0.939-3 11

7.3 Ioop 3: Hotek

*Comipooent No 300 * Hot Let ofloop of RV outlet to gine valve

3000000 hIt-lp3 pipe

300001 4

3000101 0.56745 4

3000201 0.56745 3

3000301 1.49 I

3000302 1.34

3000401 0.0 4

3000601 0.0 4

3000801 1.0-5 0.8504

3000901 0.0 0.03

3001001 00000004

3001101 00010003

3001201 013 15.6030-6 537.33 0.0 0.0 0.0 1

3001202 013 15.6022+6 37.3270.00.0 0.02

3001203 013 15.6012+6 587.270.00.0 0.03

3001204 013 15.6003.+6587.8260.00.0 0.04

3001300 1

3001301 4092+.50.0 0.0 3

3001401 0.850 0.0 1.0 1.03

3002001 0.939-3 4

• Componen No 301

* Loop 3: Hot leg Gate Valve

3010000 blS-gv =gljun

3010101 30040002 302010001 0.3117 0.05 0.05 0002000

3010201 1 4892.5 0.0 0.

* Componem No 302

H Iot La of 2003 of0MGV to SG3 Inlet

3020000 b12-Ip3 pipe

3020001 3

3020101 0.56745 3

3020201 0.56745 2

3020301 1.23 i

3020302 1.052 2

3020303 1.252 3

3020401 0.0 3

30206010.0 1

3020602 45.0 2

3020603 45.0 3

30207010.0 1

30207020.67 2

3020703 0.873

3020801 1.0-6 0.8503

3020901 0.0 0.0 1

3020902 0.039 0.039 2 R1d 1.38.90deg40k 0.26

3021001 0000000 3

30211010001000 2

3021201 013 15.5906+657.321 0.00.0 0.0 1

3021202 013 15.5079-6357.8190.00.0 0.02

3021203 013 15.5901+6 587.815 0.0 0.0 0.0 3

3021300 1

3021301 4992750.0 0.0 2

3021401 0.0 0.01.0 1.02

302200 .939.3 3

* 7.3.2 SG3: Hot Collector

* Conioo No 310

S 03 Hot Collector inlet Volune

3100000 S3-Hcia branch

31001 2 I

3100101 0$60.670 0.00.090.0 0.670 1.0" 50.33 0000000

3100200 013 15.5544+6 537.3010.939-3

3101101 302030002310010001 0.0 0.271 0.271 0001000

3102101 310010002311010001 0.0 0.000 0.000 0001000

3101110 0.350 0.0 1.0 1.0

3102110 0.334 0.0 1.0 1.0

3101201 4392.5 0.0 0.0

D-13
L

3102201 4892.4 0.0 0.0

: Cona n NNo-31 I

SCU lotC4,olleorTube cocecuon Level I

3110000 SG3-Hell birnch

3110001 2 1

3110101 0-5,60.445 0.00.090.0 0.445 1.0-50.834 0000000

3110200013 IS.S304S6 587.8000.939-3

3111101 311010002312010001 0.00.00.0 0001000

3112101 311010003 321010001 0.00.00.0 0001100

3111110 0.834 0.01.0 1.0

3112110 0.013 0.0 1.0 1.0

31112014425.6 0.0 0.0

3112201466.87 0.0 0.0

* Caoomeot No 312

* SG3 Hot ColleatorTube oneeaim level 2

3120000 SG3-HcU branhA

3120001 2 1

3120101 0.5460.446 0.00.090.0 0.446 1.0-50.834 000000

3120200 013 15.56194+6 587.8050.939-3

3121101 312010002 313010001 0.00.0 0.0 0001000

3122101 312010003322010001 0.00.0 0.0 0001100

3121110 0.834 0.01.0 1.0

3122110 0.013 0.01.0 1.0

3121201 3611.0 0.0 0.0

3122201 814.53 0.0 0.0

* Comtoet No 313

SO3 Hot Collector Tube •o ioc levl 3

3130000 SG3-Hcl3 branch

3130001 2 I

31301010.5"60.446 0.00.090.0 0.446 1.0-50.834 0000000

3130200 013 15.575646 587.812 0.939-3

3131101 313010002314010001 0.0 0.00.0 0003000

3132101 313010003 323010001 0.0 0.00.0 0001100

3131110 0.3 0.0 1.0 1.0

3132110 0.013 0.0 1.0 1.0

31312012367.5 0.0 0.0

3132201 1243.5 0.0 0.0

* Coaponent No 314

* SO3 Hoe Collctor Tube cocection level 4

3140000 S03-HI•4 brnc

3140001 2 I

31401010.5460.464 0.00.090.0 0.464 1.0-50.34 0000000

3140200013 15.589744 587.81t0.939-3

3141101 3140100023150100010.00.0 0.0 0001000

3142101 314010003 324010001 0.0 0.0 0.0 0001100

3141110 0.834 0.0 1.0 1.0

3142110 0.013 0.01.0 1.0

3141201 3082.8 0.0 0.0

3142201 1284.7 0.0 0.0

* Conyoncos No 315

SSO)3 Hot Collccor Tube coumin level S 3150000 SG3-ldS brnch

3150001 2 1 3150101 0.5460.464 0.00.090.0 0.464 1.0-50.234 0000000

3150200013 15.594046 587.8200.939.3

3151101 3135010002316010001 0.00.00.0 0001000

3152101 315010003325010001 0.00.00.0 0001100

3153110 0.8 0.0 1.0 3.0

3152110 0.013 0.0 1.0 1.0

3151201 0.0 0.0 0.0

3152201 3082.8 0.0 0.0

" Coaponnc No 316

" SG3 Hot Collcor Top

3160000 SG3-li•t ipe

316000 2

31601010.546 1

3160102 0.0 2

3160201 0.546 1 3160301 0.485 I

3160302 3.552

3160401 0.0 1

3160402 0.505 2 3160601 90.0 2

3160901 1.0-5 0.834 1

3160902 1.0-5 0.02

3160901 0.0 0.01

316100100000002

3161101 0001000 1

3161201013 15.5921+6 58283 0.0 0.0 0.0 1

3161202013 5.5853186 2.2360.0 0.0 0.02

31613001

3161301 0.0 0.0 0.0 1 3161401 0.834 0.0 1.0 1.0 1

3162001 0.939-3 2

* 7".33 53: Tube Bundles

SComponen No 321

* SG3 Tube Buodle Level I • 101STubes LmlO.61m

3210000 SG3-Tbll pipe

3210001 5

3210101 0.13512 5

3210301 2.122 5

3210401 0.0 5

3210601 0.0 5

3210801 4.0.6 0.013

3210901 0.0 0.04

3211001 0000(00 5

3211101 00010004

3211201 013 15.5304.4579.87 0.00.0 0.0 1

321 202 013 15.50824 573.420 0.0 0.0 0.02

3211203 013 15.4864.6569.3120.00.0 0.03

3211204 013 15.46484 564.215 0.0 0.0 0.0 4

3211205 013 15.4434.4 560.995 0.0 0.0 0.05

32113001

3211301 466.87 0.0 0.04

3211401 0.013 0.0 1.0 1.04

32120010.93963 S

* CQpooent No 322

* SG3 Tube Bundle Level 2

* 1790"Tub= ;L 10.76

3220000 S03.TbI2 pipe

3220001 5

3220101 0.23865 5

3220301 2.152 5

3220401 0.0 5

3220601 0.0 5

322080 4.0.6 0.0135

3220901 0.0 0.04

3221001 00000005

322110100010004

3221201 013 15.541546579.5720.00.0 0.01

3221202 013 .53-596M..9400.00.0 0.02

3221203 013 15.4980+6567.751 0.0 0.0 0.03

3221204 013 15.476646563.661 0.00.0 0.04

3221205 013 15.455546 560.488 0.0 0.0 0.05

3223300I

3221301 814.53 0.0 0.04

3221401 0.013 0.0 1.0 1.04

3222001 0.939-3 5

SComponet No 323

* S03 Tabe Bundle Level 3

289 TubeK L- 11.04 m 3230000 S03-TbI3 pip

3230001 5

3230101 0.382 5

3230301 2.208 5

3230401 0.0 5

3230601 0.0 5

32308014.0- 0.013 5

3230901 0.0 0.04

3231001 0000000 5

323110100010004

3231201 013 15.5564•65"8.95900.0.0 0.01

3231202 013 15.536045 71.998 00.0.0 0.02

3231203 013 1-515046 566.6320.00.0 0.03

3231204 013 IS.49604565220.00.0 0.04

3231205 013 15.4763+65593840.00.0 0.05

32313001

3231301 1243.5 0.0 0.04

3231401 0.013 0.0 1.0 1.0 4

3232001 0.939.3 5

*Coapowse No 324

* SG3 Tube Bundle Level 4

* 2932 Tubec L - 12M m 3240000 53-Tbl4 ppe

3240001 5

3240101 0-3917 5

3240301 2.25 5

324040 0.0 5

3240601 0.0 5

3240801 4..6 0.013 5

3240901 0.0 0.04

3241001 0000005

324110100010004

3241201 013 15-568846578.950.00.0 0.0 1

3241202 013 15.5473+65719830.00.0 0.02

3241203 013 15.5262+6566.6140.0 0.0 0.03

3241204 013 15.5053562U.5040.00.0 0.04

3241205 013 135.464'6559.3650.00.0 0.05

32413001

3241301 1284.7 0.0 0.04

3241401 0.013 0.01.01.04

32420010.939-3 5

* CotoeM No 325

S03 Tube Bundle level 5

2368TubwL-lI4 m

3250000 S3-TbU pipe

3250091 5

3250101 031431 5

3250303 2M35

3250401 0.0

3250601 0.0 5

3250801 4.0-6 0.013 5

3250901 0.0 0.04

3251001 00000 5

325110100010004

3251201 013 15.5730+6579.3800.00.0 0.0 3

3251202 013 135-5497 572.638 0.0 0.0 0.0 2

3251203 013 15.5267 567.389 0.0 0.0 0.03

3251204 013 15.5%40+ 563.289 0.0 0.0 0.04

D-1 4

3251205 013 15.4815446560.1310.00.0 0.05

32513001

32M5130M 102.80.0 0.04

3251401 0.013 0.01.01.04

3252001 0.939-3 5

MA73.4 SO3: CoM CoUeor

* Cn~onem No 330

* SO) Col Collacm OWNtl Vokm

3300000 S03-Com branch

3300001 2

3300101 0.56 0.670 0.0 0.0 -90.0-.670 1.0-5 0.834 0000000

3300200013 15.433146 559.740.939-3

3301101 331010002330010001 0.0 0.0 0.0 0001000

3302101 330010002340010001 0.0 0.0 0.0 0001100

3301110 0.834 0.01.0 1.0

3302310 0.850 0.0 1.0 1.0

3301201 492.A 0.0 0.0

3302203 4 A 0.0 0.0

SCoMPaonc No 331

S 503 Cold CollecaorTube onecti level I

3310000 SO3-Cdl branch

3310003 2 1

3310101 0.5460.445 0.00.0 -90.0-.445 1.0-S Ol4 0000000

3310200013 15.4367+6 559.8760.939-3

3311101 332010002331010001 0.00.00.0 0001000

3312101 321050002331010003 0.00.00.0 0003300

3311110 0.834 0.0 1.0 1.0

3312110 0.013 0.0 3.0 1.0

33112014425.6 0.0 0.0

3332201 466. 0.0 0.0

SCOMPOM No 332 • SG3 Cold Co•leorTube couecam level 2

3320000 SG3-Cd2 branch

332=0001 2 1

332010 0.5460.446 0.00.0 -90.0-0.446 1.0-50.34 0000000

3320200013 15.4473+6 559.7580.939-3

3321101 3330100023320100010.0 ".00.0 0001000

3322101 3220500023320100030.0 0.00.0 0001100

3321110 0.834 0.0 1.0 1.0

3322110 0.013 0.0 1.0 1.0

33212013611.0 0.0 0.0

3322201 814.53 0.0 0.0

*COzoPOeOM No 333 • SO3 Cold Collec Tube coectiom level 3

3330000 SD- bIc

3330003 2 1

3330101 0.5460.446 0.00.0 -90.0.0.446 1.0-50.834 0000000

3330200013 15.460746 $59.5950.939-3

3331101 334010002 3330100010.0 0.0 " 0001000

3332101 3230500023330100030.0 0.00.0 0001100

3331110 0.834 0.0 1.0 1.0

3332330 0.013 0.0 1.0 1.0

3331201 2367.5 0.0 0.0

3332201 1243.5 0.0 0.0

" Componen No 334

" SG3 Cold Collctr Tube conalce0 level4

3340000 SG3OCcI4 bruach

3340001 2 1

3340101 0.5460.464 0.00.0 -90.0-0.464 1.0-5 0.834 0000000

3340200013 15.469046 559.7120.939-3

3341101 33501000233400001 0.00.00.0 0001000

3342101 3240500023340100030.000.0.0 0001100

3341110 0.834 0.0 1.0 1.0

3342110 0.013 0.0 1.0 1.0

3341201 1082.8 0.0 0.0

3342201 1284.7 0.0 0.0

• Conponce No 335 • SG3 Cold Collectr Tube c level 5

3350000 SC brAn

3350001 2 1

33501010.5460.464 0.00.0 -90.04.464 1.0-50.834 000000

3350200013 15.469744560.1260.939.3

3351101 3360100013350100010.000.0.0 0001000

3352101 325050002 335030003 0.0 0.0 0.0 0001100

3351110 0.834 0.0 1.0 1.0

3352110 0.013 0.0 1.0 1.0

3351201 0.0 0.0 0.0

3352201 1082.8 0.0 0.0

" C.•oevooct No 336

* SG3 Cold CollectorTop

3360000 S03.Co pipe

3360001 2

3360101 0.546 1

33601020.0 2

3360201 0.546 1

3360301 0.485 1

3360302 1.552

3360401 0.0 1

3360402 0.505 2

3360601 90.0 2

336080 3.0-S 0.834 1

3360023 .0-5 0.0 2

3360903 0.0 0.0 1
336100 0OO0OO 2

33611010001000 1

3361201 013 15.4662+66558.6260.00.0 0.01

3361202 013 15.45874.6 559.5n 0.0 0.0 0.0 2

3361300 1

3361301 0.0 0.0 0.0 1

3361401 0.134 0.0 1.0 1.0 1

3362001 0.939-3 2

* 7.3.5 Loop 3 Cold 14e

* Componen No 340

* Seal Loop of S3 Outlet to MCP3 Inlet

34000oo sI-.p3 pipe

34000019

3400101 0.56745 9

3400301 0.8 1

3400302 1.2 2

3400303 1.052 4

3400304 1.516

3400305 1.052 8

3400306 1.749

3400401 0.0 9

3400601-90.0 2

3400602 .45.0 4

3400603 0.0 6

3400604 45.0 8

3400605 90.0 9

3400701 .0.8 1

3400702-1.2 2

3400703 -0.67 4

3400704 0.06

3400705 0.67 8

3400706 1.74 9

34001 1.045 0.8509

3400901 0.0 0.02

3400902 0.039 0.0393 0]id= 1.58.90 d•-g.k0.26

3400903 0.0 0.06

3400904 0.039 0.0397 R/4d- l•,90dft.k k0.26

3400905 0.0 0.08

34010010000000 9

34011010001000 0

3401201 013 15.4421+6559.8770.00.0 0.01

3401202 013 15.4491+6559.8790.00.0 0.02

3401203 013 15.4556.5 559.SA0 0.0 0.0 0.03

3401204 013 15.4582+6559.AI 0.00.0 0.04

3401205 013 15.4602+6559.1S 0.00.0 0.05

3401206 013 15.459'6 559.11110.0 0.0 0.0 6

3401207 013 15.45656 559.879 0.00.0 0.07

3401208 013 15.4493+ 659.876 0.00.0 0.08

3401209 013 15.4399+6 559.872 0.00.0 0.09

34013001

3401301 4892.40.0 0.0 1

3401401 0.850 0.0 1.0 1.01

3402001 0.939-3 9

* 7.3.6 Main CkcUIaion Pump 3

SConmon•nt No 341

"MCP#3

3410000 MCP#3 pucp

3410101 0.0 $.27 3.00.0 0.0 0.0 0000000

3410108 340090002 0.00.00.0 000010

341010 342010001 0.0 0.0 0.0 0000100

3410200 013 15.722446 560.0100.939.3

3410201 1 4892.4 0.0 0.0

3410202 1 4892.4 0.0 0.0

3410301141--1.3.106140

3410302 104.72 1.06.549 84.0 47511.7500.747.0 0.0.0.0.

0.

*7..6.1 Table ipmp velociy

3416100 Ocatilvv 341

34161010.00.0

3416102 500.0 500.0

7.3.7 Loop 3 Cold Lie of MCP to IRV

* Componcen No 342

"Cold leg ofMCP#3 to COl leg MOV

3420000 olt4p3 pipe

3420001 2

3420101 0.56745 2

3420301 2.1075 2

3420401 0.0 2

3420601 0.0 2

3420701 0.02

3420801 1.0.5 0.150 2

3420901 0.0 0.0 I

342100100000002

34211010001000•1

3421201 013 16.011146560.1070.00.0 0.01

3421202 013 16.010146 560.107 0.0 0.0 0.02

3421300 1

3421301 4892.40.0 0.0 1

3421401 0.850 0.0 1.0 1.0 1

3422001 0.939-3 2

* Compoocnt No 343

"Loop 3: Cold kg Gte Valve

33430000 cD3-mnv sJitn 3430101 34202002 344010001 0.3117 0.05 0.05 0001000

34302021 148924 0.0 0.

* Component No 344

* Cold kg ofMOV to RV

34400o c-M3 pipe 3440001 11

34401010.56745 11

3440301 1.5 1

3440302 1.052 2

3440303 1.252 4

3440304 1.02 S

3440305 2.52 6 3440306 2.5 7

3440307 4.5

3440308 3.5 9

3440309 1.2 11

3440401 0.011

34406010.0 1

344060245.0 5

3440603 0.011

3440701 0.0 1

3440702,0.67 2

3440703 -0.87 4

3440704-0.67 5

3440705 0.0 It

3440801 1.0.6 0.850 II

3440901 0.0 0.0 i

3440902 0.039 0.0392

3440903 0.0 0.03

3440904 0.039 0.0394

3440905 0.0 0.0 10

3441001 O0000 II

34411010001000 10

3441201 013 160011+6 560.103 0.00.0 0.01

3441202 013 16.0031+6560.1030.00.0 0.02

3441203 013 16.OO64+6560.103 0.0 0.0 0.03

3441204 013 16.0123+6560.1060.00.0 0.04

3441205 013 16.015746560.1060.00.0 0.05

3441206 013 16.0176,6560.1060.00.0 0.06

3441207 013 16.0169'6 $60.105 0.0 0.0 0.07

3441208 013 16.0155+6560.103 0.0 0.0 0.08

3441209 013 16.014046560.1000.00.0 0.09

3441210 013 16.0131465560.0990.00.0 0.0 10

3441211 013 16.0126+56 0.009 0.0 0.0 0.0 Ii

34413001

3441301 4892.40.0 0.0 10

3441401 0.850 0.0 1.0 1.0 10

3442001 0.939-3 II

7.4.1 Loop 4: Hklleg

* Comoo No 4W0

*Ho 1of Leg oopi OftV oUtl to gue valve

4000000 bl.14 pipe 40000014

4000101 0.56745 4

40D0201 0.56745 3

4000301 1.49 1

4000302 1.14

4000401 0.0 4

4000601 0.0 4

400801 1. 0.5150 4

40000I 0.0 0.03

4001001 0000000 4

4001101 0001900 3

4001201 013 I5.61S5I46."511290.00.0 0.01

4001202 013 15.614746 51.525 0.0 0.0 0.0 2

4001203 013 15.6139+6 SS.525 0.0 0.0 0.03

4001204 013 15.613046 "S,.525 0.00.0 0.04

40013001

4001301 4524.80.0 0.0 3

4001401 0.850 0.0 1.0 1.0 3

4002001 0.939-3 4

• Component No4401

* Loop 4. H1t kg Gate Valve

4010000oooo e agli 40102o0 40004o002 402010001 0.3117 0.1 0.10002000

40o20201 4525.0 0.0 0.

