3 System Process Outline_SLP R2

8/3/2019 3 System Process Outline_SLP R2

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Classroom Lecture for SLP 60MW CCGT Power Plant Expansion Project

Plant Overview

1

3. System/Process Outline

1st : July 08 & 09, 20082nd : July 12 & 13, 2008

TOSHIBA PLANT SYSTEMS & SERVICES CORPORATION


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Plant Overview

2

3. System/Process Outline

1. Condensate System

2. HRSG HP and LP System

3. Feedwater System

4. Main and Auxiliary Steam System

5. Extraction Steam System

6. Turbine Bypass System

7. CW & ACW System8. CCCW System

9. Condensate Drain System


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Plant Overview

3

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )

Steam TurbineGen

Gen GT Comp.

ST GS System

Stack

BD Tank(Continuous)

BD Tank(Intermittent)


M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )

Steam TurbineGen

Gen GT Comp.

GT Comp.

ST GS System

Stack

BD Tank(Continuous)



M

M

M

M

M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

Condensate System (1)

The purpose of Condensate System is mainly to

Condense the ST exhaust steam or dumpedsteam by the Turbine Bypass System

Feed the condensed water to the HRSG

1. Function of System

2. Outline of System

This system is comprised of the following lines ;

Mainstream Recirculation Line Spray Line Seal Water line


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Plant Overview

4

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )

Steam TurbineGen

Gen GT Comp.

ST GS System

Stack

BD Tank(Continuous)



M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )

Steam TurbineGen

Gen GT Comp.

GT Comp.

ST GS System

Stack

BD Tank(Continuous)



M

M

M

M

M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent


The purpose of Condensate System is to ;

Condense the ST exhaust steam

Condense dumped steam by the Turbine

Bypass System Feed the condensate water to the Deaerator

2.1. Condensate System Mainstream

(1) Function of the line

This system contains the following major equipment ;

Main Condenser

Vacuum Pumps

Condensate Pumps (CPs)

ST Gland Steam Condenser (GSC)


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Plant Overview

5


(2) Major Equipment Information

Equipment Type Capacity, Design Manufacturer

Main Condenser Circular/Axially Mounted/

Two Pass/Divided

HeatLoad:37415kJ/s,

Tube Material:SA249 TP316L

Larsen & Toubro(India)

Vacuum Pumps Liquid Ring 2x100% Tsurumi (Japan)

CondensateExtraction

Pumps

Vertical 2x100%,Flow:107m3/h,

Total Head:193m@990kg/m3

Torishima (Japan)

ST Gland SteamCondenser

Shell & Tube 1x100% Siemens (Czech)This is a part ofST System



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Plant Overview

6

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )

Steam TurbineGenGen GT Comp.

ST GS System

Stack

BD Tank(Continuous)



M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


GT Comp.

ST GS System

Stack

BD Tank(Continuous)



M

M

M

M

M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent



(3) Hotwell Level Control

Condenser Hotwell is controlled by theCV at the Deaerator Inlet.

NoteThe Makeup-water CV at Deaerator inletis used for the level control of the LPDrum.


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Plant Overview

7

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )

Steam TurbineGenGen GT Comp.GT Comp.

ST GS System

Stack

BD Tank(Continuous)



M

M

MM

MM

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

2.2. Condensate Recirculation Line


In general, this system is provided tosecure minimum required water flow foreither condensate pump or GSC (glandsteam condenser).

Line is tapped from GSC outlet In SLP case minimum requirement

comes from GSC (Min. RequiredFlow : 25 t/h)

Recalculation flow goes back to theCondenser Hotwell

Pneumatic actuated FCV and FT areprovided for this purpose


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Plant Overview

8

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

MM

MM

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent


2.3. Condensate Spray Line

This line feeds spray water to the following system/equipment ;

LP Extraction Steam DSH

ST LP Casing Spray

ST Gland Steam System Spray

HP and LP Turbine Bypass DSH

After the tapping point, Y-strainer is installed.

Differential pressure is monitoredby DCS.


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Plant Overview

9

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

MM

MM

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent


2.4. Condensate Seal Water Line

This line feed seal water to the followingequipment/system ;

Vacuum Pump Seal Line

The valves which downstream or

upstream is connected to vacuum lines.

