peta pembangkit pt indonesia power

7/23/2019 Peta Pembangkit PT Indonesia Power

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UP Semarang

PLTGU , PLTG1,469 MW,

UP Perak Grati

PLTU Perak Minyak 100 MW

UP Perak Garti

PLTGU GratiMinyak 462 MW

UP Bali

PLTG dan PLTD335 MW

UP Mrica

PLTA 305 MW

UP SagulingPLTA 797

MW

UP Kamojang

PLTP 360 MW

UP Priok PLTGUMinyak, PLTG danPLTD 1,446 MW

PLTUBatubara

3,400 MW,

Peta PembangkitPT INDONESIA POWER


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SINGLE LINE DIAGRAM SURALAYA

G G G G G GG

CILEGON 1 CILEGON 2

SALIRA 1 SALIRA 2ILEGON 1 CILEGON 2

GANDUL 1 GANDUL 2

SST 3 SST 2 SST 1

TOWN SST 4

IBT 1 IBT 2

7 6 5 4 3 2 1

500 kV

150 kV


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CONSTRUCTION PERIOD & CAPACITY

1.

2.

3.

4.

.

CONSTRUCTION

No.

FIRST FIRING

SYNCHRONIZE

COMMERCIAL OPERATION

I T E M

26-05-84

24-08-84

04-04-85

11-03-85

11-06-85

26-03-86

28-05-88

25-08-88

06-02-89

04-02-89

24-04-89

06-11-89

22-06-96

16-12-96

25-06-97

26-01-97

26-03-97

11-09-97

14-07-97

19-09-97

19-12-97

1980 1984 1994

UNIT 2UNIT 1 UNIT 3 UNIT 4 UNIT 5 UNIT 6 UNIT 7

Constructon period & capacity

7.

9.

.

Gross max cap (at commissioning)

Gross max Cap (After last periodical Manitenance)

400 401.6402.5400 599 604 599

Jan-Feb04SI+

Feb-Mar04 SI+

Apr03

ME

Oct- Nov02 SI

Mei-Jun03ME

Jan-Aug03 SE

Nop-Des03SI

5. INSTALL CAPACITY 400 400400400 600 600 600

6. NET MAX CAPACITY (DMN) 381 381381381 579 579 579

8. 399 397400396 598 600,13 603.55

Last periodical Manitenance


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Coal Tranportation.