* Comaoc No 402

Ho 88cc 1 fblo;4 oflGV to 34 hilt=

4020000 bl14 pipe 40200013

4020101 0.56745 3

4020201 0.56745 2

4020301 1.28 1

4020302 .052 2

4020303 1.2I= 3

4020401 0.0 3

40206010.0 1

4020602 45.0 2

4020603 45.0 3

4020701 0.0 1

4020702 0.67 2

4020703 0.17 3

4020M01 1.0-6 0.8503

4020901 0.0 0.01

402O0O2 0.052 0.052 2 Rid 1.58 90•dg Ikt 0.26

4021001 00O0 3

4021101 0001000 2 4021201 013 15.59724658MM160.00.0 0.0 1

4021202 013 15.5945+6 58.514 0.0 0.0 0.02

4021203 013 15.5865651-.509 0.0 0.0 0.0 3

402130012

4021301 4525.00.0 0.0 2

4021401 0.850 0.0 1.0 1.02

40220010.939-3 3

*7.4.2 S04: Hot Collector

* Compoocnt No 410 *SG4 Hotc Collector Inlet Volnue

4100000 SG4-Hcin branch

4100001 2 1

4100101 0.5460.670 0.0 0.0 90.0 0.670 1.0- 50.834 0000000

4100200 013 15.5346+6 588.412 0.939-3

4101101 402030002410010001 0.00.8575 0.85750001000

4102101 410010002411010001 0.00.0000 0.00000001000

4101110 0."50 0.0 1.0 1.0

4102110 0.134 0.0 1.0 1.0

4101201 4525.0 0.0 0.0

4102201 4525.0 0.0 0.0

" Compoonen No 411

* S04 Hot Collector Tube conection level I

4110000 0S4-Hell bantch

4110001 2 1

41101010.5460.445 0.000.09D.0 0.445 1.0-5 0.8L4 0OOOOO

4110200013 15.5329+6 518.481 0.939-3

4111101 411010002412010001 0.0 0.0 0.0 0001000

4112101 411010003421010001 0.0 0.0 0.0 0001100

4111110 0.134 0.01.0 1.0

4112110 0.013 0.0 1.0 1.0

4111201 4093.7 0.0 0.0

4112201 431.26 0.0 0.0

C mpco•ent No 412

* S04 Hot Collector Tubeect level 2

4120000 SG4-Hc12 branch

4120001 2 I

4120101 0.46 0.446 0.00.090.0 0.446 1.0-5 0.834 0000000

4120200 013 15.540046 588.484 0.939-3

4121101 412010002 413010001 0.0 0.0 0.0 0001000

4122101 412010003422010001 0.0 0.0 0.0 0001100

4121110 0.834 0.0 1.0 1.0

4122110 0.013 0.0 1.0 1.0

4121201 3340.9 0.0 0.0

4122201 752.79 0.0 0.0

• Cmponoent No 413

SS04 Hot Clector Tube eoection level 3

4130000 S04-H•13 branch

4130001 2 1

4130101 0.5460.446 0.00.090.0 0.446 1.050.-34 0000000

4130200013 15-551446 511.4900.939M3

4131101 413010002 414010001 0.0 0.0 0.0 00IOO

4132101 4130100034230100010.0 0.0 0.0 0001100

4131110 0.34 0.0 1.0 1.0

4132110 0.013 0.0 1.0 1.0

4131201 2190.9 0.0 0.0

4132201 1150.1 0.0 0.0

Coompone No 414

S04 Hot Collector Tube coectwoo evei 4

4140000 SCG4kWc1 branch

4140001 2 1

4140101 0.5460.464 0.00.0 90.0 0.464 1.0.50.834 0OOO

4140200 013 15.5622%6 518.4950.939-3

4141101 414010002 4150100010.0 0.0 0.0 0001000

4142101 414010003 4240100010.0 0.0 0.0 0001100

4141110 0.134 0.0 1.0 1.0

4142110 0.013 0.0 1.0 1.0

4141201 1002.1 0.0 0.0

4142201 1111.7 0.0 0.0

" Cmonoent No 415

" S04 Htc Collector Tube eooecion levels

4150000 SG4-HcL5 brach

4250001 2 1

41501010.5460.464 0.00.090.0 0.464 1.0-50.1134 0000000

415200013 15.66346 588.4960.939-3

4151101 41501002 4160100010.0 0.0 0.0 0001000

4152101 4150100034250100010.00.00.0 0001100

4151110 0.834 0.0 1.0 1.0

4152110 0.013 0.0 1.0 1.0

4151201 0.0 0.0 0.0

4152201 1002.1 0.0 0.0

" ComipoonenNo 416 * S04 Hot Collector Top

4160000 S04-Hct pipe

41600012

4160101 0-546 1

41601020.0 2

4160201 0.546 1

4160301 0.415 1

4160302 1.552

4160401 0.0 1

4160402 0.505 2

D-1 5
4160601 90.0 2

4160301 1.0-S 0.334 1

4160802 1.0-S 0.0 2

4160901 0.0 0.0 1

416100100000002

4161101000100 1

4161201 013 15.56426 582.341 0.00.0 0.0 1

4161202 013 1..5S72+4582W390.00.0 0.02

41613001

4161301 0.0 0.0 0.0 1

4161401 0.34 0.0 1.0 10 1

4162001 0.939-3 2

* 7.4.3 S04: Tube Bundles

* Coqx,• INo421

' S04 Tube Buode Level I

S1012TubL-10.61m

421000O SG4-TbU pipe

421000 5

4210101 0.13512 S

4210301 2.122 5

4210401 0.0 3

4210601 0.05

42103014.0-4 0.0135

4210901 0.0 0.04

4211001 0000000 5

421110100010004

4211201 013 15.3134+64579.93900.0 0.0 1

4211202 013 13.944%" M.OSS0.00.0 0.02

4211203 013 15.4757.6 567.682 0.0 0.0 0.3

4211204 013 15.457246 563.446 0.0 0.0 0.04

4211205 013 15.4389+6 560.160 0.0 0.0 0.05

42113001

4211301 431.26 0.0 0.04

4211401 0.013 0.0 1.0 1.04

4212001 0.939-3 5

* Coi No 422

'S04 Tube Bundle Level 2

1 l79STub= L- 10.76

4220000 SG4-TbI2 pipe

422000125

4220101 0.2336 5

4220301 2.252 5

4220401 0.0 5

4220601 0.0 5

4220301 4.0.6 0.0135

4220901 0.0 0.04

4221001 0000000 5

422110100010004

4221201 013 15.22546 59.6130.00.0 0.01

4221202 013 15.503746572.5700.00.0 0.02

4221203 013 15.48,516567.1220.00.0 0.03

4221204 013 J5.466,• 656.9030.00.0 0.04

4221205 013 i5.4,47+6S59.6630.00.0 0.05

42213001

4221301 732.79 0.0 0.04

4221401 0.013 0.0 1.0 1.04

4222001 0.939-3 5

• Component No 423

* SG4 Tube Budle Level 3

2141 Tub=s L a 11.04 m

4230000 SG4-Tbl pipe

4230001 5

4230102 0.328 5

4230302 2.208 5

4230401 0.0

4230601 0.0 3

4230301 4.0-6 0.013 5

4230901 0.0 0.04

423100100000005

4231101 00010004

4231201 013 15.5349 ."S78.989 0.0 0.0 0.0 2

4231202 013 15.517346457.6260.00.0 0.02

4231203 013 13.5000+65660170.00.0 0.03

4231204 013 15.43D0.6561.7960.00.0 0.04

4231205 013 15.4660+6558.5950.00.0 0.0"

42313001

4231301 1150.1 0.8 0.04

4231401 0.013 0.0 1.0 1.04

4232001 0.939-3 5

* Component No 424

* 0SG4'WTe Buudle c4

* 2932Tubo•;LM I.25m

4240000 SCA.Tbl4 pipe

424000125

4240102 0133917 5

4240301 2.255

4240401 0.0 5

42406010.0 3

4240801 4.0-6 0.013 5

4240901 0.0 0.04

42410010000000 5

42411010001000 4

4241201 013 15.5450.6 57&9580.00.0 0.0 2

4241202 013 IS526,.65715770.00.0 0.02

4241203 013 5.503S4.6563.9600.00.0 0.03

4241204 013 15.4904.6561.7330.00.0 0.04

4241205 013 13.472646 553.380.00.0 0.0.5 42423002

4241301 II20TO.O 0.04

4241401 0.013 0.0 1.0 1.04

4242002 0.939-3 5

" Coiqonnt No 425

" SG4 Tube Bumdle Level 5

" 2368TubesL-1.2.5m

4250000 SG4-TbtS pipe

4250001 5

42501010.31431 5

4250301 2.25 5

4250401 0.0 5

4250601 0.0 5

425O31 4.0.4 0.013 5

42I0901 0.0 0.04

4251001 00000005

425110100010004

4231201 013 23482.64579.4110.00.0 0.0 1

4251202 013 3.=52•+6.57=2290.00.0 0.02

4251203 013 1-.59034566.7550.00.0 0.03

4251204 013 15.4858+6 562.532 0.0 0.0 0.04

4251205 013 15.469446 55934 0.0 0.0 0.05

42513001

4231301 1002.2 0.0 0.04

4251401 0.013 0.0 1.0 1.04

4252002 0.939-3 5

* 7.4.4 S04: Cold Collector

• Co"•om No 430

* SG4 Cold Colltor Ocalt Voh=o

430000 S4.-Como bmncb

4300001 2 1 43001010.5460.670 0.00.0 -90.0-0.670 1.0-3 0.834 0000000

4300200 013 15.430746 559.053 0.939-3

4301101 431010002430010001 0.0 0.0 0.0 0001000

4302101 430010002440010001 0.0 0.0 0.0 0001100

4301110 0.834 0.0 1.0 1.0

4302110 0.8,00.01.0 1.0

4301201 4523.0 0.0 0.0

4302201 4525.0 0.0 0.0

* •Coppoom No 431

S04 COld Collector Tkbe comectioa level I

4310000 S-4.Cd branch

4310001 2 1

431010 0.1 .4A45 0.00.0 .90.004445 1.0.50.834 0000000

4310200 013 15.43316 3559.054 0.939-3

4311101 432010002431010001 0.00.00.0 0001000

431210l 421050002 431010003 0.00.00.0 0001100

4311110 0.834 0.0 1.0 2.0

4312110 0,013 0.0 2.0 1.0

4311201 4093.7 0.0 0.0

4312201 431.26 0.0 0.0

* Compoome No 432

* SG4 Cold C4olc Tube €oetone level 2

4320000 S0 ca hooc

4320001 2 1

4320102 0.1460.446 0.00.0 .90.0-0.446 1.0-.5 0.83 00D 0

4320200013 15.4416#6 58.9400.939-3

4321101 433010002 43210001 0.00.00.0 0001000

4322101 4220500024320100030.00.00.0 0001100

4321110 0.834 0.0 1.0 1.0

4322110 0.013 0.0 1.0 0.0

4321201 3340.9 0.0 0.0

4322201752.790.00.0

* Ccqponeo No 433

* S04 Cold Colleto Tube coemmi level 3

4330000 SC4-C banch

4330001 2 1

4330101 0.546 0.446 0.0 0.0 -90.0.0446 1.0-.5 0.834 00000

4330200 013 25.432646 558.7310.93963

4331101 434010002433010001 0.0 0.00.0 0002000

4332101 423050002433010003 0.0 0.00.0 0001100

4331110 0.834 0.0 1.0 1.0

4332110 0.013 0.0 1.0 1.0

4331201 2190.8 0.0 0.0

43322011150.1 0.0 0.0

Coeiponet No 434

S04 Cold Coleor Tube conection level 4

43.400 SG4.Cc24 branch

4340001 2 1

4340102 0.146 0.464 0.0 0.0 -90.0-0.464 1.0-5 0.334 0000000

4340200013 15.49246 553.340.939-3

4341101 4350100024340100010.0 0.00.0 0002000

4342101 424030002 434010003 0.0 0.000 0002100

4341110 0.834 0.0 1.0 1.0

4342110 0.013 0.0 1.0 1.0

4341201 1002.2 0.0 0.0

4342201 11237 0.0 0.0

Componen No 435

S04 Cold Coleaor Tube conectie level S

435000 ,4-Ca brinb

4350001 2 1

4350101 0.546 0.464 0.00.0 .90.0-0.464 2.0-30.834 0000000

D-16

4350200013 15.435936 559.3000.939-3

4351101 436010001 43S010001 0.0 0.00.0 0)01000

4352101 420500024350200=0 0.0 0.00.0 0001100

4331110 0.834 0.0 1.0 1.0

4352110 0.013 0.0 1.0 1.0

4351201 0.0 0.0 0.0

4352201 1002.1 0.0 0.0

" Componem No 436

* S04 CQld CollecorTop

4360000 S04-Co pipe

4360001 2

4360101 0.546 1

4360102 0.0 2

4360201 0..546

4360301 0.435 1

4360302 1.552

4360401 0.0 1

4360402 0.0M 2

4360601 90.0 2

43608011.0.5 0.934 1

4360302 1.0.- 0.02

4360901 0.0 0.0 I

4361001 0000000 2

4361101 001000 2

4361201 013 13.4558+6557.5930.00.0 0.01

4361202 013 15.4493.62557.43300.0.0 0.02

4361300 1

4361301 0.0 0.0 0.0 1

4361401 0.834 0.0 1.0 1.0 1

4362001 0.939-3 2

*7A.4. Loop 4 Cold Les

* Component No 440

* Seal Loop of SG4 Outlet io MCNI tntl

440000 o2.p4 pp

4400001 9

440001 0.56745 9

4400301 0.8 1

4400302 1.2 2

4400303 1.052 4

4400304 1.51 6

4400305 1.052 8

4400306 1.749

4400401 0.0 9

4400601 .90.0 2

4400602 .45.0 4

4400603 0.0 6

4400604 45.0 8

4400605 90.0 9

440070120.8 2

4400702 -1.2 2

4400703 40.67 4

4400704 0.06

440070S 0.67 8

4400706 1.74 9

44003011 .0.6 0.509

4400901 0.0 0.02

4400902 0.052 0.0523 *Pd -.. 518.90deg->Ik0.26

4400903 0.0 0.06

4400904 0.052 0.0527 * d.M - IA90 des0-gt0.26

4400905 0.0 0.0 8

4401001 0000000 9

44011010001000 8

4401201 013 15.4392+63559.0560.00.0 0.0 2

4401202 013 15.446246559.0580.00.0 0.02

4401203 013 15.452n+6 59.09 0.0 0.0 0.03

4401204 013 15.435246559.0600.0 0.0 0.04

4401205 013 15.4572+6 559.059 0.0 0.0 0.05

4401206 013 15.4567+6 559.0590.00.0 0.06

4401207 013 15.4.53846559.0370.00.0 0.07

4401208 013 15.4463+6559,.0,4•0.00.0 0.03

4401209 013 13.4370+6 559.05000.0.0 0.09

4401300 2

4401301 4525.0 0.0 0.0 8

4401401 0.850 0.0 1.0 1.08

4402001 0.939-3 9

* 7.4.6 Main COculat1"m Pump 4

* Componn No 44

* MCPS4 4410000 MCPO4 punp

4410101 0.0U.237 3.00.0 00.0.0 0000000

44101011440090002 0.0 0.00.0 0000100

4410109442010001 0.0 0.00.0 0001r00

4410200 013 15.7242+6 559.204 0.939-3

4410201 1 4525.0 0.0 0.0

4410202 1 4525.0 0.0 0.0

441030 141 -. -3 -20 615 0

4410302 104.72 1.0 6.057 84.0 47511.7500. 747.0 0.0 0.0 0.0

0.00.0

*7.4.6.I Table punp velocky

4416100 0 cnnvar 441

4416101 0.0 0.0

4416102 500.0 500.0

* 7.4.7 Loop 4 Cold Leg of MCP to RV
* Coaonect No 442

* Cold Ieg ofMCpst Io Cold kg MGV

4420000 cII4p4 pipe

4420001 2

4420101 0.56745 2

4420301 2.10752

4420401 0.0 2 4420601 0.0 2

4420701 0.02

44208011.0-5 0.90 2

4,20901 0.0 0.0 1

4421001 00000O0 2

44211010001000 1

4421201 013 16.0178+6 559.305 0.0 0.0 0.0 1

4421202 013 16.016%6 559.305 0.0 0.0 0.02

4421300 1

4421301 4525.00.0 0.0 1

4421401 0."50 0.0 1.0 1.0 1

4422001 0.939-3 2

• Cosponem No 443

* Loop 4: CoAd k Gate Valve

4430000 e04-mW Ljnogjs

443010144202000244401000103117 0.10.1 0001000

4430201 1 4525.0 0.0 0.