The following need seal water to avoid airentering inside the devices;

Condenser Drain Valve

Condensate Pump Inlet Isolation Valves Minimum Flow Control Valve Outlet

Isolation

Vacuum Breaker Outlet Pipe

P&ID LINK
http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/


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Plant Overview

10

2. HRSG HP and LP System
http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/


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Plant Overview

11

HRSG (1)

One (1) - natural circulation, horizontal gas flow, dualpressure heat recovery steam generator (HRSG) isprovided to produce superheated steam by exchangingthe heat from the GT exhaust gas.

1. General

All the devices/equipment of the HRSG (both HP andLP) are controlled by plant DCS.
http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/


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Plant Overview

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HRSG (2)2. LP System

Heat Exchanger Associated System/Equipment

Preheater - Preheater Recirculation Line*- Preheater Bypass Line*

LP Drum withDeaerator

- Makeup Water Line to Deaerator*

- Pegging Steam Line*

- Chemical Injection Line

- Intermittent Blowdown Line

LP Evaporator -

LP Superheater LP Startup Vent (on outlet piping)

HRSG LP System mainly consists of ;2.1. LP System Main Equipments/Lines
http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/


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Plant Overview

13

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

BFP

Makeup Water


Stack

BD Tank(Continuous)



M

M

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

BFP

Makeup Water


Stack

BD Tank(Continuous)



M

M

MM

MM

StartupVent

StartupVent

HRSG (3)

2.2. Preheater and Associated System

(1) Preheater Recirculation Line

This system is provided for thepurpose of maintaining the tubeouter surface temperature of the

Preheater above dew point ofexhaust gas.

Inlet Water Temp < 50 C

The system will be online. Inlet Water Temp 50C

Preheater outlet water is returned to the inlet

Inlet Temp 50C

2x100% Recirculation Pumps are provided.

ARC Valve is provided for the control of minimum required flow.
http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20system%28fc%29.pdf/http://slp-m-t-pd-0007r7%20condensate%20syst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14/56


Plant Overview

14

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

BFP

Makeup Water


Stack

BD Tank(Continuous)



M

M

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

BFP

Makeup Water


Stack

BD Tank(Continuous)



M

M

MM

MM

StartupVent

StartupVent

HRSG (4)

2.2. Preheater and Associated System

(2) Preheater Bypass Line

This system is provided for thepurpose of avoiding steaming atdownstream of the Hotwell Level CV

Valve before Deaerator.

Preheater Outlet Temp LP Drum Temp

The system will be online.

Water temp after the confluence is controlled by the bypass flow.

Water temp before the CV is controlled at ;

LP Drum Temp - 1 C

Drum Temp - 1C
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Plant Overview

15

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

MM

MM

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

HRSG (5)

To handle large amount ofmakeup water that needdeaeration, the Make-up WaterLine is connected to theDeaerator.

2.3. LP Drum with Deaerator and Associated System

(1) Make-up Water Line to Deaerator

Deaerator is installed on the LP Drum

Deaerator is designed to reduce DO(Dissolved Oxygen) content down to a

maximum of 7 ppb.
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Plant Overview

16

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

MM

MM

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

LP Drum water level iscontrolled by the make-upwater flow CV.

HRSG (6)


(1) Make-up Water Line to Deaerator (Continue)

NoteThe CV at Deaerator inlet is usedfor the level control of theCondenser Hotwell.
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Plant Overview

17

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

STLPCasingSpray

STGSSystemS

pray

LPHP

HPSH#2

HPSH#1

HPEVA

HPECO

LPSH

LP

EVA

PREHTR

Dea

Recirc. Pump

CP GSC

BFP

Makeup Water

MP Line

( SLP )

LP Line ( LCP )


ST GS System

Stack

BD Tank(Continuous)



M

M

MM

MM

LP Line

( SLP )

MP Line ( LCP )

StartupVent

StartupVent

HRSG (7)

Pegging Steam Line isprovided to utilize auxiliarysteam for water heating anddeaerating the LP drum waterprior to and during unit start.


(2) Pegging Steam Line
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18/56


Plant Overview

18

HRSG (8)

Heat Exchanger Associated System/Equipment

HP Economizer -

HP Drum -

HP Evaporator - Continuous Blowdown Line

- Intermittent Blowdown Line

HP Superheater#1HP Superheater#2

- Desuperheator (between #1 and #2)- HP Startup Vent (on outlet piping

Date post:	06-Apr-2018
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3 System Process Outline_SLP R2

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