Bukit Asam

AdaroKidecoBerau

SURALAYA


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West Java

Sunda StraitSuralaya PP

Jakarta

M. Enim

Prabumulih

B. Raja K. Bumi

Tarahan

Palembang

COAL TRANSPORTATION ROUTE

South Sumatra

Banten

coal Trans. PT BA


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LAYOUT SURALAYA


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Batubara MFO LFO

GWH x1000Ton kliter kliter

1990 10.436 4.367 39.296 16.957

1991 11.287 4.843 40.953 13.987

1992 10.130 4.617 64.346 11.609

1993 9.964 4.275 93.626 10.9091994 10.178 4.319 29.621 8.698

1995 9.893 4.499 29.144 9.529

1996 10.852 5.028 35.645 10.283

1997 13.221 5.803 16.528 14.233

1998 15.979 7.456 55.935 17.659

1999 18.513 8.237 148.406 12.565

2000 21.209 9.589 158.784 18.575

2001 21.063 9.796 22.358 11.339

2002 21.449 9.711 49.215 12.718

2003 23.556 11.008 3.914 9.615

Tahun

Produksi

Bruto

Pemakaian Bahan Bakar

DATA PRODUKSI , BAHANBAKAR 1990-2003


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1.000

10.000

100.000

1.000.000

B.Bara (Jt.Ton) 7.280 8.212 9.590 9.795 9.712 11.009

HSD (k,liter) 17.850 16.613 18.674 11.338 12.718 9.615

MFO (k.liter) 55.935 145.302 157.133 22.357 49.215 3.914

th 1998 th 1999 th 2000 th 2001 th 2002 th 2003

Grafik pemakaian Bahan Bakar 1998-2003


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Hopper K & BF.20/21,

BF 26/27,MS.13/14Hopper L Hopper M

RH. D&

BF.09/10

Plant Distribute Hopper &

BF 501A/B, BF 601A/B, BF 701A/B

COAL BUNKER COAL BUNKER

Unit 7 Unit 5Unit 6 Unit 4 Unit 2Unit 3 Unit 1

Coal stock area

SC. 22

SC. 25

SC. 24

SC. 23

BC. 26

BC. 27 BC. 21

BC. 20

SC.30

SC. 31 SC. 29

SC. 28

ST / RE 2

TelescopicChute

BeltWeigher

BC. 502B

BC. 502A

BC. 702B

BC. 702A

BC. 602B

BC. 602A

BC. 02

BC. 17

BC. 16

BC. 15 BC. 11

BC. 12

B C

. 1 4

B C

. 1 3

BC. 703A

BC. 703B

Coal Ship

Coal Ship

COAL HANDLING SYSTEMSURALAYA POWER PLANT

UNITS 1 ~ 7JH. H

JH. G&

HG36/37,HG40/02

JH.B&

C S. &MS.03/04

JH. J&

HG. A/B

JH.F

JH. C&

MCC,BF.11/12,MS.09/10

JH. E&

CoalSampling

CHCR

TelescopicChute

M/H. &BF.32/33

RH.A & BF.03/04

BS.34/35

BS.02

BS.36/37

COAL HANDLING SYSTEM


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169 k, 538 C

40 k, 336 C

39 k, 538 C

10 k, 330 C

174 k 251 C

180 k, 142 C

28 k. 40 C

12 k, 109 C

G

SUBFP

DEAERATOR

LP HEATER

LP HEATER

LP HEATER 4

LP HEATER 3

LP HEATER 2

HP HEATER 6

HP HEATER 8

HP HEATER 7

BFP

HP IP

LP 1 LP 2

HP BY PASS

LP BY PASS

MAIN DRUM

BOILER

SUPERHEATERREHEATER

ECONOMIZER

DESAL PLANT

FWT

DEMINPLANT

COND.

PUMP

CONDPOLISH

T U R B I N E S

SEA

GLAND STCOND

FUEL

ASH

condenser

BOILER CYCLE


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STACK ELECTROSTATICPRECIPITATOR

80 %

BOILER

170.000 Kg/Hr6 % Ash

Coal

MFOOIL

HSD

BOTTOM ASH 20%2.040 Kg/ Hr.

EP EFFICIENCY = 99,50 %FLY ASH = 8.119,2 Kg/ Hr.

FLAY ASH 40,8 KG/HR

ASH CYCLE


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Coal Flow diagram

Mill

STOCK AREA

Coal bunker

Hp. DST/RE

Coal Feeder

PAF

Boiler

Pyrite

PAH


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C. CHEMICAL ANALYSIS OF ASH

( % by w t. ) AVG. COAL WORST COAL

1. Silica ( SiO 2 ) 59.4 42.4 - 83.52. Iron (Fe 2O 3) 4.6 0.8 - 12.93. Aluminium Oxcide 24.7 3.5 - 37.04. Calcium Oxcide (CaO ) 3.1 0.7 - 11.55. Magnesium Oxcide (MgO) 1.7 0.3 - 8.36. Sodium Oxcide ( Na 2O) 2.5 0.6 - 6.87. Pottassium Oxcide (K 2O) 0.5 0.1 - 0.88. Shulpur Oxcide ( SiO 3 ) 2.3 0.1 - 6.69. Titanium Dioxcide ( Tio 2 ) 0.8 0.3 - 1.4

10. Phospathe Pentoxide (P 2O 5) 0.4 0.04 - 1.3

D. FUSION POINT OF ASH ( C )

1. Initial 1279 1010 - 15002. Softning 1395 1190 - 15103. Fluid 1443 1350 - 1620

COAL SPECIFICATION (Ash Analisys)( Design)