C ,orspooem No 444 • Cold kIg ofCold leg MGV to RV

4440000 e12-Wp pipe

4440001 11

4441010.56745 11

4440301 1.5 1

4440302 1.052 2

4440303 1.252 4

4440304 1.052 5

4440305 1.528 6

44403062.57

4440307 4.5 8

4440308 3.5 9

4440309 I.25 11

4440401 0.0 11

4440601 0.0 1

4440602 -45.0 5

44406030.0 11

4440701 0.01

4440702-0.67 2

4440703.0.87 4

4440704.0.67 5

4440705 0.0 11

44400I 1.0-6 0.850 It

4440901 0.0 0.0 1

4440902 0.052 0.052 2

4440903 0.0 0.03

4440904 0.052 0.052 4

4440905 0.0 0.0 20

44410010000000 11

44411010001000 10

4441201 013 16.002346559.2M90.00.0 0.0 2

4441202 013 16.004346 559.299 0.0 0.0 0.02

4441203 013 16.00744 559.299 0.0 0.0 0.0 3

4441204 013 16.01346 6559.301 0.0 0.0 0.04

4441205 013 16.0166.6559.3020.00.0 0.05

4441206 013 16.01866 559.3020.00.0 0.06

4441207 013 16.0180-+6$593000.0 0 .07

4441208 013 16.0168+65592970.00.0 0.08

4441209 013 16.01546559.290.00.0 0.09

4441210 013 16.0147+6559.2930.00.0 0.0 10

4441211 013 16.0143465592930.00.0 0.0 It

4441300 2 4441301 4525.00.0 "0 10

4441401 0.850 0.0 1.0 1.0 10

44420010.939-3 11

S. Pessurizer. Surp md Spray Lies

a 8.1 Pessurize Sage

* Comnpm No 501

pRP a•tg line emonacion with Loop 4

5010000 prz-94 sogjun

5010101 400040002 2010001 0.094 2.64 1.35 0001100

5010201 1 0.0 0.00.0

• Coponmne No 502 - Prssurize Surge line

50200018

5020101 0.094 8

5020301 2.015 1

5020302 1.335 2

5020303 1.433 3

5020304 2.6704

502030S 2452 5

5020306 3.0 7

5020307 3.148

5020401 0.0 8

$020601-45.0 1

5020602 -45.0 2

5020603 .90.0 3

5020604 -90.0 4

5020605 0.0 7

5020606 90.0 81

5020701-IA2 I

5020702 -1.2072

502003 -1.433 3

5020704-1.74

5020705 0.07

5020706 2.17 8

S02001 1.0-5 0.3463

5020901 0.180.18 1 *R/Jd4.9,90-ýk.0.12 02090D 0.0 0.0 2

5209 0.180.13 3 'R/d.4,90-ek.0.1$

5020904 0.0 0.06

5020905 0.180.18 7 OR/d=4.9.90-.k-0.l8

5021001 000O000 8

50211010001000 7

5021201 013 15.663846588.6340.00.0 0.0 1

5021202 013 1M672-4 .658A69 0.00.0 0.02

5021203 013 I1S6817.6589.2930.00.0 0.03

5021204 013 15.692346590.0370.00.0 0.04

5021205 013 25.698146591.7790.00.0 0.05

5021206 013 15.6992.6 595.008 0.0 0.0 0.06

5020227 013 15.698246600.-720.00.0 0.07

5021208 013 15.6915+6608.1540.00.0 0.08

5021300 2

50213020.00.0 0.0 7

5021401 0.346 0.0 1.0 1.07

5022001 0.939-3 8

* Ccapoeor No 503 • P112 gi- o eoonctior wikh Loop 4

5030000 prz-b14 52iljun

5030101 50208000254010001 0.0940.0 0.00001100

50302012 0.00.00.0

8.2 Press•rizer Tank

SPressurizer Tank

5040000o PR pipe

5040002 10

50401010.0000 10

5040301 0.970 11 below bearers

5040302 0.550 2*PRZbearer

500303 .000 3 'above beaters

5040304 1.400 9*

040305 0.8800 * op PUT

5040401 4.652 i

5040402 3.897 2

5040403 7.069 3

5040404 9.896 9

5040405 4.016 10

* 79 cub. m 5040601 90.0 10

5040801 1.0-5 0.0 1

54002 1.0-5 3.0 9

5040803 M.0-50.0 10

504090 0.0 0.09

5041001 0000000 10

5041101 0001000 9

5041201013 15.6919+6,616.164 0.0 0.00.0 1

5042202013 15.6774+6617.881 0.0 0.00.0 2

5041203013 15.6729+6617.994 0.0 0.00.0 3

5041204 013 15.6659+6617.997 0.0 0.00.0 4

5041205 013 15.6577 6617.997 0.0 0.0 0.0 5

5041206013 15.649546617.733 0.0 0.00.0 6

5041207013 15,6413•6615.043 0.0 0.00.0 7

0 Level L77 m 50412D8000 15.6347461.407.6 2.44466 0.563810.0 t

041209 002 15.63164-61.000 0.0 0.00.0 9

5041210002 15.63046 1.000 0.0 0.00.0 10

5041300 1

5041301 0.00.0 0.0 9

50414013.00.01.0 1.09

042001 0.939-3 7

5042002 0.939-3 20

383 Pressurzr~ Siady stare Controrllers

*Coropowem No so5

SPRZ Presure Contoller Valve

5050000 prz-p valve

050201 504100002 506000000 0.0 0.00.0 0001000

s0o01 10.00.0 0.0

505030 rP~vt

050301 601

Q Coeer No 506 *P1 Pressure BQUndary Volume

5060000 prz-p maipvol

3060101 0.0 1.0 1.00.00.0 0.0 I.-S 0.0 0000000

5060200 002 0 onulvar 500

5060201 1U.0.6 15.0+6 1.0

5060202 16.046 16.0"6 1.0

* Compooemt No 50

MZ L.evel Boundary Volmine

508000 paz-2 tnkD-1 7

S080201 0.0 10.070.00.00.0 0.0 I.-s 0.0 0000000

5080200 001

5080201 0.0593.00.0

• Component No 509

SPFZ Level Cotroller 509000 per-I V~Undp

50901 508000000 504010001 0.0

5090200 20 cmrivr 09

S90201 -1.00.-000.0 0.00.0 590202 -0.05 -5.0 0.0 0.0

5090203 0.00 0.0 0.0 0.0 590204 0.05 5.0 0.0 0.0

$090205 1.0 2000.00.0 0.0

9. Secondary Side

9.1 Fedwater Line for Loop I

SCosnpomes No 150

• -eodwater Boundary Volam for Loop 2

1500000 FWT.11 mndpvol

1500101 0.16 1.0 0.00.00.0 0.0 1.-50.0 0000000

150020 003 602

1500201 -2.0 7.056+6 437.25

1500202 0.0 7.0566 437.25

• Component No 151

L Loop I Fcdwastrpunp

1520000S0SI-F"Wundpjun

1510101 150000000 152010001 0.0

1510200 1

1510201 0.0345.6 0.00.0

: Conooem No 152

rdwno mew Wpe

1520000 FW-SGI pipe

1520001 2

1520101 O.06469 I

15203 2.0 I

1520601 0.0 1

1520801 120.5 0.0 2

1521001 0010000 1

15212010035.95496"6437.1170.0 0.0 0.0 1

• CoVepo No 153

SFeedwaer lie e•o ecioo to SO1

1530000 j200-202 bgljun

1530101 152010002 166010001 0.0 .020.00001000

1530201 1 345.600.00.0

9.2 SONI Swondary Side

• Component No 161 • SOO1 Tebe bundles Level I

2620000 01-112 bmncb

1610001 1 0

16101010.00.445 3.0 0.0 90.00.445 1.0-5 0.015 0000100

1610200000 5.90065+6 1.1960#.625909+6 0.21384

1611101 161010002 162010001 0.00.00.0 0001000 -

1611110 0.015 0.0 1.0 1.0

1611201 0.29589 0.77050 0.0

* Componen No 162

S 500I Tube bundles Level 2

1620000 sgl.r12 banch

1620001 1 0

1620101 0.00.446 5.940.090.00.446 1.0-50.0150000100

1620200000 5.89811461.1982.62.392106 0.30530

1621101 162010002 163010002 0.00.00.0 0001000

1621110 0.015 0.0 1.0 1.0

1621201 0.3252 0.82842 0.0

• Compn entNo 163

" S091 Tube bundles Level 3

1630000 ogi-T13 braoch

16300021 0

16301010.00.446 8.970.090.00.446 .0-5 0.01OS00000

1630200000 5.8958 1.1997462S910+6 0.41187

1631101 163010002 164010001 0.00.0 0.0 0001000

1631110 0.015 0.0 1.0 1.0

16312010.32240 0.86114 0.0

* Conpooenr No 164

• SI Tee bundles Level4

164,0000 igI-T4 branch

1640002 1 0

1640101 0.0 0.464 9.4 0.0 90.0 0.464 1.0-5 0.015 0000100

1640200000 5.89392+6 .2000+62.591126 0.51323

1641101 164010002 165010001 0.0 0.00.0 0001000

1641110 0.015 0.01.0 1.0

1641201 0.35684 1.0339 0.0

* Cozrpoaes No 165 • S50I Tube bundles Level5

2650000 s1I-T bramncb

1650001 2 0

16502010.00.464 9,930.090.00,4641.0-S 0.0150000100

1650200000 5.89213461.1999462-5911+6 0.53938

1651101 165010002 166010001 0.00.00.0 0001000

1651120 0.015 0.0 1.0 1.0
1651201 0.27069 1.0558 0.0

* ComponcutNo 166

SSCO1 Voh=e between ube budle ad pfanracd sdiec

1660000 sg8-16 band

16600011 0

16601010.00.245 10.71 0.090.00.2451.0-50.00001000

1660200 000 5.39119+6 1.1352+6 2.59114+ 0.95583

1661101 166010002 167010001 2.50.00.0 1001100

1661110 0.013 0.01.0 1.0

16612010.28431 0.29528 0.0

" Co -oe No 167

* SCAI Volum above peftated she

1670000 sill17 soolvol

1670101 0.0 0.650 28.558 0.0 90.0 0.650 1.05 0.0 0001000

1670200 000 5.8870446 1.162462.5911+6 0.34728

" Compoumee No168 o S04 Separator

1680000 sI-sep separater

1680001 3 0

1680101 0.00.260 10.09 0.090.00.260 1.05 0.0 0000000

168200000 $.8491+6 1.197.42U5911+6 0.49M84

681101 168010002 169010001 0.00.00.0 0001100° 0.35

1682101 168010001 177010002 0.00.00.0 0001100 0.05

1683101 167010002 168010001 0.00.0 0.0 0001100

1681110 0.0 0.0 1.0 1.0

1682110 0.0 0.0 1.0 1.0

1693110 0.0 0.01.0 1.0

16812010.188190.64312 0.0

1682201 2,4662 2.588 0.0

1683201 5.2534-3 0.84002 0.0

• Copoaum No 169

• ,G0i Seam doa

1690000 sgl-sd branch

1690001 1

16901010.00.580 10.21 0.090.00.-530.0-50.00001000

1690200002 5.8843246 1.0

1691101 169010002 180010001 0.00.1 0.1 0001100

16911100.1870.0 1.0 1.0

1691201 0.0 346.85 0.0

SComponet No 171

" SOO] Side cannels in the oftube bunds Level 1

1710000 sgl-1i branch

2710001 2 0

1710101 0.0 0.445 3.99 0.090.00.445 1.0-.50.20001000

1710200000 .90192+6 1.1924.162.591046 4.73308-2

1711101 171010002 172010001 0.00.00.0 0001100

1712101 171010004 161010003 0.00AO.4 0001100

1711110 0.2 0.0 1.0 1.0

1712110 0.03340.0 1.0 1.0

1711201..20947 .10213 0.0

1712201 1.6391 1.7705 0.0

* Conpecu No 172

SSOI5 Sid chunns in the ofmube bundlea Level 2

1720000 sg1412 brandh

1720001 2 0

1720101 0.00.4464.1 0.090.00.4461.0-50.20001000

1720200000 5.89886+6 1.1804+62.5910+6 0.150

1721101 172010002 173010001 0.00.00.0 0001100

1722101 172010004 162010003 0.00.4OA 0001100

1721110 0.2 0.01.0 1.0

1722110 0.03340.0 1.0 1.0

1721201-0.42569 -0.32527 0.0

1722201 1.4781 1.6"71 0.0

SCompooenm No 173

* SG1 Side c esin t(rebmdle.•evai3

1730000 1-513 brench

1730001 3 0

1730101 0.00.446 6.3"0.090.00.446 1.0-5 0.2 0001000

1730200000 5.8960846 1.1765462.5911+60.21108

1731101 173010002 174010001 0.0.00.0 0001100

1732101 173010004 163010003 0.00.40.4 0001100

1733101 173010002 178010001 0.00.00.0 0001100

1731110 0.2 0.01.0 1.0

1732110 0.03340.0 1.0 1.0

1733110 0.1 0.01.0 1.0

1731201.0 I8703 -3.14247-2 0.0

1732201 0.78193 1.0303 0.0

1733201-0.89402-031244 0.0

" Cwovso No 174 * SOI Chinn ls betwoe SO side wall and sheer vrtial wall

1740000 sglsM b1,•

1740001 1 0 1740101 0.00.4642.3 0.090.00`464 1.0-. 0.2 001000

1740200000 S.193184.61.1945462.5911+6 8L3498-2

1741101 174010002 175010001 0.00.00`0 0001100

1741110 0.2 0.01.0 1.0

1741201.0=2328.1.94714-2 0.0

" Caozsocat No 175 * SG•l Channela beween SO s"de wall and shoet varied wall

lecl 2 1750000 s&sl banch

1750001 1 0

1750101 0.0 0.464 3.88C0.0 0.0 0.4641.0. 0.2 0001000

1750200000 5.89046+61.1921462.591146 0.36046

1751101 175010002176010001 0.00.00.0 0001100

1751110 0.20.01.0 1.0

1751201 .. 51623 -3.57991-2 0.0

* C=.on tNo 176

*S 102cha betwee SO side wall and shet veal wail

level 3 1760000 s41-s16 branch

1760002 I 0

1760101 0.0 0.245 1.0 0.0 90.0 0.45 1.0.5 0.2 0001000

1760200000 5.8889946 1.186746 2.5911460.66340

1761101 176010002 167010001 0.00.00.0 0001100

1761110 0.2 0.01.0 1.0

1761201.0.264 -7.17213-2 0.0

*Coanonent No 177 * SGOl a•auncl between SO side wal and sheer vertical wall leve14

177000 s1-W7 branch

1770001 1 0 •

17701010.0 13S90.072 0.090.0 1.359 1.0-5 0.05 0001000

1770200000 5.8816+6 1.198"25911246 1.29266.2

1771101 17401000 177010001 0.00.00.0 0001100

1771110 0.050.01.0 1.0

1771201-2.500402793 0.0

Comqpoct eNo 178

* SGOI Chials btweenTube bunle and sheer va•al waDl

* andmmd a lin *A middle level 1

1780000 s1-sI brad

1780001 2 0

17801010.0 0.4643.750.090.00.4641.0-.50.2 0001000

1780200000 5.89389.6 1.1621+6 2.5911+6 0.56590

1781101 78010002 179010002 0.00.00.0 0001100

1782101 178010004 164010003 0.0 0.4 0.4 0001100

1781110 0.2 0.01.0 1.0

1782110 0.03340.01.0 1.0

1713201 0.70•59 430212 0.0

1782201 4.23940 -0.62467 0.0

" Coet No I79

" SCSl aumnala betwesTube bADle and sheer vM wall

" and a•ndlin f middleevd T 2

1790000 81-59 hbrand

1790001 2 0

17901010.0 0.464 4.72 0.0 90.0 0.4641.05 0.2 0001000

1790200000 5.89157461 .1583462.5911460.47277

1791101 179010002 166010001 0.00`00.0 0001100

1792101 179010004 165010003 0.0 0.4 0.4 0001100

1791110 0.2 0.0 1.0 1.0

1792110 0.03340.0 1.0 1.0

1791201-3.4523 7.27U86-0.0

1792201-1.1901 -2.6437 0.0

9.3 SOuI Steam Line

* Compon•t No ISO

•SGl SteamOutlet Pipe

i800000 SOVSp pP

18000011

1800101 0.274646 i

1800301 2.79 1

1800401 0 1

100601 90.0 1

1800801 1.0-S&0197 I

18010010010000 1

1801201002 5.84344'•1.00`000 0.0 2

" COTqOeeieNo 281

" So1 Steam Ou

1810000 1j80-182 s&Wjwe

1810101 180010002 1820100030.00.0 0.00001100

18120202 100 346.84 0.0

• Coavist No 182

• SGl SteamlHeader

182000 SI/Sl pipe

1820001 2

1280101 0.2206 2

1820301 5.67 2

1320401 0.02

18206010.02

1820801 1.0-50.530 2

1820901 0.0 0.0 I

182100010D00002

1821101 0001000 1

1821201002 5.4599+6•1.00.00.0 0.0 1

1821202 002 5.80197+6 1.00`00.0 0.0 2

1821300 2

18213010.0 346.77 0.0 1

• ConiocieNo 183

• So 1Heade Steam Lin cooneeiton

1830000 SLI-ous ugljua

1830101 182020002 184010001 0.22060.0 0.00001000

1830201 10.0 346.660.0

" Copoatxme No 184

SStcam line ofSol beaderto FIV

* l.IA3 6a AS , Flow ar.m 0.• s2q.m

1840000 SOVI/l pipe

1840001 6

1840101 0.26426

1•40301 5.0 2

1840302 9.02

1940303 16.34

1840304 8.25

1840305 14.0 6

1840401 0.0 6

1840601 0.04

1840602.36.05

1840603 0.06

81407010.04

184002 4.85

1840703 00 6

1840801 1.0-.50.5 6

1840901 0.0 0.0 5

1341001 00100006

1841101 000000 5

1841201002 5.31069+6 1.000.000 0.0 I

1841202002 5.90770#6 1.00.00.0 0.0 2

1841203002 5.80205+6 1.00.00.0 0.0 3

1841204002 5.7947846 1.00.00.0 0U0 4

1I41205002 5.79007+6 1.00.00.0 0.05

1841206002 5.73564+6 1.00.00.0 0.0 6

1841300 1

1842301 0.0345.02 0.05

" Caqon No 18S

'S" l Pressue Regulad Valve

1850000 SOl/P1R valve

1850101 140600M 186010001 0.2642 1.0 1.00000100

18502011 0.0344.95 0.

1850300 nautly

1850301 702701 0.050M7M

CmpowntNo 286

"SG# I StemLinesotbed MSIV

* I-n = 6.0 m6 Flow as - 0242 sqm

1860000 S1-41 pipe 18f600011I

1860101 0.2642 1

1860301 6.0 1

1860401 0.01

1860601 90.02

18607016.0-

1860801 1.0-5 0.58 I

18610010010000 1

1861201 002 5.626+6 1.00.00.0 0.0 1

* CcciponasNo 187

1870000 MSIVI valve

1870101 186010002 194010001 0.2642 1.0 1.00000100

11702011 0.0344.95 0.

1870300 nmuvlv

1870301402 5010.125 1.0

9.4 SCl B351-A

* Componmm No 189 • 1RU-AI

1890000 B3U-Al valve

1890202 184050002 190000000 0.02236 1.0 1.00000120

1890201 1 0.0 0.0 0.

189301 6036040.066666667 0.0

ComnponentNo 190 * AZnsWpheW

19000oo am dpvol

900101o 800.0070.00.0 0.0 0.0 .- 60.0 0000000

190O200 002

1900201 0.01.05+5 1.0

* 9.4.1501 la-bouse

*conipoesuNO191

1910000 32.B I-l valve

1910101 184 002 192000000 0.0223641.0 1.00000120

19102011 0.0 0.0 0.

1910300 mbnvlv

19103017127110.0666666667 0.0

- Coepooeu•No 192 'In-Hoc.

192000O -b0.l undpvol

1920101 8.0 0.0 70.0 0.0 0.0 0.0 536 0.0 0000000

19202000 02

1920201 0.0 5.761584 1.0

9.4.2 Core Steam Line

• Compoon No 194

Common Steam Lin ofMlSIV to Tuiine

* a - 6.0 m, Flow arm a 4 0.2642 sq.n

1940000 St-In pipe

19400011

1940101 i.0561 I

D-1 8
1940301 6.0 1

1940401 0.0 1

1940601 90.0 1

1940701 6.0 1

1940801 1.0-50.58

19410010010000 1

1941201 002 5.62668+6 1.00.00.0 0.0 1

SCoponent No 195

* CCoru Steam use Outslt

.1950000 stl aljun

1950101 194010002 196000000 0.0 0.00.0 0001000

19502021 0.0 2404.93 0.0

Conmpooec No 196

1960000 T'bn andlpvol

1960101 8L00.070.00.0 0.0 0.00.5.5-0.0 0000000

1960200 002

1960201 0.0 5.64.6 1.0

* 9.5 Feed.ater Line for Leop 2

* Componen No 250

* Feedwa • 3oundary Volume for Loop 2

2500000 FWr-12 endpvol

25001010.196 1.0 0.00.00.0 0.0 -5 0.0 0000000

2500200 003 602

2"00201 -1.0 7.056.6 436.25

2500202 0.0 7.056.' 436.25

• Cenpooem No 251

* Loop 2 Feedwate pump

2520000 SG2.FW lndpjen

2510101 250000000 252010001 0.0

2510200 1

2510201 0.0 345.0 0.0 0.0

* Component No 252

Feedwater line of Scrvo Valve to the SO2

252=000 FW-SG2 pipe

25200011

25201010.06469 1

2520301 2.0

2520601 0.0 1

2520801 1.0-S 0.0 1

2521001 0010000 1

2521201 003 5.93360+6 436.115 0.0 0.0 0.0 1

SComponent No 253

* Feedwaesr Line coneteion to SG2

2530000 j252:266 mgLju

2530101 252010002 266010001 0.0 5.0 20.0 0001000

2S30201 1 345.0 0.00.0

* 9.6 S102 Secoisdm Side

*Comonent No 261

* SON2 Tube bundles Level 1

2610000 sa2.TII branch

2610001 1 0

2610101 0.0 0.445 3.0 0.0 90.0 0.44 1.0-5 0.015 0000100

2610200000 5.879246 1.19704'62.59114+6 0.23102

2611101 261010002 262010001 0.00.00.0 0001000

2611210 0.015 0.0 1.0 1.0

2611201 0.291460.77492 0.0

• Componem No 262

S G02 Tube bundles Level 2

2620000 sg2.Tr2 bran

2620001 1 0

262010.00.446 5.940.090.00.446 1.0-50.015 0000100

2620200 000 5.$767646 1.19P+6 2.5912+6 032243

2622102 262010002 263010001 0.00.00.0 0002000

2622110 0.01S 0.0 1.0 1.0

2621202 0,31746 0.83240 0.0

* Cooponcm No 263

* SG#2 Tube bundles Level 3

263000o s&2-T3 br.anch

2630001 20

2630201 0.00.446 8.970.090.00.446 M.0-50.0150000100

2630200000 5.87460+6 1.1988462.5912+6 0.43894

2631101263010002264010001 0.0 0.00.0 0001000

2631110 0.015 0.0 1.0 2.0

26312010.27062 0.83983 0.0

* Ceompone No 264

* SG2 Tube bundles Level 4

2640000 sg2-Tl4 brnc

2640001 1 0

26401020.0 0.464 9.4 0.0 90.0 0.464 1.0.- 0.015 0000200

2640200000 5.872734•1i.1998+62.5912+6 0.52829

2642101 264010002 265010001 0.00.00.0 0001000

2642110 0.015 0.0 1.0 1.0

26412 0.25579 0."534 0.0

" Component No 265

" S0#2 Tube bundks Level

2650000 o&2-TLS braseb

2650001 0

2650101 0.00.464 9.930.090.00.4641.0-50.0150000100

26S0200000 5.97102+6 1.1997462.5912+6 0.56136

2651101 26010002266010001 0.00.00.0 0001000

2651110 0.015 0.0 1.0 1.0

2651201 0.19973 &.02230.0

" Compn No 266

" SG2 Vohme between tube bundl and peraorated e

2660000 sg2.26 b1anc 2660001 1 0

2660201 0.00.245 10.71 0.0 90.00.2M51.0-50.00001000

2660200000 5.870074 1.1161+6239144'6 0.08965

2661102 266010002267010001 2.50.00.0 1001100

2661110 0.013 0.0 1.0 1.0

2661201 0.308200.32135 0.0

" Compoecn No 267

" S002 Volume agunv perfowated diefe

2679000 M2-17 IsoI

26701010.00.65028.558 0.090.00.650 2.0-50.00002000

2670200 000 5.8643046 1.173046 2.5913+6 0.34157

• Component No 269

* 5062 Sepates 26800OO ,g2-sp seqt "

2680001 3 0

2680101 0.00.260 10.09 0.0 90.0 0.260 .0.-50.00000000

2680200000 5.86217+61.1943+62.59144+6 666

2681101 268010002269010001 00.0.00.0 0001200 * 0.4

2682101268010001 277010002 0.0 0.0 0.0 0001100 • 0.1

2683101 267010002268010001 0.00.00.0 0001100

2681110 0.0 0.0 1.0 1.0

2682210 0.0 0.0 1.0 1.0

2683110 0.0 0.0 1.0 1.0

2681201 0.4833 0.60077 0.0

2682201 2.0077 2.14700.0

2683201 9.16702-3 0.85815 0.0

SCemponent No 269 • S0#2 lean dora

26900OO a-2.d brunch

269000111

2690101 0.00.580 10.21 0.090.0058 2.0-0.00001000

269020 002 5.86164+6 1.0

269110126901000220020001 0.00.10.1 0001100

26911100.11170.01.0 1.0

2691201 0.0 343.95 0.0

" Component No 271

" S02 Side channels in the oftube bundles Level I

2710000 sa.2dl brnb

2710001 2 0

27101010.00.4453.990.090.00.4451.0-50.20001000

2710200000 5.88008462.2873+62.591226 536907-2

2711102 271010002272010001 0.00.00.0 0001100

2712101 271010004261010003 0.0 0.40.4 0001100

2711110 0.2 0.01.0 .0

2712110 0.03340.0 1.0 1.0

2711201 -. 20479-9.22926-2 0.0

2712201 1."191.7005 0.0

• Component No 272 " 802 Side channels in the ofabe bundles Levl 2

272000 jg2.a12 baneb

2720001 2 0 27201010.00.4464.1 0.090.00.446 .0-5 0.2 000 1000

2720200000 5.87705•46 1.1853+62.5912+6 0.172

2721101 272010002 273010001 0 0.0 0.0 0001100

2722101 272010004262010003 0.00.40.4 0001100

2722110 0.2 0.01.0 2.0

2722110 0.03340.0 1.0 1.0

2721201-0.40379-0.30190 0.0

2722201 1.39312 3530.0

C omeponent No 273 * SGM Side channl in the of tbc bundles Level 3

2730000 1"2a~ brandh 2730001 30

2730101 0.0 0.46 6.380M090.00.446 1.0-5 0.2 0001000

2730200000 5.8742946 1.11946 2."12+6 0.21403

2731101 273010002274010002 0.00.00.0 0001100

2732101273010004 263010003 0.00.40.4 0001100

2733101273010002278020001 0.0 0.00.0 0001100

2731110 0.2 0.01.0 1.0

2732110 0.03340.01.0 1.0

2733110 0.1 0.01.0 1.0

2731201 0.21958 -7.71092-2 0.0

2732201 0-2127 0.367540.0

2733201-4.64526-0.23813 0.0

" Componeen No 274

" SCW2 Claunels between SO side wall and sheat vatical wall

2740000 sg2-s14 brach

27400021 0

2740101 0.00.4642.30.090.00.464 1.0-50.20001000

274=0000 5.8714446 1.170.62-.5912+6 0.12115

2741101274010002275010001 0.00.00.0 000100

2741110 0.2 0.0 1.0 1.0

2741201 .2253 ... 05943-2 0.0

*Coospones: No 275

*S302 Channels between SO side wall and sbect vertical wall

level 2

2750000 *&2l banch

2750002 1 0

27501010.00.464 3.980.090.00.4641.0-50.20001000

2750200 000 5.86950+6 1.139+.659"13D6 0.19773

2751101275010002276010001 0.00.00.0 0001100

2751110 0.20.01.0 1.0

2752201 -0.36765 -0. 12214 0.0

* COMeOe No 276

S 3062 Claanels between SO side wal and beet vtica wall

Level 3

2760000 sg2.e16 branch

2760001 1 0

27601010.00.245 1.00.090.00.245 1.0-50.20001000

276020000 5.86630+6 1.1761+62.591346 038923

2761101 276010002267010001 0.00.00.0 0001100

2761110 0.2 0.0 1.0 1.0

2761201-033377 -0.19000 0.0

" Caqonent No 277

" £O62 Channels bewen 1 side "wl and sbhet vertical wall

level 4

277000 ag2-e17 brcanch

2770001 10

2770101 0.00 1.3590.072 0.090.0 1.359 2.0-50.05 0001000

270200 000 5.86479+6 1.1943+62.591346 5.70662.2

2771101 274010002 277020001 0.00.00.0 0001200

2771110 0.050.0 1.0 1.0

2771201-2.1061 0.28215 0.0

• Conpocent No 278 • S062 Ceannels between TUbe bundle and sheet verica wall

* and hAnne in the middle level I

2780000 &241 branch

2780001 2 0

2730101 0.0 0.464 3.75 0.090.00.464 .0-5 0.2 0001000

27M0200000 $.323 1.1679+62.591446 0.59726

27811012780100022790100D1 0.00.00.0 000100

2782101278010004 264010003 0.0 0.4 0.4 0001100

2781110 0.2 0.0 2.0 1.0

2782110 0.03340.0 1.0 1.0

2781201 0.45278-9.11490-2 0.0

278220140.95366-1.7357 0.0

° Cmaqiose No 279

SSO12 Caannecl between Tube bundle and sheet vertial wall

* and hannl in the utiddle level 2

2790000 %. branich

2790001 2 0

27902020.0 0.464 4.72 0.0 90.0 0.464 1.0- 0.2 0001000

2790200000 D5.870836 1.1513+62.591446 0.66511

2791101 279010002266020001 0.00.00.0 0001100

2792201 279010004265010003 0.00.40.4 0001100

2791110 0.2 0.0 1.020

2792110 0.0334 0.0 1.0 1.0

2791201-4.628 &829284-2 0.0

279221-0.82•92-.6266 0.0

" 9.7 S092 Stun Line

C* mponentNo 280

S002 Steia Onks tlec,

280000 $02Stp Ope 280000121

2800201 0274646 1

280301 2.79 1

2800401 0.0 2

2800601 90.0 1

2800801 1.05 0.187 1 2801001 0010000 2

2801201 002 .206"6 1.00.00.0 0.0 1

* Copoent No 231

* S02 SteamOut

28100005280-282 ugljan,

2821001 280010002 282010003 0.0 0.0 0.0 0001100

22020 10.0 343.96 0.0

° Component No 282

* SG2 Stain Header

2820000 S pipe

2820012 2

2820101 0.672

2820301 S.672

28204010.0 2

820601 0.02

282001 M52.0.030 2

2820902 0.0 0.0 2

282100 0010000 2

28221101 0001000 I

28201 002 5.8231946 1.00.00.0 0.0 1

282102 002 5.77874+6 1.0 0.00.0 0.0 2

2821300 1

28213010.0 344.060.0 1

D-1 9
" Comtonem No 283

" S2 Hader Stem Line connection

2830000 S.2-oux snSgj,,

2230101 282020002 284010001 0.22060.0 0.00001000

2930201 1 0.0 34423 0.0

" Compocnet No 284

" Steamline ofSG2bhadtro'IV

" Len• a 6. m, Flow rm O .264sq.m

2240000 S02,5tl pipe

2240001 6

2840103 0.26426

2240301 5.0 1

2840302 9.02

2840303 16.34

2840304 8.25

2840305 14.0 6

2840401 0.0 6

2840603 0.04

2240602.36.0 5

2240603 0.06

22407010.0 4

2840702 -4.8 5

22407030.0 6

2240201 1.0-5 0.5 6

2240901 0.0 0.0 5

2•410010010000 6

2841101 0001000 5

2841201002 5.7273846 1.00.00.0 0.0 1

2•41202002 5.7241746 1.00.00.0 0.0 2

2•41203002 5.7781446 1.00.00.0 0.0 3

2241204002 5.7702346 1.00.00.0 U 4

2241205 002 5.76502+6 1.00.00.0 0.0 S

2341206002 5.76014+6 1.00.00.0 0.0 6

2241300 1

2241301 0.0346.52 0.05

• Compoonen No 285

S02 Pre2suse, Resulated Valve

28500 SM2IPIV valve

2850101284060002 26010001 0.2642 1.0 1.00000100

22•5201 0.0 345.84 0.

2850300 znrviv

2250301 704 703 0.05 0.5209375

" Comqponen No 286

" SG2 Steam Lin to the MSIV

" Laos , 6.0 m, Flow rear 0.2642

2860000 St-.2 pipe

28600011

2860101 0.2642 1

2260301 6.01

2860401 0.0 1

2860601 90.0 1

2260701 6.0

2860801 1.0-5 0.52 1

28610010010000 1

2861201 002 S.6664 1.0 0.0 0.0 0.0 1

" Compoiac No 227

" MSIV for S2

2870000 MSY2 valve

2270101 286010002 194010001 0.2642 1.0 1.00000300

28702011 0.0 345.840.

2870300 m1Mvlv

2270301402 52 0.1428 1.0

- 9.8 SG2 BRU-A

* Co.mponenl No 229

SBRU.-A2

2890000 BRU-.A2 valve

2290101 2W40002 290000000 0.0223= 3.0 1.00000120

290201 i 0.0 0.0 0.

229300 zrnvlv

29030 605 606 0.0666666667 0.0

* Componet No 290

2900000 am tmndpvol

2900101 8.00.070.00.0 0.0 0.0 S.A0.0 0000000

2900200 002

2900201 0.0 1.05+5 1.0

9.8.1 S02 In-howe

Componemno 291

* SG2 b-5os

2910000 BRU-1n2 valve

2910101 23400002 292000000 0.0= 1.0 1.0 0000120

2910201 0.0 0.0 0.

2910300 narviv

2910301 7147130.0666666667 0.0

" Compone No 292

" In-House

2920000 Inhl modpvol

2920101 2.0 0.070.00.0 0.0 0.0 S.-60.0 0000000

2920200 002

2920201 0.0 5.6W22,26 1.0

* 9.9 Feedbrat Li for Loop 3

• Componen NO 350

* Feedwater ftoudwy Volume for Leoo 3

35000 FWT-13 =dpv

35001010.196 1.0 0.000.0 0.0 1A0.00000000

3500200 003 602

3500201 -1.0 7.05646 436.65

3500202 0.0 7.056+6 436.65

Compooem No 351

SLop 3 Feedwxw pump

35100OS03-7•.1• *j

3510101 35o000000 352010001 0.0

3510200 1

35102010.0 360.0 0.00.0

" C• OnMMtNo352

" Feedwate line of Srvo Vave to fte SC03

320000 FW-SG3 pipe 35200011I

3520101 0.06469

35203012.0 1

3520601 I 3520801 1.0-.5 0.0 I

3521001 001000 1

3521201 003 S.9594+6 436.518 0.0 0.0 0.01

*Ccomponew No 353 • Feedwaru lHne co•esmioe t SG3

3530000 j352-366 saju

3530101 352130082366010001 0.0 5.020.00001000

3530201 1 360.0 0.00.0

• 9.10M3Secoodm'y Side

Somponent•No 361

" SCA3 Tube bhudles Level I

361D0O0 S-l3oTI beran

3610001 0

3610101 0.0 0.445 3.0 0.0 90.0 0.445 1.0-5 0.015 0000100

3610200000 .996346 1.195%642.5909. 0.21866

3611101 361010002362010001 0.00.00.0 0001000

3611110 0.015 0.01.0 1.0

3611201 0.299370.77701 0.0

* Campone No 362

* $043 Tube buId•ll Level 2

360000 s3-r2 branch

3620001 1 0

36201010.0 0.446 5.94 0.0 90.0 0.446 1.0.5 0U015 0000100

3620200000 5.89711+61.1977462.591096 0.31333

3621101 3620102 363010001 0.00.00.0 0001000

3621110 0.015 0.0 1.0 1.0

3621201 032215 0.83822 0.0

*Conmzonca No 363

S 5043 Tube bundles Level 3

3630000 s53-T13 budch

3630001 3 0

3630101 0.0 0.446 8.97 0.0 90.0 0.4461.0-5 0.015 0000100

3630200000 5.8949146 1.199746 2911+,6 0.42606

3631101363010002 364010001 0.00.00.0 0001000

3631110 0.015 0.0 1.0 1.0

36312010313920.26927 0.0

* Component No 364

* SG03 Tube bundles L-vel4

3640000 ssi.T)4 budc

3640001 1 0

3640101 0.0 0.464 9.4 0.0 90.0 0.464 3.0-5 0.015 0000100

3640200 000 5.8930046 1.199946 2.591146 0.52245

3641101364010002365010001 0.00.00.0 0001000

3641110 0.015 0.0 1.0 1.0

3641201 0.34713 1.0501 0.0

*Compsonent No 365

SSG3 Tube bundles Level 5

365M00 sg3-TIS branch

365=01 1 0

3650101 0.0 0.64 9.930.090.00.464 3.0- 0.015 0000300

3650200000 5.8912646 1.1999462. I5916 0.55531

3651101365010002366030001 0.00.00.0 0003000

3651110 0.015 0.01.0 1.0

3651201 0.26301.07440.0

* Componen No 366 • S03 Volume btween tube bundle and pexomed shefe

3660000 •S3-16 anacb

36600031 0

36601010.00.245 10.71 0.090.00.2451.0.50.00001000

3660200000 5.8903546 1.1292462.591146 0.93951

3661101366010002367010001 2.50.00.0 1001100

3661110 0.013 0.0 1.0 10

3661201 0.29910 031039 0.0

* Component No 367

* 502 Volume above perbratod esbem

36700M s$"4 aglvol 367010 0.0 0.6502 2.55 0.0 90.0 0.650 M.00. 00001000

3670200000 5.607.+61.1855462.591146 0.35868

* Compocent No 368

362000 sg-sep sep~area

3680001 3 0

3680101 0.00.260 10.09 0.0 90.00.2601.0-5 0.0 0000000

3602 000 5.297'6 1.19764 2.591146 0.49991

3621101363010002369010001 0.00.00.0 0001100*0.5

3622101368010001 377010002 0.00.00.0 0001100"0.1

3623101 367010002 368010001 0.00.00.0 0001100

3621110 0.0 0.01.0 3.0

3622110 0.0 0.01.0 1.0

3683110 0.0 0.01.0 1.0

3681201 0.212 0.67652 0.0

368201 2.5417 2.6703 0.0

3683201 5.34399-3 0.5712 0.0

" Component No 369

" SG3 Steam dow

369000 Wg-id beanch

3690001 1 1 3690101 0.0 0.580 10.21 0.0 90.00.5801.0-50.0 0001000

3690200002 5.89338+6 1.0

3691101 369010002380010001 0.00.10.1 0001100

3691110 0.137 0.0 1.0 1.0

3691201 0.0 360.03 0.0

* Conpoom No 371 o S03 Side channels in the oftube bundles Level 1

3710000 s$34311 b

3710001 2 0

3710101 0.0 0.445 3.99 0.090.0 0.445 1.0-S 0.2 0001000

371020 0000 5.90090+6 1.13810+62.593106 4.5$883-2

3711101 371010002372010001 0.00.00.0 0001100

3712101 371010004361010003 0.00.40.4 0001100

3711110 0.2 0.01.0 1.0

3712110 0.03340.0 1.0 1.0

3711201-0.20984-0.10346 0.0

3712201 1.6461 1.77900.0

- Componen No 372

1 SG43 Side channels in the of tube bundles Level 2

3720000 n34•2 bane

3720001 2 0

37201010.00.4464.10.090.00.446 1.0.50.20001000

3720200000 5.89713461.17,9'62.591146 0.14715

3721101 372010002373010001 0.00.00.0 0001100

37221013720100041362010003 0.00.40.4 0001100

3721110 0.2 0.0 3.0 1.0

3722110 0.0334 0.0 1.0 1.0

3721201-0.42455 -0.32538 0.0

3722201 1A591 1.65400.0

SComponen No 373

* SG3 Side channel in the of tube bundles Level 3

3730000 ss3-u3 bencb

3730001 3 0

3730101 0.0 0.446 6.38 0.0 90.0 0.4461.- 0.2 0003000

3730200000 5.8950446 .1748462.$91146 0.21023

3731101 37301000 374010001 0.00.00.0 0001100

3732301 373010004363010003 0.0 0.40.4 001100

373310137301002372030001 0.00.00.0 0001100

3731110 0.2 0.01.0 1.0

3732110 0.03340.01.0 1.0

3733110 0.1 0.0 1.0 1.0

37312014.18705 -3.18432-20.0

3322701 0.64132 0.875520.0

3733201 -0.97943 -0223 0.0

• Coponent No 374 • SG3 Chnmnels between SG side wall and sbh vetical wall

3740000 ng3-s3 lan6c

3740001 1 0

37401010.00.4642.30.090.00.464 I.0.2 020003000

374020000 5.8921546 1.1942+62.-591136 L.66335-2

3741101374010002375010001 0.00.00.0 0003300

3741110 0.2 0.01.0 1.0

37412013-22605 -3.23820.0

" Componeut No375

" 504 Channels betwee SO side wall and shoe vertidal wall

level 2

3750000 s" b2nc

3750001 1 0

3750101 0.0 0.464 3.8 0.0 90.0 0.4641.0-502 0003000

3750200 000 .S943+6 1.19136 2.591146 036570

3751101 375010002376030001 0.00.00 0001100

3751110 0.2 0.01.0 1.0

3751201-04.53048 -3.61154-2 0.0

" Component No 376

" S03 Chanl betwen SO side wall and sheet vtical wall

level 3

376ODDO sn3-s6 blanch

3760001 3 0

37601010.00.245 1.00.0 90.0 0.25 1.0-5 0.2 0001000

3760200000 5.887996 1.1,60,62.591146 0.67386

3761101 3760100M2367010001 0.000.0.0 0001100

3761110 0.2 0.0 1.0 1.0

3761201-0.26965 -7.15029-2 0.0

D-20
" Compo.em No 377 " S£03 Cannels between So Wie wall and sheet vmical wall

level 4

37700 Og3-O17 branch

3770001 1 0

3770101 0.00 1359 0.072 0.0 90.0 1.339 1.0-5 0.05 0001000

3770200000 3O5856746 1.1977462.3911+6 0.0

3771101 374010002377010001 0.00.00.0 0001100

3771110 0.050.0 1.0 1.0

3771201-2.3417 .0.58399 0.0

- Componme No 378

0 5G83 OM eb betweem Tube bundle and sheet vmwleal wall

I ad channelinthe middle level I

3780000 sg3-sl8 macb

3780001 2 0

370101 0.0 0.4643.75 0.090.00.464 1.0-5 0.2 0O01000

3780200000 5.89297+6 1.158•46 2.591146 0.62629

3781101 378010002 379010001 0.0 0.0 0.0 0001100

3782101 37800004 364010003 0.0 0.4 0.4 0001100

3781110 0.2 0.0 1.0 1.0

3782110 0.03340.0 1.0 1.0

3781201-0.6563 -0.28274 0.0

378=2201 .025535 -0.66716 0.0

• Compon No 379

" S083 Channels between Tube bundle Wd shbet ver•cal wall

" and channel in the middlelevel 2

37900 oo 3o, branch

3790002 2 0

3790101 0.0 0.464 4.72 0.0 90.0 0,464 1.0-3 0.2 0001000

3790200000 5.89076"6 1.1547+6 2.591146 0.46998

3791 101 379010002366010001 0.0 0.00.0 0001100

3792101 379010004 365010003 0.0 0.4 0.4 0001100

3791110 0.2 0.0 1.0 1.0

3792110 0.03340.0 1.0 1.0

3791201 -3.4825 9.79002-2 0.0

37922Ol-1.1037-2.6714 0.0

0 9.11 SG3 Steam Lin

* Compottem No 380 SSO3 Stemn Outit Pipe

3800000 SG3/Stp pipe

380000 1

3800101 0.274646 1

3800301 2.79 1

3800401 0.0 1

3800601 90.01

3800801 1.0-S 0.187 1

38010010010000 1

3801201 002 .83874+6 1.0 0.0 0.0 0.0 1

" Component No 381

" S03 Steam Out

3810ooJ0380-382 omgjun

3810101 3800200023820100030.00.0 0.00001100

39102011 10.0 360.030.0

" Comnponem No 382

" SG3 Steam Reader

3820000 S3StH pipe

3820002

38"20102 0.2206 2

3820301 5.672

3920401 0.02

38206010.0 2

3820381 1.0-5 0.530 2

3820901 0.0 .0 1

382100100100002

3821101 0002000 1

3821202 002 5.84160+6 1.0 0.0 0.0 0.0 1

3821202002 5.79325+6 1.00.00.0 0.0 2

3821300 1

3821301 0.0 360.040.0 1

" Component No 383

' S03 Header Steam Lim eonnection

3830000 S.3-out scg~lun

3830101 382020002384010001 0.2206. 0.00001000

3830201 2 .0 360.05 0.0

" Compone No 384

SSteam line of£SO3besdetoFlV

" Lengt = 68.8 m. Flow ares. O.2642 sqm

3840000 SG03/Sll pipe

3840001 6

3840101 0.26426

3840302 3.0 1

3840302 9.02

3840303 16.3 4

3840304 8.25

384030•14.06

38404010.0 6

38406010.04

3940602 -36.05

3940603 0.0 6

3840701 0.0 4

3840702 -4.8 5

3840703 0.0 6

3840802 1.0-5 0.58 6

3840902 0.0 0.0 5

3841001 00•0006

3941101 0001000 5

3841201002 5.8028456 1.00.00.0 0.0 I

3841202002 5.799556 1.00.00.0 0.0 2

3841203002 5.79340.6 1.00.00.0 0.0 3

3841204002 .3.785436 1.00.00.0 0.0 4

3841205002 3.78019.6 1.00.00.0 0.0 5

3841206002 3.7735+.6 1.00.00.0 0.0 6

3841300

3341301 0.0360.01 0.05

* Comapont No 385

"S03 Phsstve Regulated Valve

3850000 SG£3PRV Valve

3850101 384060002 396010001 0.2642 1.0 1.00000100

38502011 0.0 359.96 0.

3850300 =a'vtv

3850301 706705 0.05 0.31750

*niponeni No 386

SO£0 Steam Line to the WIS5W

Leng - 6.0 m. Flow ao - 0.2642

3860000 St-1n pipe

38600012

3860101 0.2642 1

3960301 6.0 1

3860402 0.0 1

3860601 90.01

38607016.0 1

3860801 1.0-5 0.58 I

38610010010000 2

3862202002 5.626U+6 1.00.00.0 0.0 1

• Component No 387

* MSIV for SG3

3870000 ?SIV3 valve

3870101 386010002194010001 0.2642 1.0 1.00000100

38702011 0.0 359.9 0.

3870300 nt'vlv

3870301402 503 0.14281.0

9.12 S03 BJU-A

* Componme No 389

•BRU-A3

31190000 BRU-A3 valve

3890101 38400002 390000000 0.02236 1.0 1.00000120

38902011 0.0 0.0 0.

3890300 vi-v

3890302 607 608 0.0666666667 0.0

* Component No 390 * Aunnspber

3900000 am mtdpvol

3900101 8.0.0.079.00.0 0.0 0.0 5-60.0 000000

3900200 002

3900201 0.0 1.05+5 1.0

• 9.12.1 3 In-house

*Component No391

3910000 BRU-In3 valve

3910101 384030002392000000 0.02236 1.0 1.00000120

39102011 0.0 0.0 0.

3910300 mnvlv

3910301 716 715 0.0666666667 0.0

* Component No 392

* in-Hose

3920000 Inb43 ntalvII

3920101 8.00.070.00.0 0.0 0.0 1.-60.0 0000000

3920200 002

3920201 0.0 5.8&34746 1.0

* 9.13 Feedwter Line hr Loop 4

SCmponent No 450

a oFee Bdwvoundary Vohoene tfo Loop 4

4500000 F%7-4 nUdpvol

45001010.196 1.0 0.00.00.0 0.0 1.- 0.0 000000o

4300200 003 602

4500201 .1.0 7.056+6 437.05

450022 0.0 7.056+6 437.05

*Component No 451

• Loop 4 Feedwater pmp

451000• SG4-FW ndpjuo

45101011450000000 452010001 0.0

4510200 1

4510201 0.0 354.4 0.00.0

: Component No 452

* Fecdwzcr line of Srvo VaIve to the £04

4520000 FW.S04 ppe

4520001 1

4520101 0.06469 1

4520301 2.0 1

4520601 0.0 1

4520801 I.0-5 0.0 1

D-21

45210010010000 1

4521201 003 5.929036 436.914 0.0 0.0 0.0 1

* Conponoet No 453

• Feedwater line ononetcion to £S4

4530000 j452-466 =gljun

4330101 452010002466010001 0.0 5.020.00001000

4330201 I 354.4 0.00.0

S9.14 somseodaySide

* Component No 461

* SO£4 Tube bundles Level 1

4610000 g4.-T4 brneh

4610001 1 0

4610101 0.0 0.445 3.0 0.0 90.0 0.445 1.0-5 0.015 0000100

4610200 000 S.87138+6 1.19426• 2.3911*6 0.21642

4611101 461010002462010001 0.00.00.0 0001000

4611110 0.013 0.0 1.0 1.0

4611201 0.29793 0.77482 0.0

* Component No 462

* £$04 Tube bundles Lcve 2

4620000 sg4-TI2 branch

462000 1 0

4620101 0.00.446 3.940.090.0 0.446 1.0-50.015 000010

4620200000 5.86984+61.1964*62.5912+6 0.3096

4621101462010002 463010001 0.0 0.0 0.0 0001000

4621110 0.2 0.0 1.0 1,0

4621201 0.32709 0.83455 0.0

SComponent No 463

• SG£4 Tube bundles Level 3

46300DO s94-T23 branch

4630001 1 0

46301010.0 0446 8.97 0.0 90.0 0.446 .0-5 0.012 0000100

4630200000 S.86662+6 1.1981"2.5912246 0.41902

4631101463010002464010001 0.00.0 0.0 0001000

4631110 0.013 0.0 1.0 1.0 ,

4631201 0.319210.86694 0.0

• Component No 464

* SG#4 Tube bundles Level 4

4640000 sg4-TI4 braoch

464000 1 0

46401010.00A464 9.4 0.090.00.464 1.0-S 0.015 0000100

4640200000 5.86469+6 1.198442.5913+6 0.52092

4641101464010002 463010001 0.00.00.0 0001000

4641110 0.013 0.0 1.0 1.0

4641201 0.35333 1.0443 0.0

SConi•oeNo 465

SC£#4 Tube bundles Level 5

46S0000 s4T15 Wnnem 46501 1 0

4630101 0.0 0.464 9.93 0.0 90.0 0.464 1.0-.5 0.013 0000100

465020 000 5.86292+6 1.1983.62.5913+6 0.54717

4631101 465010002 466010001 0.0 0.00.0 0002000

46S1110 0.015 0.0 1.0 1.0

46512010.26937 1.0684 0.0

SCoponen No466

• £0#4 Volume between lube budl and Patented sbeete

4660000 014-16 branch

4660002 1 0

4660101 0.00.245 10.71 0.0 90.00.245 1.0-5 0.0002000

466M 000 5.86200+6 1.1312+62.2912+6 0.937S4

4661101466010002467010001 2.50.00.0 1001100

4661110 0.013 0.0 2.0 1.0

4661201 0.29241 0.30361 0.0

" Component No 467

" C184 Volume above perf-rated thme

4670000 s34-T7 mglvol

4670101 0.0 0.650 28.58 0.0 90.0 0.630 1.0-3 .00001000

4670200000 5.85778+6 1.142+62.5913+6 0.35299

* Component No 468

a 504 Separtor

460000 9C4-sp separ

4680001 3 0

46901010.00.260 10.09 0.0 90.00.260 1.0-5 0.00000000

4680200000 3.853664+6 1.1961"62.3913.6 0.49904

4681101468020002469010001 0.00.00.0 0002200

4682101468010001 477010002 0.00.00.0 0001200

4683201 467020002 468010002 0.00.00.0 0001100

4681110 0.0 0.0 1.0 1.0

4682110 0.0 0.0 1.0 1.0

4683110 0.0 0.0 1.0 1.0

4681201 0.20401 0.66192 0.0

4682212.5260 2.6525 0.0

4683201 5.49352-3 0.15078 0.0

*Compocem No 469

aSC94 Stam doam

469000D -sdbrnh

4690001 1

46901010.00.580 10.21 0.0 90.00.580 1.0-S 0.0000i000

4690200002 5.85506+6 1.0

4691101 469010002480010001 0.00.10.1 0002I00

4691110 0.187 0.0 1.0 1.0
4691201 0.0 354.580.0

* Component No 471

" S044 Side chancels in the oftube bundleS IvM I

471000 s•,4l brand

4710001 20

4710101 0.00.443 3.99 0.0 90.0 0.445 L.0-S0.20001000

4710200 000 5.8726"6 1.1901+62.5912+6 4.65918-2

4711101 471010002472010001 0.0.00" 0001100

4712101 471010004461010003 0.00.40.4 0001100

4711110 0.2 0.0 1.0 1.0

4712110 0.033401.0 1.0

4711201.0.20934.010292 0.0

4712201 1.6437 1.77640.0

* Conpoo•et No 472

" SC44 Side channels in the of tube besdles Levi 2

4720000 sg4-s2 branch

4720001 2 0

4720101 0.00.4464.1 0.090.00.446 1.0-5 0.2 0001000

4720200 000 3.06958+6 1.1780.2.591246 0.14903

4721101 472010002473010001 0.00.00.0 0001100

4722101 472010004462010003 0..4O0.4 0001100

4721110 0.2 0.0 1.0 1.0

4722110 0.03340.0 1.0 1.0

4721201442562.032552 0.0

4722201 i.4698 1.6676 0.0

C rcene No 473 • S044 Side hannels in the of tube bundles Levi 3

4730000 40 boranh

4730001 3 0

4730101 0.0 0.446 6.380.090.00.446 1.0-50.20001000

4730200000 5.6679461.1741+62.591346 0.21106

4731101 473010002474010001 ""0.00.0 0001100

4732101 473010004463010003 0.0.40.4 0001100

4733101 4730100024473010001 0.00.00.0 0001100

4731110 0.2 0.0 1.0 1.0

4732110 0.03340.01.0 1.0

4733110 0.1 0.0 1.0 1.0

4731201 -0.1M667-3.07223-20.0

4732201 0.72159 0.96151 0.0

4733201-0.93409 -.0.M3 0.0

* Componeno No 474

" S014 Cane betwee SO sidewall and sheet vatical wall

4740000 sg-sl4 brancd

4740001 1 0

4740101 0.0 0.464 2.3 0.0 90.0 0.464 1.0-S 0.2 0001000

474020 000 5.8635996 1.1926,6•2.91346 8.40016-2

4741101 474010002475010001 0.00.00.0 0001100

4741110 0.2 0.0 1.0 1.0

4741201-,22460 -1.32063-2 0.0

" Component NO 475

" SG*4 Camn•ls between SO side wall and shea vertical wall

level 2

475000 sg•-ls branh

4750001 I 0

4750101 0.0 0.464 3.380.090.00.4641.0-50.20001000

4750200 000 $.611746 1.1903462.591346 0.36106

4751101 475010002476010001 0.00.00.0 0001100

4751110 0.2 0.0 1.0 1.0

4751201 -. 52166-3.53692-20.0

* Cmp~onet No 476 * • ChannIs betwe SO side wall and sheet vertical wall

level 3

4769000 s54-6sl branch

4760001 1 0

47601010.00.245 1.00.090.00.24S 1.0-5 0.2 0001000

4760200 000 3.3597146 1.134746 2.591346 0.66803

4761101 476010002467010001 0.00.00.0 0001100

4761110 0.2 0.0 1.0 1.0

4761201 0.26756 -7.06050-20.0

SCepone No 477

SSGA4 Channels between SO side wall and sheet vertical wall

level 4

4770000 sg4-e1 brane

4770001 1 1

47701010.00 1.359 0.072 0.0 90.0 1.359 1.0-S 0.05 0001000

4770200000 5.8574146 1.1961462.391346 0.00000

4771101 474010002477010001 0.00.00.0 0001100

4771110 0.50.0 1.0 1.0

4771201 -101.94 0.0 0.0

* Co newpoat No 478

* SGS4 Channels between Tube bundle and sbeed vertial wall

nd dchamd in the middle level 1

4780000 sg4-s branch

4730001 2 0

47501010.0 0.4643.750.090.00.4641.0-50.20001000

4730200 000 3.8646646 1.15346 2.591346 0.59496

4781101 478010002479010001 0.000.0.0 0001100

472101 473010004 464010003 0.0.4 0.4 0001100

4781110 0.2 0.0 1.0 1.0

4732110 0.03340.0 1.0 1.0

4781201-0.68210-.29300 0.0

472201-0.24753 4.64835 0.0

" Component No 479

" SO34 Channels betwe Tube bundle and shed vertical wall

* and dnn in the mddle level 2

4790000 sg4-s[9 bu•ch

4790001 2 0

4790101 0.0 0.4644.72 0.0 90.0 0.464 1.0.5 0.2 0001000

4790200 000 5.323946 1.155116 2.91346 0.47149

4791101 479010002 466010001 0.00.00.0 0001100

4792101479010004465010003 0.00.40.4 0001100

4791110 0.2 0.0 1.0 1.0

4792110 0.03340.0 1.0 1.0

4791201-3.4701 L.47321-20.0

4792201 -1.1522 -2.6616 0.0

, 9.15 SG,4 4SsmLine

*Comsponent No 430 *SC-94 Sum nOustlet Pipe

4300000 SG4'Sp pipe

43000011

4300101 0.274646 1

4800301 2.79 1 4300401 0.0 1

4300601 90.01

430001 1.0-50.187 1

48010010010000 1

4301201 002 5.81208461.00.00.0 0.0 I

SComponet No 481

° S04 SteamOut

431000043o-42 nglju

4310101 430010002 482010003 0.00.0 0.00001100

4810201 10.0 354.580.0

* Componem No 432

" S04 Stesam Header

432000o SG4IStH pipe

483201 2

4820101 0.2206 2 4301 5.67 2

4820401 0.0 2

4820601 0.02

48208011.0-5 0.530 2

4320901 0.0 0.0 1

4821001 0010002

4821101 0001000 1

4821201 002 5.81477+6 1.00.00.0 0.0 1

4321202 002 5.76339+6 1.00.00.0 0.0 2

4321300 1

48213010.0 354.590.0 1

SCooon No 483 "S04 Header Steam Line connectio

4830000 SL4-ot sgljun

4830101 432020002434010001 0.22060.0 0.00001000

4830201 1 0.0354.90.0

, Component No 434

" Steamline ofSG4besaduoFlV

* Lengt=h68.8 n. Fowlow a .0242sqMm

4340000 SG4/dl pipe

4940001 6

4840101 0.26426

4340301 3.0 1

4340302 9.02

4940303 16.34

4340304 .23

4340305 14.0 6

43404010.06

43406010.04

4340602 -36.0 5

4340603 0.06

4840701 0.0 4

4340702 .4.8 5

4340703 0.0 6

48403011.0-5 0.58 6

4840901 0.0 0.0 5

43410010010000 6

4941101 0001000 5

4341201002 5.7775646 1.00.00.0 0.0 i

4341202 002 3.77440M6 1.00.00.0 0.0 2

4341203002 5.7684346 1.00.00.0 0.0 3

4841204002 5.7607146 1.00.00.0 0.0 4

434120 002 5.7556416 1.00.00.0 0.0 5

4341206002 5.75084+6 1.00.00.0 0.0 6

4941300 I

4841301 0.0354.35 0.05

SCo•aponem No 485

* S04 Ptessue i-uited Valve

4350000 S04/PRV valve

4850101 484060002436010001 0.2642 1.0 1.00000100

48502011 0.0 3M4.18 0.

4850300 navlv

4350301 706707 0.05 0.54150

*Comsponent No 436

* SG4 Steam Line to the MSIV

* L -ns =6.0 m. Flow am - 0.2642

4360000 St-t- pipe

486OO1 1 4360101 0.2642 I

4360301 6.0 1

4360401 0.0 I

4960601 90.0 1

460701 6.01

4360301 1.0-% 0.8 I"

43610010010000 1

4361201002 5.62668+6 1.00.00.0 001

" Comrponent No 487 " MSIV ftr SG*4

437000 SWV4 valve

4&70101436010002 194010001 0.2642 1.0 1.00000100

4830201 1 0 354.180.

4870300 urviv

4970301402.504 0.2 1.0

*9.16 SG4 B1U-A

* Componet No489

• BRU-4.

4390000 BRU.A4 valve

4990101 434050002 49000 0 0.022361.0 1.00000120

49•01 1 0.0 0.0 0.

4390300 nnrviv 4390301 6096100.0666666667 0.0

• Component No 490

4900000 am tmdpvol

4900101 8.00.070.00.0 0.0 0.0 5.-60.0 0000000

4900200 002

4900201 0.0 1.05*5 1.0

9.16.1 SG4 In-bouse

SComponent No 49l • SG14 bn-bouse

4910000 BRU-n4• valve

4910101 4340500 492000000 0.02236 1.0 1.0 0000120

49102011 0.0 0.0 0.

4910300 mvtv

49103011 187170.0666666667 0.0

Coarponet No 492 * In-House

4920000 bn-04 unpvol 4920101 8.00.070.00.0 0.0 0.0 S.A0.0 0000000

4920200 002

4920201 0.0 S.9168546 1.0

• 10. Hem Structurae

* 10.1Sem Genetaseoa

* 10.1.1.501

b heastre't 110.0

* SGI Her And Cold Collector

1110000020321 0.417

111001000 I

11100101 20.533

11100201 42

11100301 0.0 2

11100400-1

11100401 539.23 566.61 547.26

11100402 558.38 552.40 46.90

11100403 589.22 566.90 547.83

11100404 558.77 5n2.O0 547.38

11100403 589.17 567.03 543.10

11100406 5598.60 552.71 547.72

11100407 589.07 567.00 U431U3

1110040B 558.66 S5L77 547.78

11100409 588.82 566.85 543.07

11100410 559.00 552.91 547.74

11100411 380.36 63.6 54.07

11100412 556.16 551A7 $47.51

11100413 530.24 562.76 547.62

11100414 556.01 550.70 546.12

11100415 579.32 562.64 547.62

11100416 535.5. 550.63 546.11

11100417 579.97 563.69 549.16

11100418 556.08 551.84 543.10

11100419 579.39 563.11 54.41

11100420 55S05 551.63 547.96

11100501 111010000 200000001 10.4452

11100502 112010000 200000001 10.4464

11100503 113010000 200000001 10.4466

11100504 114010000 200000001 10.4648

11100503 115010000 200000001 10.464 10

1II00l50 116010000 200000001 10.245 12

11100507 116010000 200000001 10.2414

11100508 116020000 20000000 1 10.45 16

11100509 116020000 200000001 10.2618

11100510 116020000 200000001 10.5820

11100601 161010000 01 10.445 2

11100602 162010000 01 140.4464

11100603 163010000 0 1 10.4466

D-22
11100604 164010000 0 1 1 0.464 S

11100605 1650100000 10.464 10

11100606 166010000 0 1 10.245 12

11100607 16701000 0 1 10.24 14

11100606 167010000 0 1 0.4516

11100609 163010000 0 1 0.2618

11100610 1690100000 10.5820

111007010 0.00.0 0.0 20

111008010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.020

I1130090 0.0 20.0 20.0 0.0 0.0 0.0 0.0 1.020

" beranniceae 110-1

* SOI Vesnel Level I

111030001 323 15.98

11101100 0 1

11101101 216.13

11101201 62

11101301 0.0 2 11101400 -1

11101401 546.44 539.76 533.14

11101501 161010000 0 1 10.4451

11101601 .20 0 30213 0.445 1

111017010 0.00.0 0.01

111013010.020.020.0 0.0 0.00.0 0.0 1.0 1

111019010.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

* hew muu 110-2

" S04I Vesl Level 2

111020001 321 6.26

11102100 0 I

11102101 26.41

111022016 2

11102301 0.0 2

11102400 .1

11102401 546.74 539.99 533.33

11102501 162010000 0 3 10.4461

11102601 .20 0 302110.446 1

111027010 0.00.0 0.0 1

111028010.020.020.0 0.0 0.00.0 0.0 1.0 1

111029010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.01

b heat Eusntue 110.3

S S04I Vessel Level 3

111030001 321 5.27

11103100 0 1

11103101 25.42

111032016 2

11103301 0.0 2

11103400 -1

11103401 546.68 539.91 533.25

11103501 16301000 0 0 10.4461

11103601 .20 0 3021 10.4461

111037010 0.00.0 0.01

111038030.020.020.0 0.0 0.00.0 0.0 1.0 1

111039010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

* hemsmiti 110-4

* SGO Vessel Level 4

111040001 321 4.86

11104100 0 1

11104101 25.01

111042016 2

11104301 0.0 2

11104400 -1 11104401 5.50 $39.73 533.07

13104501 164010000 0 1 10.464 1

11104601 -20 0 30211 0.4641

311047•10 0.00.0 0.01

11104301 0.020.020.0 0.0 0.00.0 0.0 1.0 3

111049010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

" bet ura.aue 110-5

" SG#1 Vessel Level 3

11105000 1 321 4.75

11105100 0 1

11105101 24.90

111052016 2

11105301 0.0 2

11105400 -1

11105401 546.64 539.,5 533.19

11105501 165010000 0 3 10.4641

11105601 -20 0 3021 &0.4641

111057010 0.00.0 0.01

11105801 0.020.020.0 0.0 0.0 0.0 0.0 1.0 1 11105%010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.01

* beat inru=e 110.6

* soot Vemel Level 6

111060001 321 4.83

11106100 0 1

11106101 24.9A

111062016 2

31106301 0.0 2

11106400 .1 11106401 534.21 526.70 520.20

11106501 166010000 0 1 10.2451

11106601 .20 0 302110.245 1

11106701 0 0.0 0.0 0.0 1

11106901 0.0 20.020.0 0.0 0.00.0 0.0 1.0 1

11106901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 3

• bear muame 110.7 • SO#1VesseILeveI7

111070001 321 5.22

11107100 0 1

11107101 25.37

111072016 2

11107301 0.0 2

11107400 -1

11107401 543.35 536.71 530.16

11107501 167010000 3 10.6501

11107601 -20 0302110.650 1

111077010 0.00.0 0.0 3

11t3078010.020.020.0 0.0 0.0 0.0 0 3.0 

11107901 0.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

• In1cu'ure 110-8

* 0I Vessel Level I

13000031 321 6.07

11108100.0 1

11310101 26.22

11102016 2

11106301 0.0 2

1110400 -I

11103401 $54.91 533.79 532.10

i11005031 163000000 0 10.26 3

11108601 -20 0 302110.26 1

1130703 0 0.00.0 0.01

3310880 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

!1108901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 3

beestummue 110-9

S 804I Vessel Level 9

111090001 321 952

11109100 0 1

11109101 29.67

11109201 6 2

11109301 0.0 2

1110400 -1

11109401 545.67 53.95 532.33

11109501 1690100000 30.581

11109601 -20 0 3021 0.58 1

111097010 0.0 0.0 0.0 1

11109801 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

11109901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

* lrc maeue 120-1

• SGNI Tube Bundles

1120100025421 6-5-3

11201100 0 1

1120101 33.0-3

11201201 43

11201301 0.0 3

11201400 -0

11201401 573.39 567.42 561.83 556.59

11203402 367.86 563.34 559.12 555.16

11201403 563.58 560.14 556.93 553.93

11201404 560.21 557.59 555.15 552,86

11201405 557.61 355.60 553.72 551.9A

11201406 572.93 566.90 561.27 555.97

11201407 567.34 362 58.63 554.68

31201403 563.05 559.63 556.53 553.58

11201409 $59.75 557.21 54.3U 552.63

11201410 557.22 555.30 553.51 55313

11201411 572.10 66.14 560.56 555.32

11201412 566.36 562.00 557.92 554.10

11201413 562.03 531.83 355.85 353.06

11201414 $55.78 556.43 5554.24 552.13

11201415 556.32 554.58 2.96 551.44

11201416 572.12 5 14 560.54 $55.29

11201417 $66.34 561.97 55"7.89 354.06

11201418 561.99 $553.0 555.82 553.02

11201419 538.74 556.39 554.20 $52.15

11201420 556.27 54.54 552.93 551.41

11201421 72.36 M3 561.31 556.07

11201422 567.136 56.74 558.60 554.72

11201423 562.82 559.53 556.46 553.58

11201424 559.50 357.045 554.76 552.61

11201425 556.97 555.13 553.40 551.79 11201501 121010000 0¢00¢ 12160.4289 5

312015M2 1220300010000 1 371.6827 10

11201503 123010000100001 16370.4949•5

11201504 124010000 10000 1 1 6600.792 20

11201505 125010000 10003 1 5327.4133325

11201601 161010000 0 3 12160.4239 S

11201602 1620100000 1 3371.682710

11201603 163010000 0 1 16370.4949 15

11201604 164010000 0 3 1 6600.792 20

11201605 165010000 0 1 5327.4133325

112017010 0.00.0 0.0 25

112018016.5-3 20.020.0 0.0 0.00.0 0.0 1.025 .

11203900 I * I -tewdve word Inm

1120190 0.032720.0 20.0 0.00.0 0.0 0.0 1.0 10.-3 1.43 1.0

25

1I0.1.2 LG2

"beaut gn 210-0

* 03#2 IHo and Cold C*olle=

12100000 20 3 2 1 0.417

12100108 0 1

12300101 20.588

D-23

12100201 42

12100301 0.0 2

12100400 -1

12100401 536.23 56535 547.44

12100402 58.96 5523.59 547.11

12100403 536.20 56.531 547.74

12100404 553.83 552.70 547.40

12100405 586.16 565.56 547.83

12100406 553.63 552.69 547.55

12100407 586.07 565.43 547.32

1210048 553.80 552.73 547.51

12100409 585.86 565.33 547.81

12100410 558.94 552.80 547.51

12100411 577.73 561.50 $4737

12100412 555.12 546.50 539.47

12100413 577.56 56030 545.28

12100414 555.59 549.17 543.61

12100415 577.60 56031 545.28

12100416 555.89 549.29 543.63

12100417 573.99 569.13 553.44

12100413 556.93 554.45 549.97

12100419 579.40 572.02 565.36

12100420 556.95 554.55 549.46

12100501 211010000 200000001 10.4452

12100502 212010000 200000001 10.4464

12100503 213010000 200000001 1 0.4466

12100504 214010000 20000000 1 10.4648

12100505 21501000 200D0000 1 10.464 10

12100506 216010000 200000001 10.245 12

12100507 216010000 20000000 1 10.2414

12100503 216020000 20¢00000110.45 16

12100509 216020000 200000001 10.2618

12100510 216020000 200000001 10.5820

12100601 26301000 0 130.4452

12100602 262010000 0 1 0.4464

12100603 2630100000 1 10.4466

12100604 264010000 0 1 10.4643

12100605 265010000 0 1 10.464 10

12130606 266010000 0 1 0.245 12

12100607 267010000 0 1 10.2414

12100603 267010000 0 1 10.45316

12100609 263010000 0 1 10.26 1$

12100610 269010000 0 1 10.5820

12100701 0 0.00.0 0.0 20

12100801 0.020.020.0 0.0 0.00.0 0.0 1.020

12100901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.020

* beat=uacume 210-1 • S042 Vesnel Level 1

12101000 1 3 2 1 15.98

12101100 0 1 12101101 216.13

12101201 62

12101301 0.0 2

12101400 -1

12101401 546.58 539.93 533.30

12101501 261010000 0 1 10.445 1

12101601 -20 0 302110.445 1

121017010 0.0 0.0 0.0 1

1210111010.020.020.0 0.0 0.00.0 0.0 1.0 3

121019010.0 20.0 20.0 0.0 0.00 0.0 01

b heat mis'we 210.2

* SC42 Vensel Level 2

121020001 321 6.26

12102100 0 1

12102101 26.41

1202201 6 2

12102301 0.0 2

12102400 -1

12102401 546.60 539.98 533.23

12102501 262010000 0 1 10.446 1

12102601 -20 0 302110.446 1

121027010 0.00.0 0.0 1

12102801 0.020.020.0 0.0 0.0 0.0 0.0 1.0 1

12102901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

* bea nsrucure 210.3

* S062 Veel Level 3

121030001 321 5.27

12103100 0 1

12103101 2 5.42

12103201 6 2

12103301 0.0 2

12103400 -1 12103401 546.01 539.22 532.58

12103501 263010000 0 1 10.4461

12103601 -20 0 302110.446 1

121037010 0.0 0.0 0.0 1

121033010.020.020.0 0.0 0.0 0.0 0.0 1.0 1 12103901 0.0 20.0 20.0 0.0 0.0 0.0 0.0 3.0 1

* beu iucum 210-4

S W032 Vessel Level 4

321040001 321 4.86

12104100 0 1

12104101 25.01

121042016 2

12104301 0.0 2

12104400 -1

12104401 546.29 539.59 532.96
12104501 264010000 0 1 1 0.464 1

12104601 -20 0 3021 10.4641

121047010 0.00.0 0.0

12104801 0.020.020.0 0.0 0.00.0 0.0 1.0

121049010.0 20.0 20.0 0.0 0.00.0 0.0 1.01

" beat sme . 210-5

" S62 Vendel Level 5

12105O00 1 321 4.75

12105100 0 I

12105101 24.90

121052016 2

12105301 0.0 2

12105400 -1

12105401 546.17 539.44 532.20

121O5501 2650100000 I 1 0.4641

12105601 -20 0 302110.4641

12105701 0 0.00.0 0.0 1

12105801 0.020.020.0 0.0 0.00.0 0.0 1.0 I

12105901 0.0 20.0 20.0 0.0 0.00.0 0.0 101

h beat umnces 210.6 * SG32 Vessel Level 6

121060001 321 4.83

12106100 0 I

12106101 24.98

12106201 6 2

12106301 0.0 2

12106400 -1

12106401 530.02 524.62 511.45

12106501 266010000 0 I 1 0.245 1

12106601 -20 0 302110.2451

121067010 0.00.0 0.0 1

12106801 0.020.020.0 0.0 0.00.0 0.0 1.0 1

12106901 0.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

b beat s-nssse 210-7

* SG#2 Vessel Level 7

12107000 1 3 2 1 5.22

12107100 0 I

12107101 25.37

121072016 2

12107301 0.0 2

12107400 -I

12107401 541.24 534.33 527.78

12107501 267010000 0 1 1 0.650 1

12107601 -20 0 3021 10.6501

121077010 0.00.0 0.01

12107801 0.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

12107901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 I

* hem s'mnnss 2104

S ,012 Vessel Level 8

12103000•1 32 1 &.07

12106100 0 I

12109101 26.22

121082016 2

12109301 0.0 2

12105400 -1

12106401 542.76 535.62 529.02

12102501 263010000 0 1 10.26 1

12109601 -20 0 3021 1 0.26 1

12108701 0 0.00.0 0.0 I

1210801 0.0 20.020.0 0.00.0 0.0 1.0 1

121039010.0 20.0 20.0 0.0 0.00.00.0 1.01

* be• swucuze 210-9

S S,#2 Vessel Level 9

1210900 1 321 9.52

12109100 0 1

12109101 29.67

1210201 6 2

12109301 0.0 2

12109400 -1

12109401 546.09 538.63 531.28

12109501 269010000 0 I 1 0.58

12109601 -20 0 3021 1 0.58

121097010 0.00.0 0.01

12109801 0.020.020.0 0.0 0.00.0 0.0 1.0 1

12109901 0.0 20.0 20.0 0.0 0.00.0 1.0 1

Sbeat smum 220-1

* SG02 Tube Bundles

1220100025421 6.5.3

12201100 0 1 12201101 3 8.0-3

12201201 43

12201301 0.0 3

12201400 -1

12201401 572.44 566.67 561.27 556.20

12201402 567.50 58.02 558.85 554.92

12201403 56357 560.09 556.85 553.81

12201404 560.43 557.73 555.21 55185

12201405 557.96 555.84 553.86 55202

12201406 571.97.566.12 560.65 55.51

12201407 566.95 56247 $58.29 55437

12201403 563.00 559.57 556.37 553.37

12201409 559.A9 557.26 554.30 552.50

12201410 557.47 555.43 533.53 551.76

12201411 570.98 565.10 559.59 554.43

12201412 565.76 561.36 557.26 553.40

12201413 561.72 55844 55538 552.51

12201414 558.65 556.19 553.90 551.76

12201415 556.29 554.44 552.72 551.11

12201416 $71.33 565.56 560.17 555.11

12201417 566.12 561.79 557.75 553.96

12201418 562.08 55.83 555.80 $52.97

12201419 559.00 556.54 554.26 552.12

12201420 556.61 554.75 553.02 551.40

12201421 571.69 56.5.4 560.36 555.22

12201422 566.54 562.10 557.96 554.08

12201423 62.51 559.15 556.02 553.09

12201424 55939 556.8 554.47 552.24

12201425 556.97 555.03 553.21 551.52

12201501 221010000 100001 2160.4289 5

12201502 222010000 100001 1 3871.6827 10

12201503 223010000 IO0O 1 16370.4949 15

12201504 224010000 IOOO I1 6600.7921 20

12201505 225010000 iOOO 01 5327.413325

12201601 261010000 0 1 12160.4239 5

12201602 262010000 0 1 1 3371.6827 10

12201603 263010000 0 1 16370.4949 15

12201604 264010000 0 1 I 6600.7921 20

12201605 265010000 0 1 1 5327.4133 25

122017010 0.00.0 0.0 25

122018016.5-320.020.0 0.0 0.00.0 0.0 1.025

12201900 1 1tswelve - word 61

12201901 0.0327 20.0 20.0 0.0 0.0 0.0 0.0 1.0 10.-3 1.43 1.0

25

• 10.1.3 S03

b beat smaeae 310-0 SS303 Hot Ad Cold ColleeM"

131000002032 1 0.417

13100100 0 1

13100101 20.588

13100201 42

13100301 0.0 2

13100400 -1

13100401 537.62 56.81 547.16

13100402 559.82 5S2.79 546.33

13100403 537.61 566.11 547.73

1310404 559.69 55292 547,29

13100405 587.58 566.29 548.09

13100406 559.52 553.15 547.74

13100407 587.48 56615 548.11

13100408 559.61 553.21 547.79

13100409 587.27 566.12 548.05

13100410 559.95 553.35 $47.75

13100411 579.14 563.01 548.94

13100412 557.16 551.72 546.A8

13100413 579.01 562.14 547.54

13100414 557.05 551.16 546.06

13100415 578.98 562.13 547.54

13100416 556.96 551.11 546.07

13100417 57.87 568.04 555.00

13100418 $57.61 554.40 550.83

13100419 580.64 572.94 566.11

13100420 557.81 555.38 553.01

13100501 311010000 200000001 10.4O52

13100502 312010000 200000001 10.4464

13100503 313010000 200000001 10.4466

13100504 314010000 200000001 10.4648

13100505 315010000 200000001 1 0.464 10

13100506 316010000 20000000 1 10.245 12

13100507 316010000 200000001 10.2414

131OON5 31602000 200000001 1 0.45 16

13100509 31602000 20000000 1 102618

13100510 316020000 200000001 10.A20

13100601 3610100000 1 0.4452

13100602 362010000 0 1 10.4464

13100603 363010000 01 10.4466

13100604 364010000 0 1 10.4648

13100605 365010000 0 1 0.464 10

13100606 366010000 0 1 10.245 12

13100607 367010000 0 1 0.2414

13100608 367010000 0 1 0.4516

13100609 363010000 0 1 10.2618

13100610 369010000 0 1 1 0 20

131007010 0.00.0 0.0 20

131008010.020.020.0 0.0 0.00.0 0.0 1.020

131009010.0 20.0 20.0 0.0 0.00.0 0.0 1.020

* an=es 310-1 * SG03 Vessel Level 1

131010001 32 1 15.98

13101100 0 1

13101101 2 16.13

13101201 62

13101301 0.0 2

13101400 -1

13101401 546.37 539.70 533.07

13101501 3610100000 1 10.445 1

13101601 -20 0 302110.445 1

131017010 0.00.0 0.01

131018010.020.020.0 0.0 0.00.0 0.0 1.01

13101901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.01

* beat ma 310-2

S 3063 Vessel Level 2

131020001 321 6.26

D-24

131021000 1

13102101 26.41

13102201 6 2

13102301 0.0 2

13102400 -I

13102401 546.63 $39.93 533.27

13102501 362010000 0 I 10.446 1

13102601 -20 0 302110.446 1

13102701 0 0.00.0 0.0

131020010.020"020.0 0.0 0.00.0 0.0 1.0 1

131029010.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

* beat mu•seue 310-3 * S3#3 Vessel Level 3

131030001 321 5.27

13103100 0

13103101 25.42

131032016 2

13103301 0.0 2

13103400 -1

13103401 546.61 .539.84 533.18

13103501 363010000 0 1 1 0.446 I

13103601 -20 0 30211 0.446 I

131037010 0.00.0 0.0 1

13103801 0.0 200 20.0 0.0 0.0 0.0 0.0 1.0 1

131039010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

Sbe=at smuu 310.4

• SG3 Ve•el Level 4

131040001 321 4.86

13104100 0 1

13104101 25.01

131042016 2

13104301 0.0 2

13104400 -1

13104401 546.47 539.69 533.04

13104501 364010000 0 1 10.464 1

13104601 -20 0 3021 10.4641

131047010 0.00.0 0.01

131048010.020.020.0 0.0 0.00.0 0.0 1.0 1

131049010.0 20.0 20.0 0.0 0.00.0 0.0 1.01

" be•a ssuu 310-5

• SG03 Vessel Level 5 13105000 1 32 1 4.75

13105100 0 1

13105101 24.90

131052016 2

13105301 0.0 2

13105400 -I

13105401 546.60 539.82 533.15

13105501 365010000 0 i 10.464 1 13105601 -20 0 30211 0.464 I

131057010 0.00.0 0.01

13105301 0.0220.00.0 0.0 0.00.0 0.0 1.0 I

131059010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

Shest usrne 310.6

SSG#3 Vesne Level 6

131060001 321 4.83

13106100 0

13106101 24.98

13106201 6 2

13106301 0.0 2

13106400 -1 13106401 533.20 526.44 520.21

13106501 366010000 0 I 1 0.245 I

13106601 -20 0 3021 1 0.245 I

131067010 0.00.0 0.01

131063010.020.020.0 0.0 0.00.0 0.0 1 1

131069010.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

* hem smnue 310-7

• S03 Vessel Level 7 131070001 321 5.22

13107100 0 1

13107101 25.37 131072016 2

13107301 0.0 2

13107400 -I

13107401 543.35 536.69 530.14

13107501 367010000 0 1 10.650 1

13107601 -20 0 3021 1 0.650 1

131077010 0.00.0 0.0 1

13107801 0.020.020.0 0.0 0.00.0 0.0 1.0 1

131079010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

b heat smxee 310-8

* SG#3 Vessel Levd e

131080001 321 6.07 1310100 0 1 13106101 26.22

131082016 2

13108301 0.0 2

13108400 -1

13108401 546.08 538.85 532.14

13108501 368010000 0 1 10.26 I

13108601 .20 0 302 10.26 1

131087010 0.00.0 0.01

131083010.020.020.0 0.0 0.00.0 0.0 1.0 1

131089010.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1
Sbeaw icture 310-9

S 6083 Vessel Level 9

131090001 321 9.52

13109100 0 I

13109101 29.67

131092016 2

13109301 0.0 2

13109400 -1

13109401 546.3538.81 532.04

13109501 369010000 0 1 0..58 I

13109601 -20 0 3021 10.58 1

131097010 0.0 0.0 0.01

13109M01 0.0220.00.0 0.0 0.00.0 0.0 1.0 1

131099010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.01

" beat anuctwe 320-I

* SGO3 Tube Budles

132010002542 1 6.5-3 13201100 0 1

13201101 38&0-3

13201201 43

13201301 0.0 3

13201400 -1

13201401 573-56 567.54 561.91 556.62

13201402 568.46 563.78 559.41 555.30

13201403 564.42 560.77 537.36 554.16

13201404 $61.17 558,31 555.65 553.16

13201405 559.59 55635 554.25 552.29

13201406 573.11 567.02 561.33 555.98

13201407 567.94 563.26 558.90 554.80

13201408 S63.88 560.28 556.92 553.77

13201409 560.67 557.89 555.31 552.88

13201410 558.16 556.01 554.00 552.11

13201411 572.27 566.21 560.55 555.23

13201412 566.92 562.37 558.11 554.12

13201413 52.80 559.37 556.17 553.17

13201414 559.62 557.03 554.62 552.35

13201415 557.17 555.21 55338 551.66

13201416 572.36 566.31 560.65 555.34

13201417 566.99 562.44 558.19 554.21

13201418 562.84 559.42 556.23 553.24

13201419 559.64 557.06 554.66 552.40

13201420 557.19 555.23 353.40 551.69

13201421 S73.04 $67.01 561.38 55X09

13201422 567.76 563.17 558.68 554.86 13201423 563.64 560.14 S55. 553.79

13201424 560.41 557.73 555.22 552.67

13201425 557.91 555.84 553.90 552.09

13201501 321010000 10000 1 1 2160.4289 5

13201502 322010000 10000 I 1 3871.6827 10

13201503 323010000 10000 1 16370.4949 15

13201504 324010000 10000 1 1 6600.7921 20

13201505 325010000 10000 I1 15327.4133 25

13201601 361010000 0 1 12160.4289 5

13201602 362010000 0 1 13871.6827 10

13201603 363010000 0 1 1 6370.4949 15

13201604 364010000 0 1 1 6600.7921 20

13201605 365010000 0 1 1 5327.413325

132017010 0.00.0 0.0 25

13201801 6.5-320.020.0 0.0 0.00.0 0.0 1.025

13201900 1 * I -twelve word 1

132019010.032720.0 20.0 0.00.00.0 0.0 1.0 10.3 1.43 1.0

25

1 10.1.4 SG4

b best mKucere 410.0 SS044 lIo and Cold Collector

1410000020321 0.417

14100100 0 i

14100101 20.3588

14100201 42

14100301 0.0 2

14100400 -I

14100401 588.29 565.97 546.89

14100402 558.99 552.26 546.54

14100403 589.27 566.27 547.46

14100404 558.88 552.46 547.01

14100405 588.23 566.42 547.78

14100406 558.71 552.59 547.41

14100407 588.13 566.39 547.80

14100409 558.78 552.6• 547.46

14100409 587.90 56625 547.74

14100410 559.12 552.79 547.43

14100411 S7.64 563.12 548.70

14100412 55623 551.35 547.19

14100413 57931 523 $547.26

14100414 556.09 550.54 545.76

14100415 579.23 562.17 547.26

14100416 S55.99 $50.51 545.75

14100417 5"736 563.04 548.70

14100418 556.21 551.68 547.75

14100419 579.30 562.64 547.96

14100420 556.21 551.64 47.-9

14100501 411010000 200000001 10.4452

14100502 412010000 20000000D 1 10.4464

14100503 413010000 200000001 10.4466

14100504 414010000 200000001 10.4648

141005 415010000 20000000 1 1 0.464 10

14100506 416010000 20000000 1 1 0.245 12

141005 416010000 2000000 1 1 0.24 14

141005M 416020000 2000000 I 0.45 16

1410009 416020000 2000010 1 I 0.26 18

14100510 416020000 20000000 1 10.5820

14100601 461010000 I 10.445 2

14100602 462010000 0 1 10.446 4

14100603 463010000 0 1 10.4466

14100604 4640100000 1 10.4648

14100605 465010000 0 1 I0.464 10

14100606 466010000 0 1 10.245 12

14100607 467010000 0 I 1 0.24 14

14100609 467010000 0 I 1 0.45 16

14100609 468010000 0 I 1 0.26 M1

14100610 469010000 0 I 103820

14100701 0 0.0 0.0 0.0 20

14100801 0.020,020.0 0.0 0.0 0.0 0.0 1.020

14100901"0.0 20.0 20.0 0.0 0.00.0 0.0 1.020

* beanmtrucsure 410-1

64Vessel S Level 1

14101000 1 3 2 1 15.98

14101100 0

14101101 216.13

14101201 62

14101301 0.0 2

14101400 -1

14101401 546.08 539.42 532.91

14101501 461010000 0 1 10.445 1

14101601 -20 0 30211 0.445 I

141017010 0.00.0 0.01

141019010.020.020.0 0.0 0.00.0 0.0 1.0 1

141019010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

b heast ture 410-2

SSG604 Vessel Level 2

141020001 321 6.26

14102100 0 1 14102101 26.41

141022016 2

14102301 0.0 2

14102400 -1

14102401 54639 539.65 533.01

14102501 462010000 0 1 10.4461

14102,01 -20 0 30211 0.446 1

141027010 0.00.0 0.01

141028010.020.020.0 0.0 0.0 0.0 0.0 1.0 1

14102901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0

* beat sucture 410-3

SSC44 Vessel Level 3

141030001 321 5.27

14103100 0 1

14103101 2 5.42

14103201 6 2

14103301 0.0 2

14103400 -I

14103401 54633 539.57 532.92

14103501 463010000 01 1 0.446 I

14103601 -20 0 3021 1 0.446 1

141037010 0.00.0 0.0 1

141038010.020.020.0 0.0 0.0.0 0.0 1.0 1

14103901 0.0 20.0 20.0 U.0 0.00.0 0.0 1.0 1

" bea trucre 410.4

" S64 Vessel Level 4

141040001 321 4.96

14104100 0

14104101 2 5.01

14104201 6 2

14104301 0.0 2

14104400 .1

14104401 546.17 539.41 532.76

14104501 464010000 0 1 10.464 1

14104601 -20 0 302110.464 1

141047010 0.00.0 0.01

141048010.020.020.0 0.0 0.00.0 0.0 1.0 1

141049010.0 20.0 20.0 0.0 0.00.0 0.0 1.01

* bean ucture 410-5

S 6044 Vessel Level

14105W000 1 3 2 1 4.75

14105100 0 1

14105101 24.90

141052016 2

14105301 0.0 2

1410540 -1

14105401 54630 539.3 532.87

14105501 465010000 0 1 10.464 1

14105601 -20 0 302110.4641

141057010 0.00.0 0.01

141058010.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

141059010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.01

" beut muma 410-6

" SG#4 Vessel Level 6

1410600 1 321 4.83

14106100 0 I

14106101 24.98

141062016 2

14106301 0.0 2

14106400 o1

14106401 533.42 526.16 519.85

14106501 466010000 0 1 I 0.245 I

14106601 -20 0 30211 0.245 1

14106701 0 0.0 0.0 0.0 i

14106801 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

141069010.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

SbeI•m ucture 410-7

S O"44 Vessel Level 7

141070001 321 5.22

14107100 0 1

14107101 25.37

141072016 2

14107301 0.0 2

14107400 -1

14107401 542.97 536.33 529.79

14107501 467010000 0 1 1 0.650 1

14107601 -20 0 302110.650 1

14107701 0 0.0 0.0 0.0 1

14107801 0.020.020.0 0.0 0.00.0 0.0 1.0 I

14107901 0.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

" best u 410-8

" SC04 Vssel Level 8

14108000 1 3 2 1 6.07

14108100 0 1

14108101 26.2M

14109201 6 2

14108301 0.0 2

14108400 -1

14108401 545.54 538.81 532.19

14108501 468010000 0 1 10.26 1

14109601 -20 0 302110.26 1

141087010 0.00.0 0.0 1

141088010.020.020.0 0.0 0.00.0 0.0 1.0

141089010.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

*benazurucure 410-9 S* 064 Vessel Level 9

14109000 1 321 932

14109100 0 I

14109101 29.67

14109201 6 2

14109301 0.0 2

14109400 -1

14109401 545.26 53836 531.96

14109501 469010000 0 1 10-58 1

14109601 -0 0 302110.53 I

14109701 0 0.0 0.0 0.0 1

14109901 0.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 I

14109901 0.0 20.0 20.0 0.0 0.00.0 0.0 1.0 1

" beu Woa*ure 420-1

" S6C4 Tube Bundles

142010002542 1 6.5-3

14201100 0 I

14201101 39&0-3

14201201 43

14201301 0.0 3

14201400 -I

14201401 573.22 567.21 561.59 53631

14201402 567.86 563.26 558.96 554.92

14201403 563.67 560.13 556.92 553.73

14201404 560.34 557.62 5.m07 552.69

14201405 557.74 555.63 553.65 551.M 0

14201406 572.76 $66.69 561.01 S5558

14201407 $67.34 56.75 559.46 554.43

14201409 563.14 559.65 556.41 553.36

14201409 559.86 557.22 554.75 552.43

14201410 55733 $55.31 553.42 551.65

14201411 571.92 565.90 560 54•.98

14201412 566.34 561.88 557.71 353.91

14201413 562.09 558.78 555.69 552.80

14201414 559.6 556.40 554.10 551.95

14201415 556.39 55435 5532.84 551.23

14201416 571.97 565.94 560.31 555.02

14201417 566.36 561.90 557.74 $53.93

14201418 562.9 358.78 $535.70 $52.81

14201419 558.84 55639 554.10 551.95

14201420 55637 554.54 55283 551.23

14201421 572.6 56.68 561.06 555.78

14201422 567.16 562.65 558.44 554.49

14201423 562.90 559.51 S5534 553.37

14201424 559.61 557.05 554.,66 552.42

14201425 557.09 555.13 553.32 551.62

14201501 421010000 10000 1 12160.4289 S

14201502 422010000 10000 1 1 3871.6827 10

14201503 423010000 10000 1 16370.4949 15

14201504 424010000 10000 1 1 6600.7921 20

14201505 425010000 10000 1 15327.413325

14201601 461010000 0 I 12160.4299 5

14201602 462010000 0 I I 371.827 10

14201603 463010000 0 I 16370.4949 15

14201604 464010000 0 1 1 6600.7921 20

14201605 465010000 0 1 I 5327.413325

142017010 0.00.0 0.025

14201801 6.5-32 0.0 20.0 0.0 0.00.0 0.0 1.025

14201900 1 0 1 -twelve word bnmm

142019010.0327 20.0 20.0 0.00.00.0 0.0 1.0 10.-3 1.43 1.0

25

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11001401 589.22 584.42 579.91

11001402 539.23 584.42 579.91

11001403 589.23 584.42 579.91

11001404 589.22 584.42 579.91

11001405 589.27 584.41 579.90

11001406 589.27 5K4.41 579.90

11001407 589.26 584.40 579.89

11001408 558.75 554.42 S50.40

11001409 558.75 5S4.42 550.40

11001410 558.76 554.42 550.40

11001411 558.76 554.42 550.40

11001412 558.75 554.42 550.40

11001413 553.75 55,.4A2 50.40

11001414 558.75 554.42 550.40

11001415 558.75 554.42 550.40

11001416 558.75 554.41 550.39

11001417 559.01 554.68 550.65

11001418 559.01 554.68 550.65

11001419 559.00 554.67 550.65

11001420 559.00 554.67 550.65

11001421 559.00 554.67 550.65

11001422 559.00 554.67 550.65

11001423 559.00 554.67 550.65

11001424 559.00 554.67 550.65

11001425 559.00 554.67 550.65

11001426 559.00 554.66 550.64

11001427 558.99 554.66 550.64

11001428 558.99 554.66 55O.64

11001429 558.99 554.66 55O.64

11001501 1O0010OO0 1 11.49 

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11001513 144010000 0 11.5 19

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11001516 144050000 0 1 11.052 23

11001517 1440600000 1 I.522 24

11001518 144070000 0 1 12.5 25

11001519 14408000 0 114.5 26

11001520 1440900000 1 13.5 27

11001521 144100000 0 I 1.2529

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11001609 -200 3021 11.5113

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11001611 -20 0 3021 11.7416

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11001613 -20 0 30211 1.5 19

11001614 -20 0 3021 1 1.052 20

11001615 -20 0 302111.2 222

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11001617 -20 0 30211 .528 24

11001618 -20 0 302112.5 25

11001619 -20 0302114.5 26

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12001402 586.23 581.42 576.96

12001403 536.23 581.42 576.96

12001404 562 581.42 576.96

12001405 5U2 581.42 576.95

12001406 56M 51A1 576.95

12001407 5•862 .511 576.94

12001408 558.84 554.52 550.50

12001409 55S34 554.52 550-50

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12001411 558.4 554.52 5.50.50

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12001416 558.84 55450 550.48

12001417 559.07 554.74 550.72

12001418 559.07 554.74 550.72

12001419 559.07 554.74 550.72

12001420 559.07 554.74 550.72

12001421 559.07 554.74 550.72

12001422 559.07 554.74 550.72

12001423 559.09 554.74 530.72

12001424 559.08 554.74 550.72 12001425 5S9.08 554.74 50.72

12001426 559.07 554.74 550.72

12001427 559.07 554.74 550.72

12001428 559.07 554.74 550.72

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12001505 202030000 0 111.2527

12001506 240010000 0 110.88

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12001510 240070000 0 1 11.052 15

12001511 2400900D0 0 1 1.7416

12001512 24201000 0 12.1075 18

12001513 244010000 0 1 11.5 19

12001514 244020000 0 I 1.052 20

12001515 244030000 0 I II.=52 22

12001516 244050000 0 I 11.052 23

12001517 244060000 0 I 11-.528 24

12001518 2440700000 1 12.5 25

12001519 244080000 0 1 14.5 26

12001520 24409000 0 1 3. 27

12001521 244100000 1 11.2529

12001601 -20 0 302111.49 

I

12001602 -20 0302111.84

12001603 -20 0 3021 I 1.28 

5

12001604 -20 0 30211 .0526

12001605 -20 0 3021I1.2527

12001606 -20 0 302110.18

12001607 -20 0 302111.29

12001608 -20 0 302111.052 11

12001609 -20 0 3021 11.5113

12001610 -20 0 302111.052 15

12001611 -20 0 3021 11.7416

12001612 -20 0 3021 2.1075 18

12001613 -20 0 3021 11.5 19

12001614 .20 0 3021 11.052 20

12001615 -20 0 3021 1.2152 22

12001616 -20 0 3021 1.05 2 23

12001617 -20 0 3021 I.5"28 24

12001618 -200 302112.5 25

12001619 -20 0 3021 14.5 26

12001620 -20 0 302113.5 27

12001621 -20 030211.25 29

12001701 00.0 0.0 0.0 29

120018010.0 20.0 20.0 0.0 0.00.0 0.0 1.0 29

* beae sname 300-1

Loop3

1300100029 3 2 1 0.425

13001100 0 

I

13001101 20.495

13001201 7 

2

13001301 0.0 

2

13001400 -1

13001401 587.64 522.81 578.33

13001402 587.64 582.81 578.33

13001403 587.64 582.81 57833

13001404 587.64 58..81 578.33

13001405 587.63 582.81 57.32

13001406 587.63 582.80 57832

13001407 587.63 582.20 578.31

13001408 559.70 555.36 551.32

13001409 559.70 555.36 55132

13001410 559.71 555.36 551.32

13001411 559.71 555.36 551.32

13001412 559.71 555.36 551.32

13001413 559.71 555.36 55132

13001414 559.70 55535 551.32

13001415 559.70 555.3 551.32

13001416 559.70 55535 551.31

13001417 559.93 555.59 551.55

13001418 559.93 555.59 551.55

13001419 559.93 555.59 551.55

13001420 559.93 555.59 551.55

13001421 559.93 555.58 551.53

13001422 559.93 555.8 551M5

13001423 559.93 555-8 551.55

13001424 559.93 555.58 551.55

13001425 559.93 555.58 551.55

13001426 559.93 555.58 551.54

13001427 559.92 555.58 551.54

1300142n 559.92 555.58 551.54

D-26

13001429 559.92 55.58 51.5.4

13001501 300010000 0 1 11.49 

1

13001502 3000200000 1 11.4

13001503 302010000 0 1 1.28 

5

1300154 302020000 0 1 11.0526

13001505 302030000 0 1 1.2527

13001506 340010000 0 1 10.88

13001507 340020000 0 I 11.29

13001508 340030000 0 I 1.052 I1

13001509 340050000 0 1 11.5113

13001510 340070000 0 1 11.052 15

13001511 340090000 0 1 11.74 16

13001512 342010000 0 1 12.1075 1I

13001513 344010000 0 1 1.5 19

13001514 344020000 0 1 11.052 20

13001515 344030000 0 1 1.252 22

13001516 344050000 0 1 11.052 23

13001517 344060000 0 1 1.528 24

13001518 344070000 0 1 12.5 25

13001519 344080000 1 14.5 26

13001520 344090000 0 1 13.5 27

13001521 3441000000 11.25 29

13001601 -20 0 30211 1.49 

I

13001602 -20 0 3021 11.84

13001603 -20 0 3021 I 1.28 

5

13001604 -20 0 3021 11.0526

13001605 -20 0 3021 I .227

13001606 -20 0 302110.88

13001607 -20 0 302111.29

13001608 -20 0 30211 1.052 II

13001609 -200 30211 1.5113

13001610 -20 0 302111.052 I1

13001611 -20 0 3021 11.7416

13001612 -20 0 3021 1 2.1075 18

13001613 -20 0 3021 115 19

13001614 -20 0 3021 11.052 20

13001615 -20 0 302111352 22

13001616 -20 0 3021 I 1.052 23

13001617 -20 0 302111.522 24

13001618 -20 0 302112.. 25

13001619 -20 0 302114.5 26

13001620 -20 0 302113.5 27

13001621 -20 0 30211.25 29

130017010 0.00.0 0.0 29

130019010.020.020.0 0.0 0.00.0 0.0 1.0 29

* beet sM=a 400-1

* Loop4

140010002932 1 0.425

14001100 0 

1

14001101 20.495

14001201 7 

2

14001301 0.0 

2

14001400 -1

14001401 588.33 583.49 578.99

14001402 58833 583.485 8.99

14001403 58833 583.48 578.99

14001404 58833 583.48 578.99

14001405 58.32 583.47 578.98

14001406 588.31 583.47 578.98

14001407 588.31 583.46 572.97

14001406 558.87 554.54 50.52

14001409 558.87 554.54 550.52

14001410 558.87 554.54 550.52

14001411 558.8 554.54 550.52

14001412 558.87 554.54 550.52

14001413 558.87 554.54 550.52

14001414 558.87 554.54 550.51

14001415 558.87 554.54 550.51

14001416 558.86 554.53 550.51

4001417 559.12 554.79 550.77

14001418 559.12 554.79 550.77

14001419 559.11 554.78 550.76

14001420 559.11 554.79 550.76

14001421 559.11 554.78 550.76

14001422 559.11 554.78 550.76

14001423 559.12 554.78 55076

14001424 559.11 5504.78 55076

14001425 559.11 554.08 550.76

14001426 559.11 554.78 550.75

14001427 559.11 554.78 550.75

14001428 559.11 554.77 550.75

14001429 559.11 554.77 550.75

14001501 400010000 0 1 11.49 

1

1400150 4000200 00 111.84

14001S03 402010000 0 1 1.28 

5

14001504 402020000 0 1 11.0526

14001"50 402030000 0 1 11.2S27

14001506 4400100D 0 1 10.8-8

14001507 440020000 01 11.29

14001508 440030000 0 1I 1.052 11

14001509 44005 0 I 11.5113

14001510 440070000 0 I 11.052 IS

14001511 440090000 1 11.7416

14001512 442010000 0 1 1 2.1075 18

14001513 444010000 0 1 1.5 19

14001514 444020000 0 1 1.052 20

14001515 444030000 0 1 1.252 22

14001516 444050000 0 1I 1.052 23

14001517 4440600000 111-522 24

14001518 444070000 0 1 12.5 25
• I 7" 

1

14001519 444080000 0 I 14.5 26

14001520 444090000 0 1 3.527

14001521 44410000 0 1 11.2529

14001601 -20 0 3021 11.49 

1

14001602 .20 0 30212 2.84

14001603 -20 0302211.21 

5

14001604 -20 0 3021 11.0526

14001605 -20 0 3021 11.2527

14001606 .20 0 3021 10.88

14001607 -20 0 30211 1.29

14001608 -20 0 3022 11.052 H1

14001609 -20 0 3021 11.5113

14001610 -20 0 302111.052 15

140016t1 -20 0 302111.7416

14001612 -20 0 3021 12.1075 1I

14001613 -20 0 302111.5 19

14001614 .20 0 3021 21. 52 20

14001615 -20 0 3021 I 2.252 22

14001616 -20 0 302111.052 23

14001617 -20 0 30212 1.28 24

14001618 .20 0 3021 2.5 25

14001619 -20 0 302114.5 26

14001620 -20 0 3113.5 27

14001621 .20 030211 1.2529

140017010 0.00.0 0.0 29

140018010.020.020.0 0.0 0.00.0 0.0 1.0 29

103 Reacor Vessel

b* smut= 10-1

* Ra Vmel Th'mk Cylindril

101010002042 1 2.068

10101100 0 

I

10101101 12.075

10101102 22.2675

101012014 

1

101012025 

3

10101301 0.0 

3

10101400 -1

10101401 558.97 557.34 546.22 535.61

10101402 558.96 $57.33 •46.21 535.61

10101403 558.96 557.33 546.22 535.61

10101404 558.97 557.34 S46.22 535.61

10101405 558.96 55733 546.21 535.61

10101406 559.02 557.39 546.28 535.67

10101407 559.02 557.39 546.27 535.66

10101408 559.02 55739 546.28 535.67

10101409 559.03 557.41 546.29 535.68

10101410 559.01 557.38 546.27 535.66

10101411 559.86 558.23 547.07 536.42

10101412 559.86 558.22 547.06 536.41

10101413 559.86 558.22 547.06 536.41

10101414 559.85 558.21 547.05 536.40

10101415 559.80 558.16 547.01 536.36

10101416 559.11 557.48 546.36 535.74

10101417 559.11 557.48 546.35 535.74

10101418 559.11 557.48 546.36 535.75

10101419 559.12 557.48 546.36 535.75

10101420 559.14 55731 5. $35.76

10101501 009020000 0 1 1 0.186125 

1

10201502 009030000 0 1 0.26375 

2

10101503 009040000 0 1 0.26375 

3

10101504 009000 0 1 0.25125 

4

10101505 009060000 11 0.20375 

5

101506 010020000 0 11 0.1861256

10101507 010030000 01 0.26375 

7

10101508 010040000 0 0.26375 

8

10101509 010050000 0 1 0.25125 

9

10101510 010060000 0 11 0.206375 10

10201511 011020000 0 11 0.186125 11

10101512 011030000 0 110.2637512

10101513 011040000 0 11 0.2637513

10101514 0110500000 22 0.2512514

10101515 011060000 0 I 0.206375 15

10101516 012020000 02 I 0.186125 16

10101517 012030000 0 1I 0.2637517

10101518 012040000 0 1 1 0.26375 18

10101519 012050000 0 11 0.2512519

20101520 01206000 0 1 1 0.206375 20

10101601 -. 0 03021 2 0.1861251

10101602 .20 0 3021 1 0.26375 

2

10101603 -20 0 3021 1 0O.W75 

3

10101604 -20 0 30211 0.25226 

4

10101605 -20 0 30211 0.206375S

10101606 .20 0 30211 0.18612256

10101607 -20 0 30212 0"265 

7

10101608 -20 0 30212 026375 

8

10101609 -20 0 30212 0.25125 

9

10101610 -20 0 30212 0.2075 10

10101611 -20 0 3021 I 0.186125 11

10101612 -20 0 3021 1 0.26375 12

10101613 -20 0 30211 0.2637513

10101614 -20 0 3021 1 0.2512524

10101615 -20 0 30211 0.2075 15

t0101616 -20 0 30212 0.186125 16

10101617 -20 0 30211 0.2637517

10101618 -20 0 30211 02637518

10101619 -20 0 30211 0.2512519

10101620 -20 0 30212 0.206375 20

101017010 0.00.0 0.0 20

10101801 0.020.0 20.0 0.0 0.00.0 0.0 1.0 20

*beet srocrtre 10.2

R eacto Vessn Thick Cylindrica

1010200016421 1.971

10102100 0 

1

10102101 I 1.978

10102102 22.2=5 101022014 1

1010202 5 

3

10102301 0.0 

3

10102400 -l

10102401 589.29 587.40 56766 549.30

10102402 582.48 $80.71 561.44 543.59

10102403 585.39 583.62 54.10 546.03

10102404 585.37 53.5 564.07 546.01

10102405 557.63 556.01 538.72 522.71

10102406 555.60 554.00 536.87 $21.01

10102407 5515 55 .533921 523.15

10102409 S5.78 556.16 538.86 522.83

10102409 558.99 557.37 $39.97 523.86

10102410 559.06 557.43 540.04 523.92

10102411 559.89 558.27 540.80 524.62

10102412 559.13 557.51 540.10 523.98

10102413 559.01 557.38 539.99 523.87

10102414 559.07 557.44 540.05 523.92

10102415 559.91 5= 540.82 524.63

10102416 559.16 5"573 540.12 524.00

10102501 061010000 0 11 03121

10102502 062010D00 0 1 0.312

10102503 063010000 0 1 0.31 

3

20102504 064010000 0 11 0.314

10102505 001010000 0 1 0.11455

10102506 002010000 0 I 1 0.114,56

10202507 003010000 0 11 0.11457

10102508 004010000 0 11 0.11458

10102509 005010000 0 11 0.369

10102510 006010000 0 1 1 0.36 10

10102511 807010000 0 11 0.36 11

20102512 008010000 0 12 0.36 12

10102513 009010000 0 2 0.2.525 13

10202514 010010000 0 11 0.2525 14

10102515 011010000 0 1 0.22525 15

10102516 012010000 0 I 0.2225 16

10102601 .20 0 30211 0.311

10102602 -20 0 30211 0.312

10102603 .20 0 30211 0.313

10102604 -20 30222 0.314

10102605 -2 0 30212 0.11455

10102606 -20 0 30212 0.11456

10102607 -2 0 30212 0.11457

10102608 20 030211 0.11458

10102609 .20 0 30211 0.369

10102610 -20 0 30211 0.36 10

10102611 -20 0 30211 0.36 11

10102612 -20 0 30211 0.36 12

10102613 -20 0 30211 0.22525 13

10102614 -.20 0 30211 0.2525 14

20202625 .20 30221 022 15

10102616 .20 0 3021 0.22M 16

101027010 0.00.0 0.0 16

20102801 0.020.020.0 0.0 0.0 0.0 0.0 2.0 16

* begt strure 10-3

SResctw Vessel loucm Part

10103000 442 1 3.428

10103100 0 

1

20103101 1 3.435

10103102 2 3.658

101032014 

1

101032025 

3

10103301 0.0 

3

10103400 -1

10103401 576 556.12 543.72 531.75

10103402 557.38 555.82 543.45 531.49

10103403 S5582 550.96 $44.52 532.50

20103404 557.05 555.49 543.14 531.20

10103501 014010000 0 1 10.178 

1

10103502 015010W00 2 10.1712

10103503 0160100M 0 1 10.1783

2010354 017010000 0 1 10.1784

10103601 -20 0 3021 10.178 

1

10103602 .0 0 302110.1782

10103603 .20 0 3021 1 0.178 

3

10103604 -20 0 3021 10.178 

4

10103710 0.010.0 0.04

10103&02 0.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 

4

Sbeat mamoe 10.4

101040003642 1 1.745

10104100 0 

1

10104101 3 1.110

10104201 5 

3

10104301 0.0 

3

10104400 -1

10104401 588.38 58024 572.422 3 564

10204402 585.49 579.29 573.17 567.13

0204403 56.811 579.30 571.90 564.60

20204404 587.43 579.53 571.74 564.07

20104405 U88.98 579.16 569.49 559.96

20104406 585.68 576.96 568.37 559.90

20104407 587.33 5 S.35 569.51 560.79

10104408 587.97 578.54 5•925 560.09 10104409 589.45 579.40 569-51 559.77

10104410 586.09 577.19 .568A1 559.75

10104411 587.74 578.57 560.53 560.61

10104412 588.41 578.76 56926 559.89

10104413 566.23 563.89 56139 559.31

10104414 566.24 563.92 561.63 559.36

10104415 566.45 564.34 56225 560.19

10104416 56626 S6.96 561.69 559.45

10104417 566.24 563.92 $61.63 55936

10104418 56625 563.95 561.67 559.41

10104419 56.46 56437 562.29 560.24

10104420 56628 .563.99 561.73 59.31

10104421 559.33 559.9 559.23 559.18

10104422 559.34 559.31 $59.2 55924

10104423 559.57 559.74 559.90 560.06

10104424 559.37 559.36 55934 55933

10104425 559.33 55928 559.24 559.19

10104426 559.35 559.31 359.2 559.24

10104427 55937 559.74 559.90 560.06

10104423 559.37 559.36 559.35 559.33

10104429 559.34 559.29 55924 559.19

10104430 559.35 559.32 559.29 55925

10104431 559.56 559.73 559.89 560.05

10104432 559.37 55936 559-35 559.33

10104433 559.16 559.17 559.18 559.19

10104434 559.24 55925 559.2 55925

10104435 559.97 560.00 560.01 560.03

10104436 559.33 559.35 559.36 559.37

10104501 0490100000 2 10.1145 

1

10104502 05M10000 0 1 10.1145 

2

10104503 051010000 0 2 10.1145 

3

10104504 052010000 0 1 10.1145 

4

10104505 041010000 0 1 103600 

5

10104506 042010000 0 1 203600 

6

10104507 043010000 0 1I 0.360 

7

10104508 044010000 0 1 0.3600 

8

10104509 037010000 0 1 10.1000 

9

10104510 038010000 0 1 10.108010

10104511 0390100000 1 1 0.100 11

10104512 040010000 0 1 10.109012

10104513 034040000 1 10.11725 13

10104514 034040000 0 1 0.11725 14

10104515 034040000 0 10.11725 15

10104516 0340400000 2 10.11725 16

10104517 034040000 0 1 10.186125 17

10104518 034040000 0 1 10.186125 IS

10104519 034040000 0 1 0.186125 19

10104520 034040000 0 1 0.186125 20

10104521 034030000 0 1 0.26375 21

1020452 034030000 0 1 0.26375 22

10104523 034030000 0 11 0.26375 23

10104524 034030000 0 1 1 0.26375 24

10104525 034020000 0 1 0.26375 25

10104526 03402000 0 1 026375 26

10104527 034020000 0 1 0.26375 27

1010452804020000 0 1 0.2637528

10104529 034010000 0 1 0.25125 29

10104530 034010000 0 1 2025125 30

10104531 034010000 0 1 2025125 31

10104532 034010000 0 1 01 51225 32

10104533 018010000 0 11 020675 33

10104534 019010000 0 1 0,2-6375 34

10104535 020010000 0 12 0206375 35

10104536 021010000 0 2 1 0207536

10104601 001010000 0 1 10.1145 

1

10104602 002010000 0 1 10.1145 

2

10104603 003010000 0 1 10.1145 

3

10104604 004010000 0 1 0.1145 

4

20104605 00501000 0 1 03600 0 

5

10104606 006010000 0 1 203600 

6

20204607 007010000 0 12 03600 

7

20104609 008010000 0 1 103600 

8

10104609 009010000 0 1 0.1080 

9

10104610 010010000 0 1 0.108010

10104611 011010000 0 1 30.2080I1

10104612 012010000 0 1 0.108012

10104613 009010000 0 1 10.11725 13

10104614 010020000 01 20.11725 14

10104615 011010000 0 1 10.11725 15

10104616 012010000 0 1 0.11725 16

10104617 009020000 0 1 0.186125 17

10104618 010020000 0 1 10.186125 18

10104619 011020000 0 1 10.186125 19

10104620 012020000 0 1 10.186125 20

10204621 009030000 0 1 0.26375 21

10104622 010030000 0 11 02637522

10104623 011030000 0 1 102637 23

10104624 012030000 0 1 1026375 24

10104625 009040000 0 1 0.26375 25

10104626 010040000 0 1 0.26375 26

10104627 0040000 0 1 0126375 27

10104628 012040000 0 1 0.26375 29

10204629 009000 0 11 0.25225 29

10104630 010050000 0 1 0.25125 30

10104631 011050000 0 1 10.25125 31

10104632 012050000 0 1 0.25125 32

10104633 009060000 0 1 0206375 33

10104634 0100600000 1 10.206375 34

10104635 011060000 0 1I0.20637535

10104636 012060000 0 1 0206375 36

D-27
L

101047010 0.00.0 0.0 36

101048010.020.020.0 0.0 0.0 0.0 0.0 1.0 36

10104901 0.020.020.0 0.0 0.00.0 0.0 1.0 36

Sb• urucm - 10.5

•Ce mnsvpp pla

10105000 441 10.0

10105100 0 1

10105101 30.2

10105201 S 3

10105301 0.0 3

1010S400 -1

10105401 559.16 559.17 559.16 559.15

101050 559.24 559.26 55925 559.24

10105403 559.97 559.98 559.98 559.96

10105404 559.33 559.34 559.33 559.32

10105501 012011000 0 1 11.875 1

10105502 019010000 0 1 11.17552

10105503 020010000 0 1 11.r753

10105504 021010000 0 1 11.0754

10105601 022010000 0 11 1.875 1

10105602 023010000 0 1 11.752

10105603 024010000 0 1=1753

10105604 025010000 0 1 1 754

101057010 0.00.0 0.04

10105801 0.0 20.02 0.0 0.0 0.0 0.0 0.0 1.0 4

10105901 0.020.020.0 0.0 0.0 0.0 0.0 1.04

* bheazmu-zm 106

* C•e uppa p -5 - -4 plaz

10106000 441 10.0

10106100 0 1

10106101 30.2

10106201 5 3

10106301 0.0 3

10106400 .1

10106401 590.59 590.44 590.29 590.14

10106402 587.28 587.10 586.91 586.71

10106403 58839 588.39 3.38 588.37

10106404 589.60 589.43 59.26 589.08

10106501 030010000 0 1 12.2591

10106502 031010000 0 1 12.2592

10106503 03201000 0 1 12.2593

10106504 0330100000 1 12.2594

10106601 0370100000 1 12.2591

10106602 03801D0000 1 12.2592

10106603 039010000 01 12.2593

10106604 0400100000 1 12.2594

101067010 0.00.0 0.04

10106801 0.020.020.0 0.0 0.00.0 0.0 1.04

101069010.020.020.0 0.0 0.0 0.0 0.0 1.04

" beat meucn 10.7

" Lowa protect,. tube pporctMd pla

10107000 44 1 10.0

10107100 0 i

10107101 3 0.2

10107201 5 3

.10107301 0.0 3

10107400 -1

10107401 590.13 500.11 590.09 590.06

10107402 586.71 58.70 58668 586.65

10107403 588.37 5936 588.34 538.31

10107404 589.07 59.06 589.04 589.01

10107501 037010000 0 1 110.425 I

10107502 038010000 0 1 I 10.425 2

10107503 039010000 0 1 I 10.425 3

10107504 040010000 0 I I 10.425 4

10107601 041010000 0 1 I 10.425 I

10107602 042010000 0 I 110.425 2

10107603 043010000 0 I I 10.425 3

10107604 044010000 0 I 110.425 4

101077010 0.00.0 0.04

10107801 0.020.020.0 0.0 0.00.0 0.0 1.04

101079010.020.020.0 0.0 0.00.0 0.0 1.04

- bewa• = =ssa 10-8

"adnO soiJs no.m.p oo s.s.f left

1010800 44 1 10.0

10108100 0 I

10108101 30.2

101082015 3

10108"01 0.0 3

10108400 .1

10108401 590.06 590.04 590.01 589.98

1010M402 586.65 586.69 586.72 586.75

10108403 588.31 588.31 588.30 588.2

10108404 589.01 589.01 589.01 589.00

10108501 041010000 01 1 3.6 1

10108502 042010000 0 1 13.6 2

10108503 043010000 0 11 31 3

10108504 044010000 0 1 1 3.64

10108601 045010000 0 1 3.6 1

10108602 046010000 0 I 1 3.6 2

10108603 047010000 0 I 1 3.63

10108604 048010000 0 1 1 3.64

101087010 0.00.0 0.04

101098010.020.020.0 0.0 0.00.0 0.0 1.04

1010801 0.0 20.0 20.0 0.0 0.00.0 0.0 1.04

* bea srutlme I1-1

' Pmumtdve Tube

s 60 wbes Din - 0.108. Daen 0.116

10111000 1342 1 0.054

10111100 0 I

10111101 30.058

101112015 3

10111301 0.0 3 10111400 -I

10111401 590.13 590.13 590.13 590.13

10111402 86.70 58670 56.70 586.70

10111403 588.37 58837 58.37 588.37

10111404 589.07 589.07 589.07 589.07

10111405 590.06 590.06 590.06 590.06

10111406 586.65 586.65 58.65 586.65

10111407 58831 53.31 5881 588.31

10111408 59.01 539.01 589.01 589.01

10111409 59.98 589.98 589.98 589.9S

10111410 586.75 .56.75 586.75 536.75

10111411 5.2 538 S2 55288

10111412 S89.00 589.00 $39.00 589.00

10111413 589.20 539.20 589.20 589.20

10111501 037010000 0 I1 6.481

10111502 033010000 01 I 6.482

10111503 039010000 01 I 6.483

10111504 040010000 0 I 1 6.484

10111505 041010000 0 122.035 5

10111506 042010000 0 1 122.035 6

10111507 043010000 0 122.0357

10111508 044010000 0 1 122.0358

10111509 045010000 0 1 131.599

10111510 046010000 1 131.59 10

10111511 0470100000 1 131.59 I1

10111512 048010000 0 1 131.59 12

10111513 054010000 0 1 1 952 13

10111601 037010000 0 I1 6.481

10111602 038010000 0 11 6.482

10111603 039010000 0 11 6.483

10111604 040010000 0 11 6.484

10111605 041010000 0 1 122.035 5

10111606 042010000 0 1 122.035 6

10111607 043010000 0 I 122.035 7

10111608 044010000 0 1 122.035 8

10111609 0450100000 I 131.599

10111610 046010000 0 1 131.59 10

10111611 047010000 0 1 131.59 II

10111612 048010000 0 I 131.59 12

10111613 054010000 0 I 195.52 13

101117010 0.00.0 0.0 13

101118010.020.020.0 0.0 0.00.0 0.0 1.0 13

101119010.020.020.0 0.0 0.00.0 0.0 1.0 13

* be•awua= 11-2

• Prtmive Tubes

* 61ubesDiuO.180kDoue0.116

10112000 1342 1 0.090

101121000 1

10112101 30.095

101122015 3

10112301 0.0 3

10112400 -1 10112401 590.13 590.13 590.13 590.13

10112402 5O6.70 586.70 580.70 586.70

10112403 53837 58837 583 538.

10112404 589.07 539.07 589.07 5W9.07

10112405 590.06 590.06 590.06 590.06

10112406 586.65 596.65 586.63 586.63

10112407 59831 538.31 588.31 58831

10112408 589.01 589.01 53.01 59.01

10112409 589.98 589.98 589.98 539.98

10112410 586.7S 586.75 586.73 536.75

10112411 588.28 5882 588.28 5•8.2• 10112412 589.00 589.00 589.00 589.00

10112413 589.20 589.20 589.20 589.20

10112501 037010000 0 11 6I- 1

10112502 038010000 0 11 &6588 2

10112503 039010000 0 1 I 6.588 3

10112504 0010000 0 1 I 6.588 4

10112505 0410100000 1 122.402 5

10112506 04201000 0 1 122.402 6

10112507 043010000 0 1 122.402 7

10112508 0440100000 I 122.4028

10112500450100 0 1 132.1179

10112510 046010000 I 132.11710

10112511 047010000 01 132.11711

10112512 048010000 0 1 132.11712

10112513 054010000 0 1 197.11213

10112601 037010000 0 11 6.588 I

10112602 038010000 0 I 1 6.588 2

10112603 039010000 0 11 6.588 3

10112604 04001000D 0 11 6M 4

10112605 041010000 0 1 122.402 5

10112606 0420100000 1 122.4026

10112607 043010000 0 1 122.402 7

10112608 044010000 0 1 122.402 8

10112609 045010000 0 1 132.117 9

10112610 046010000 0 1 132.11710

10112611 047010000 0 I 132.11711

,10112612 04M100000 1 132.11712

10112613 0540100000 1 197.11213

10112701 0 0.00.0 0.0 13

101128010.020.020.0 0.0 0.00.0 0.0 1.0 13

D-28

101129010.020.020.0 0.0 0.00.0 0.0 1.0 13

1 !0.4 COM

Sb• smuuctme 26-1

* 40.7S FA contspoodgt oloop 1: Q 0245632

10261000109211.2-3

1026110001

10261101 43.785-3

10261102 1 3.M60-3

10261103 3 4.565-3

10261201 14

10261202 -3 5

10261203 -2 8

10261301 1.04

10261302 0.08

10261400-1

10261401 1173.1154.1105.1034.94.5.5 88.581.46375.21

10261402 1674.1628.1513.1352.1164.624.611.8 600.4

589.65

10261403 1725.1675. 1553.1382. I I. 630.6 61.2 606.5

595.3

10261404 1683.1636.1520.1358L 1170. 633. 621.1 609.8 599.1

10261405 158&.1540.1439.1299.1132.632.621.5 611.1

601.26

10261406 1397.1368.1293.1187.1058. 627.0617.9 609.3

601.1

10261407 1209. 1189. 113&. 1063.970.2 620.1 613. 606.3

599.93

10261406 1044. 1031. 997. 947. U4.0613.3 608.1 603.14

59.44

10261409 867.1860.1842.2 815.5 781.2 60.1 601.9 598

595.9

10261410 707.8 7053 698.8 688.9 676.1 59.9 595.5 594.3

593.0

102615010 0 0 14488.04210

10261601 026010000 10000 1 1 4488.042 10

1026170110026 0.08623 0.0 0.0 I

10261702 10026 0.14930 0.0 0.02

10261703 10026 0.154600.0 0.03

10261704 10026 0.14930 0.0 0.04

10261705 10026 0.13670 0.0 0.05

1026170610026 0.11360 0.00.06

10261707 10026 0.08333 0.0 0.07

10261708 10026 0.06519 0.0 0.08

10261709 10026 0.03996 0.0 0.09

10261710 10026 0.01682 0.0 0.0 10

10261901 0"0114920.020.00.00.00.00.0 1.0 10

* be gr= 27-1

* 40.73 FAe orrqpt tLop 2.Q.246615 Q 

10271000 10922 11.2-3

1027110001

102711014 3.735-3

10271102 1 3.860-3

10271103 3 4.55-3 10271201 I 4

1027102-3 5

10271203 -2 8 10271301 1.04

10271302 0.08

10271400-1

10271401 1103. 1087.1045. 931 908 591.1 584.9 579.0

5735

10271402 1535. 1496. 1402.1268.1 I10. 616.6606.595.9

586.29

10271403 1577.1537.1436.12935.1128.622.8611.7601.3

591.

10271404 1542.1504. 140L 1275. 1116. 625.614A.604.3

594.71

18271405 1455. 1422.1339.1222. 1081. 624.5 614.7 605.5

596.7

10271406 1298.1274.1212.1122.1012.619.7611.6603.9

596.7

10271407 1135. 110. 1074.1011.931.7613.6607.26013

595.6

1027140 989.979.6 949 907.8,52.8A607.5 602.9 5985

594.27

10271409 833.2 827.3 811.9 78.8 759.1600.2 597.3 594.6 592.0

10271410 691.7 689.5 683. 675.2 664.592. 591.68 590.6

589.47

102715010 0 I 4438.042 10 10271601 027010000 10000 I 1 4438.042 10

10271701 10027 0.08623 0.0 0.0 I

10271702 10027 0.14930 0.0 0.02

10271703 10027 0.15460 0.0 0.03

10271704 10027 0.14930 0.0 0.04

10271705 10027 0.13670 0.0 0.0 5

1027170610027 0.11360 0.0 0.06

10271707 10027 0.08833 0.0 0.07

10271708 10027 0.06519 0.0 0.08

10271709 10027 0.03996 0.0 0.09

10271710 10027 0.01682 0.0 0.0 10

102719010.0114920.020.00.0"00.0 01.0 10

* begt smast 28-1

* 40.75 FA eoeqmosdif to Loop 3. Qa 0.256065

10221000 1092 1 1.2-3

10201100 0 1

102811014 3.785-3
10281102 1 3.840-3

10281103 3 4%5-3

10281201 14

10281202 -3 5

10281203 -2 3

10281301 1.04

10281302 0.08

10281400-1

10281401 1212.1096.1053. "91.5 914.0 92.3 386.0 580.1

574.4

10282402 1552. 1513. 1416,1279. 1117. 6183 607.4 597.2

587.5

10281403 1396.1555. 1452. 1306. 1136. 624.5 613.262.

592.6

10281404 1560. 1520. 1423. 1285.1123. 6M.7615.9 605.7

595.9

10281405 1471. 1437.13n2. 1232. 1088.626.2616.3 606.9

398.0

10281406 1312 1286. 1223.1131. 2018.621.3613.1 6053

597.9

1028140W 1145.1127.1083. 1013.937.0613.0608.6602.6

596.8

10281408 997.1 985.7 96.3 912.68257.3 608.9 604.2 399.7 595.3

10281409 838.1 8320 816.3 792.7 762.4 601.3 398.6 59A5.

593.2

10281410 6943 692.1686.3 677.6 666.1 594.1 592.9 591.7

590.6

1028150t 0 00 1 44,o.042 10

10281601 028010000 10000 1 I 4488.042 10

10281701 10028 0.08623 0.0 0.0 1

10281702 10028 0.14930 0.0 0.02

10282703 10028 0.15460 0.0 0.03

1028170410028 0.14930 0.0 0.04

10281705 10028 0.13670 0.0 0.05

10281706 10028 0.1160 0.0 0.06

10281707 10028 0.08833 0.0 0.07

10281708 10028 0.06519 0.0 0.08

10281709 10028 0.03996 0.0 0.09

10281710 10028 0.01682 0.0 0.0 10

10281901 0.01149 20.0 20.0 0.0 0.0 0.00.0 1.0 10

b heat stu'cture 29-1

* 40.75 FA coespoding to Loop 4: Q0.2 1688

10291000 1092 11.2-3

1029110001

10291101 4 3.785-3

10291102 1 3.0-3

10291103 3 4.565-3

10291201 14

10291202 -3 5

10291203 -2 8 10291301 1.04

10291302 0.08

10291400.1

10291401 1149.1131.1085.1017.933.1393.8 S97.1 380.8

374.8

10291402 1626.1583.1474.1323.1146. 621.5 609.9 599.0

588.6

10291403 1673. 1627.1512. 1352. 1165.628.1616.1604.8

394.1

10291404 1634.1390.1482.1330.112.-630.5618.9608.1

397.7

10291405 1337. 1499. 1405.1273. 1125.'629.9619.3609.3

599.9

10291406 1364.1336. 1266. 1165. 1042.624.6 6159 607.6

599.7

10291407 1183. 1165. 2116. 1045.957.3 618.0 611.2 604.7

598.6

10291408 1026.1013.81.1933.7873.5611.5606.4601.7

597.1

10291409 855A 149.832. 806.5 773.8 03.3 600.4 597.5 394.7

10291410 702.4700.0693.8684.4672.1 59S.794.4 393.1 392.

10291301 0 00 1 4488.04210

10291601 029010000 10000 12 4488.042 10

1029170110029 0.08623 0.0 0.0 1

10291702 10029 0.14930 0.0 0.02

10291703 10029 0.12560 0.0 0.03

10291704 10029 0.14930 0.0 0.04

10291705 10029 0.13670 0.0 0.05

1029170610029 0.11360 0.0 0.06

10291707 10029 0.08833 0.0 0.07

10291708 10029 0.06519 0.0 0.08

10291709 10029 0.03996 0.0 0.09

10291710 10029 0.01682 0.0 0.0 10

10291901 0.0114920.020.00.00.00.00.0 1.0 10

* 10.3 Pressurimis lastrs

* bes:stucture 504-1

*PR.Z keers Group No I

* Number of Blocks-33 Power. 270 kW, D- 13 mc.

Lea,•t of I Reaste 1.90S m

F -. 3"9*0.0777- 2.4079sq.mHaeq-51.3678m

0•341000 14210.0

130411000 1 130411013 13.0-3

15041201 43

15041301 1.03

1I041400-1

15041401 617.89 617.89 617.89 617.89

230415010 00 1 51.36782 15041601 50402000012 0 51.3678 1

15041701 501 1.0 0.0 0.0 1

150419010.020.020.00.00.00.00.0 1.0 1

* seat ucmure 504-2

IP hecates Oroup No 2

* Number ofnlocks .3; Power. 270kW. D - 13 mn.

Least of I Na -er 1.905 ma * F- 3"9"0.0777. 24079sqIeq=1.S3678m

I2042000 14210.0

I204210001

2142102 3 13.0-3 15042201 43

13042301 1.03

15042400. 1

15042401 617.89 617.89 617.89 617.19

130425010 00 1 5136781

15042601 30402000001 1 513678 2

134-2701 0 1.0 0.0 0.0 1

13042901 0.020.020.00.00.00.00.0 1.0 2

* heat stuure ,04-3

* PRZ beatr Omup No 3

" Number ofBkoclzk-* Power- 720kW. D 13 UM,

" Leat of I Heater = 1.905 m

" F 8-9*0.077.W $.3944W ar Hateqt 136.981 m

13043000 14 2 10.0

15043100 0 1

130431013 13.0-3

15043201 43

15043301 1.03

13043400 .1

15043401 617.89 617.89 617.89 617.19

143301 0 0001 136.9812

15043601 30402000001 1 36.901 1

15043701 503 1.0 0.0 0.0 2

2543901 0.0 20.0 20.0 0.0 0.0 0.0 0.0 1.0 1

I bear . 304.4

*R Pbevers Grou No 4 N 1unmber ofBloc• - 14:.PWer- 1260kW, D 13 M.

Length of I Eater -= 1.903 c

* F- 1490.07*7. 9.7902sq.m= Ilq239.7167m

15044000 14210.0

1504410001

15044101 3 13.0-3

15044201 43

23044301 1.03

13044400-1

15044401 617.89 617.89 617.89 617.89

150445010 00 1 239.7167 1

13044601 50402000001 1 239.71671

15044701 304 1.0 0.0 0.0

15044901 0.020.020.00.00.00.00.0 1.0 1

* 11. Thera Poeties

20100100tbt/f•cl I 1 *U02

20100200 bdftm I 1 'Zrl%Ni

20100300thbVktu3 1 *OGasinveaprodIboaomI

20100400 tbVfctn I 1 0 Stainless Steel. 0SX13HIOT

20100500 tbVfct 12 * SveeL. 1X2HMA (P.vese=)

20100600tbft 1 * Steel, 22k (as vessel and p7)

201000 /tbtft I 1 * MCP, SG-v. PUZ-v. PIZ surge md

20100800,bl/2fim I *Iab0so

* U02 Tr Cedutiviy

20100101 300.08.15

20100102 500.0 6.70

20100103 700.0 5.40

20100104 00.0 440

20200105 1100.0 3.75

20100106 1300.03.23

20100107 1300.02.80

20100108 1700.0 2.3

20100109 1900.02.40

20100110 2100.02.42

20100111 2300.02.44

20100112 2500.02.50

20100113 2700.02.65

20100114 2900.0390

20100115 3100.0330

20100116 3120.03.44

20100117 3120.1 11.00

SZrlNi Th aW Cnductivity

20100201293.0 17.2

20100202 373.0 18.0

20100203 473.0 193

2020024 373.0 20.1

20100203 673.0 20.3

20100206 773.0 20.9

20100207 873.0 21.2

2010020 973.0 22.0

20100209 1273.0 27.8

20100210 1373.0 29.0

20100211 1473.0 30.1

20100212 1573.0 31.2

20100213 1573.01 343222

20100214 1673.0 37.7650

D-29

20100215 1773.0 41.6875

20100216 2173.0 46."357

20100217 1973.0 51.1556

20100218 2073.0 56.7933

20100219 2173.0 36.0000

20100220 3500.0 36.0000

- CAP therms] conducrvty

20100301 helium 0.68

20100302 umon 0.27

20100303 krypton 0.05

SStainless Steel theral conductiviy

20100401 273.0 16.:9 - 3.52 16.9

20100402 373.0 16.9 * 13.52 169

20100403 473.0 2&2 * 14.A8 I&8

20100404 573.0 19.5 - 15.60 19.5

20100405 673.0 203 * 16.64 203

20100406 3073.0 20.3 * 16.64 20.3

- Steel termal cooductivy

20100301 273.0 39.8

20100502 373.0 39.8

20100503 673.036.8

20100504 3073.0 36.8

- SG Vessel & PRZ Steel therml conductivity

20100601 273.049.3

20100602 373.0 49.3 12010D603 673.043.4

20100O604 3073.0 43.4

MCP. SO-v. PUZ-v. PRZ surge sMd isg. le.

Ssnteel 10GH2FA ihem conductivity

20120702 273.034.0

20100702 373.0 34.0

20100703 473.039.0

20100704 37.0 40.0

20100705 673.042.0

201007063073.042.0

* Absorber ibermal conductivity

20100801 273.00.2

20100802 3000.0 0.2

: U02 volummtc beas apacity

20100151 298.152.43447+6

20100152 300.00 2.46547+6

20100153 400.002.3393.6

20100154 500.D 2."29.6

20100155 600.00 3.05383.6

20100126 700.00 3.09464+6

20100157 800.00 3.1255246

20100158 900.003.13616.6

20100159 1000.03.19162.6

20100160 1100.03..3473+6

20100161 1200.0 328729#6

20100162 1300.033.3039.6

20100163 1400.03.42468.6

20100164 1500.03-31071.6

20100165 1600.03.60877.6

20100166 1700.03.71914.6

20100167 1800.03.84198.6

20100168 1900.0 3.9•44+6

20200169 2000.04.1225636

20100170 2100.04-216"+6

2010017M 2200.04.4603536

20100172 2300.04.64706.6

20100173 2400.04.14666+6

20100174 2500.0 3.05922.6

20100175 2600.0528476.6

20100176 2700.0 5.52329#6

20100177 29.0 5.77488.6

20100178 2900.06.03947.6

20100179 3000.0631710+6

20100180 3100.0 6.0778+6

201001821 3123.06.67647.6

20100182 3123.01 3.0M559.6

• Zrl%,Nri smeice best apac*y

20100251273.0 186360.0

20100252 373.0 1863680.0

20100253 473.0 1963880.0

20100254 373.0 2096240.0

20100255 673.02227790.0

20100256 73.0 2384750.

20100257 873.0 2573290.0

20100258 973.0 2889970.0

20100259 1073.03115060.0

20100260 1173.0 3940700.0 20100261 12300.02059640.0

20100262 1400.0 2094790.0

20100263 1500.02137440.0

20100264 1600.0 2127M0.0

20100265 1700.02238050.0

20100266 1800.02293690.0

20100267 1900.02351660.0

20100268 2000.02411340.0

20100269 2100.02564930.0
20100270 2133.0 258*60.0

20100271 2133.1 3058870.0

20100272 3500.0 3058870.0

* GAP volumntri beat capacity

20100351 225.0 549.0

20100352 10000.0 549.0

* Stainless Steel volume bent capacity

20100451 273.0 3.9.6

20100452 373.0 3.946

20100453 573.0 4244

20100454 673.0 4.3346

20100455 3073.0 4.34

* Steel veoumetric beat cpmay

20100551 273.0 3M.46

20100552 373.0 3.89+6

20100553 473.0 3.9546

20100554 573.0 4.28'6

20100555 673.0 4.S2+6

20100556 3073.0 4-52+6

* SO Veed & PRZ Steel volumb-ic hee capaciy

20100651 273.0 3.8746

20100652 373.0 3.87+6

20100653 673.0 4.M346

20100654 3073.0 4.2346

* MCP, SG-v. PZ-v. PUZ suv and ing. lie

steed IOG2M A hee capacity

20100751 273.0 3.7807+6

20100752 373.0 3.7807+6

20100"53473.04.1186

20300754 573.04.4723#6

20100755 673.0 4.•57546

20300756 3073.04.357546

: Absorber beat capacY

20100851 273. 500.0

2100N52 2000.0 50O.0

IL eator KCinetics

30000000 poit sepmara

3000001 ammsmýa 2917.0+6 0.0 286.0 1.10.65

30000002 &ms79-4

30000101 0.029 0.0124

30000102 0.211 0.0305

30000103 0.191 0.111

30000•04 0.328 0.301

30000105 0.135 1.14

30000106 0.046 3.01

30000401 2917.0+6 650.0 day

30000011 3110

30000703 026010000 0 0.2118-1 0.0

30000702 026020000 0 0.3663.1 0.0

30000703 026030000 00.3797-1 0.0

30000704 0260400 0 03668.3 0.0

3000705 026050 0 00335 -I 0.0

300007 026060000 0 0.2790-1 0.0

30000707 026070000 0.2170.1 0.0

30000708 026080000 0 0.601-1 0.0

30000709 026090000 0 0.9815.2 0.0

30000710 026100000 0 0.4133-2 0.0

30000711 027010000 0 0.2126-1 0.0

3000712 027020000 0 0.362-. 0.0

30000713 027030000 0 03312.3 0.0

30000714 027040000 0 O0.362.1 0.0

30O00715 02700000 0 03371-1 0.0

30000716 027060000 0 0.2801-1 0.0

30000717 027070000 00.217S-1 0.0

3000718 027030000 0 0.160W1 0.0

30000719 027090000 0 0.9MS4-2 0.0

30000720 027100000 0 0.4149-2 0.0

30000721 028010000 0 0.220.1 0.0

30000722 028020000 0 0.3823 0.0

30000723 028030000 0 0.39581 0.0

30000724 028040000 0 0.323-1 0.0

30000725 028050000 0 0.35001 0.0

30000726 028060000 0 0.29031 0.0

30O00727 023070000 0 0.2262-1 0.0

30000728 022080000 0 0.1669.1 0.0

30000729 028090000 0 0.30231 0.0

30000730 028100000 0 0.43- 0.0

30000731 029010000 0 0.2170.1 0.0

30000732 029020000 0 0.3758-1 0.0

30000733 029030000 0 0.3890-1 0.0

30000734 029040000 0 0.3758 00

30000735 029050000 0 0.34411. 0.0

30000736 029060000 0 0.2 I 0.0

30000737 029070000 0 0.223-1 0.0

30000738 029080000 0 0.1641-1 0.0

30000739 029090000 0 0.3006-1 0.0

30000740 029100000 0 0.4234-2 0.0

30000801 0261001 00.2118-1 0.0

30000802 0261002 00.3668-1 0.0

30000803 0261003 003797-1 0.0

30000804 0261004 00.36681 0.0

30000805 0261005 003358. 0.0

30000806 0261006 00.2790.1 0.0

30000807 0261007 00.2170.3 0.0

300008 0261008 0 0.1601-1 0.0

30000809 0261009 00.9815-2 0.0

30000810 0261010 00.4133-2 0.0

30000811 0271001 00.2126-1 0.0

30000812 0271002 00.3682-1 0.0

30000813 0271003 00.321 0.0

30000814 0271004 00.36O2-1 0.0

30000815 0271005 00.3371-1 0.0

30000836 0271006 00.2801-1 0.0

30000817 0271007 00.2178-1 0.0

30000838 0271008 00.1608-1 0.0

30000919 0273009 00.9854-2 0.0

3000080 0271010 00.4149-2 0.0

30000D821 02831001 00.2203-1 0.0

30000822 0281002 00.3823-1 0.0

30000323 021003 00.39581 0.0

3008 0281004 00.38231 0.0

30 2 0281005 00.35•00 0.0

3o000026 0281006 0 02908-1 0.0

3008 0281007 00.2262-1 0.0

3000088 02810080 0.1669-1 0.0

3000329 0281009 00.1023-1 0.0

30000830 0281010 00.4308-2 0.0

30000831 0291001 00.2170-1 0.0

300D0832 0291002 00.3758.1 0.0

30000833 0291003 00389061 0.0

30000834 0291004 00.3758-1 0.0

30000835 0291005 003441-1 0.0

30000836 0291006 00.258.3I 0.0

30000837 0291007 00.22231 0.0

30000838 0291008 00.1641-1 0.0

300008"9 0291009 00.1006-1 0.0

300000 0291010 00.4234-2 0.0

SDekTreacviy Uble

cdcoo moderator reactivitY

3000050 100.0 0.0

30000502 150.0 0.0

30000503 200.0 0.0

30000"54250.0 0.0

3000050 300.0 0.0

3000006 350.0 0.0

30O00507 400.0 0.0

30000508450.0 0.0

30000509 500.0 0.0

300M0510550.0 0.0

30010011600.0 0.0

30000512650.0 0.0

30000513 700.0 0.0

30000514 750.0 0.0

30000513 800.0 0.0

300016 850.0 0.0

3000601 400.00.0

3000602 600.00.0

30000603 800.0 0.0

30000604 1000.0 0.0

30000605 1200.00.0

30000606 1400.0 0.0

3000•067 1600.00.0

30000608 1800.0 0.0

0 13. Reacter Power

SctatvaN 26

* Power of40.7$ FA comrspondinal the Loop I

*Q. 0.2664314

20O502600 Pow-Lpl 0.2664314 777.18039346 0

20O02601 0.0 1.0'lotpow 0

o caelvr N 27

• Powr of 40.75 FA comevepdie to hbe Loop 2

Q- 0.2367771

20502700 Pow-WLp2 t 0.2367713 690.68007M46 0

205027010.0 1.0 ikspow 0 , caervw N 28

* Powarof40.75 FA cmoespoodi t the Loop 3

Q- 0.2404831

20502800 Pow.Lp3 sum 0.2404I 701.4892027"6 0

20"02803 0.0 1.0 slepow 0

o caulverb 29

* Powero(40.7S FA cwespoodtto gtteLoop4

*Q= 0.2563084

20502900 Pow.-Lp4 sm 02563084747.653602846 0

20S02901 0.0 1.0loapow 0

• 13.1 PRZ Hemoas Power

"TableNo 501

* GroupNo 1

20250100 power 621

20250101-13.00.0

20250102 0.0270.0+3

* Table No 502

* GroupNo 2

20250200 power 624

20250201 -3.0 0.0

20250202 0.0 270.0+3

* Table No 503

SGroupNo 3

20250300 power 627

20250301 -1.0 0.0

20250302 0.0 720.0+3

* Table No 504

* Orop No 4 20250400 power 630

20250401 -1.0 0.0

2025•402 0.0 1260.0+3

: 13.2 SCRAM

*Ta"lNo 10

* Reactvy aft SCLAM

20201000 rA 617

20201001 -1.0 0.0

20201002 0.0 0.0

20201003 0.4 0.0

20201004 0.8-0.65

20201005 1.2-1.03

20201006 1.6-1.40

20201007 2.0-1.64

20201008 2.4-1.87

20201009 2.8-,46

20201010 32 -3.39

20201011 3.6-5.73

20201012 4.0-9.01

20201013 4.4-11.70

*TablNo II

• React* oforoup 10

, InitialpositionHfl-8% 312.4 Mc ofboltorm

*Velocity 20 Out/ 20201100 reaw 616

20201101 -1.0 0.0 t Ro

202011020.0 0.0000 * 0.00.0

202011031.0-0.0122 0.5 -.0.00099I

202011042.0-0.0236 * 1.0 -0.0011041

20201105 3.0-0.0343 • 1.5 -0.0017350

202011064.0-0.0444 12.0 -0.0023659

202011075.0-0.0540 02.5 .0.0028391

202011086.0-0.0631 *3.0 -0.0034700

202011097.0-0.0719 3.5 -0.0041009

202011108.0-0.0901 '4.0 -0.0047319

20201111 9.0-0.0882 *4.5 -0.0053628

20203112 10.0-.095 * S0.0.0058360

20201113 1l.0-.0.033 $53 -0.0064669

20201114 12.0-0.1104 *6.0 -0.0070978

20201115 13.0-0.1174 *6.3 -0.0077287

20201136 14.0-0.1244 *7.0 -0.0082019

20201117 15.0-0.1316 *7. .0.0088328

1 34. Coutinet parameter

*Table No 20

*Cooauimnattemperanare

202020D0 tew

20202001 0.0 330.0

'Table No 21

* He Tranms Coe-ficiet with Containmet

20202100 abo20202101 0.0 20.0

.I- ed input deckD-30
NBC FO. US6 U.S. NUCLEAR REGULATORY COMMSSION I. REPORT NUMER

(24G) PMh by WC. Add VOL. SuM . R-..

2M1.3= BIBUOGRAPHIC DATA SHEET , id, N r,.J

¢sos a• mauve,.)

2. TITLE AND SUBMITrLE m wtwan"vw)I NRGA06

Assessment Study of RELAPS/MOD3.2 Based On the Kalinin

NPP Unit- I Stop of Feedwater Supply to the Steam Generator No. 4 WATE C REPORT PUSUSHED

MOT YMA

October 1999

4. FIN OR GRANT NUMBER

W6500

6. AUT10oR(S) 6. TYPE OF REPORT

S. S. Pylev Technic

7. PERIOD COVERED Prl=k O.J@i. 

6. PERFORIING ORGANIATION - NAAV AND ADDRESS Vr PVovme aft* a-R•gm U.S. M,•mbWRavCaI,,.S*A2 aim adeusav Iezr~hctc

Russian Research Center - Kurchatov Insttute

Kurchatov Square I

Moscow 12382

Russia

9. $PONSOiRNG ORCINtIZATION - NAME AND ADDRESS prNR. 4ae "Swas sbow Foo, for, . prv~d, ARCDkk. Offi crP gxn .&OS Nuc€vfguJ•fy C*mrwzi

Division of Systems Analysis and Regulatory Effectiveness

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington. DC 2055540001

10. SUPPLNTARY NOTE

11. ABSTRPACT g:oW ads cr w)

This report has been prepared as a part of the Agreement on Research Partdcipation and Technical Exchange under the Code

Assessment and Maintenance Program. The data collected by Kalinin NPP Unit-1 Data Acquisition System and In-Vessel

Monitoring System during stop of feedwater supply on the SG-4 transient have been analyzed by using the RELAP5/MOD3.2 and

RELAP5/MOD3.2.2 Beta codes. Kalinin NPP-1 is a Russian designed four loop pressurzed water reactor (WER-1 000, project

V-338) rated at 1000IMWe. RELAP5 code calculation results were compared with plant data. Sensitivity studies were carried out

to Investigate the effects of modeling on major thermal-hydraulic parameters and to examine a new heat transfer model for

horizontal tube bundles.

12. KEY WO-. -- 13O. lit efrwkxshtueewv kbxft• pwp I&. AVALABIUY STATEMENT

RELAPS 

unlimited

Stean Generator It SScUPUrfCLASSFMTIoN

Assessment M* Pam

Kalinin unclassified

unclassified

15. NULNBE OF PAGES

16. PRICE

NRC FORM 5 C24M6
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if

i

IiIL

F r i P red .

Federa Recycling Program

-- ~-

UNITED STATES

NUCLEAR REGULATORY COMMISSION

WASHINGTON, DC 20555-0001

OFFICIAL BUSINESS

PENALTY FOR PRIVATE USE, $300

SPECIAL STANDARD MAIL 

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POSTAGE AND FEES PAID 

-I

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