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C. ASH ANALYSIS

( % by wt ) BUKIT ASAM ADARO BERAU

1. Silica ( SiO 2 ) 75 38.73 30.872. Iron (Fe 2O 3) 7 15.55 11.673. Aluminium Oxide ( Al 2O 3 ) 33 24.66 10.324. Calcium Oxide (CaO ) 3 8.99 16.76

5. Magnesium Oxide (MgO) 1.5 2.28 6.566. Sodium Oxide ( Na 2O) 3.5 1.12 3.157. Pottassium Oxide (K 2O) 0.7 0.97 1.098. Titanium Dioxcide ( Tio 2 ) - 1.06 0.569. Phospathe Pentoxide (P 2O 5) - 0.12 0.18

D. FUSION POINT OF ASH ( C )

1. Initial 1279 1150 11102. Softning 1395 1180 11303. Fluid 1443 1250 1140

COAL SPECIFICATION (Ash Analisys)As Received)


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A. COAL PROXIMATE ANALYSIS(% by wt. )

AVG. RANGE WORST1. Total Moisture 23.6 - 28.32. Ash Content 7.8 - 12.83. Volatile Matter 30.3 - 15.14. Total Sulphur - - -5. Fixed Carbon 38.3 32.9 - 59.3 43.86. Heating Value (kcal/kg) 5242 - 4225

7. Air Dried Moisture ( Basis) - - -8. HGI ( Grind ability ) 61.8 55 - 65 55

B. COAL ULTIMATE ANALYSIS( % by wt. )

1. Total Moisture 23.6 - 28.32. Ash Content 7.8 - 12.83. Hydrogen 3.9 2.6 - 4.1 2.64. Carbon 54.2 45.3 - 64.1 45.35. Sulphur 0.4 - 0.96. Nitrogen 0.9 0.7 - 1.1 1.17. Oxygen 9.2 3.0 13.6

COAL SPECIFICATION


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A . PROXIMATE ANALYSIS(% by wt ) BUKIT ASAM ADARO BERAU

1. Volatile Matter 32.06 36.8 36.42. Fixed Carbon 34.91 36.6 36.43. Moisture Content 27.65 24.2 -4. Inherent Moisture 1 2.88 16,6 16.35. Ash Content 5.48 0.9 3.06. Sulphur Content 0.26 0.09 0.727. HGI 57 45 498. Relative Density 1.36 1.31 -9. Heating Value ( kcal/kg ) 5,025 5,220 5,237

B. ULTIMATE ANALYSIS( % by wt )

1. Carbon - 53.57 53.62. Hydrogen - 6.57 3.273. Nitrogen - 0.85 0.884. Oxygen - 12.32 14.35. Sulphur - 0.09 0.726. Total Moisture - 25.7 24.2

COAL SAMPLING AND ANALYSIS( As Received )


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COAL FEEDER

COAL INLET

TO PULVERIZERS


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PULVERIZER

ASH HANDLING SYSTEM


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CHUTE# 3/ 4

RMVLDDCC

SDCC

MARINETOWER

# 3/ 4

RMVLDDCC

RMVLDDCC

Mill Reject

SDCCSDCC

SILO ATRANS. BIN TRANS. BIN TRANS. BIN

TRANSPORTERSTRANSPORTERS TRANSPORTERS JUMBO

TRANPORTERS JUMBO

TRANPORTERS

CONV. 12

CONV. 11

C O N V

. 1 4

C O N V

. 1 3

C O N V

. 9 A

VIB.GRID &ASH CRUSHER




C O N V

. 4

C O N V

. 3

C O N V

. 2 A

C O N V

. 1 A

CONV. 6

CONV. 5

C O N V

. 1 0 B

C O N V

. 9 B

CONV. 8A

CONV. 7A

SILO B

DISTRIBUTION BOX

CHUTECONV.

DISTRIBUTION BOX

MARINETOWER

# 1/ 2

CHUTE# 1/ 2

CONV. 8B

CONV. 7B

CONV. 20CONV. 19 CONV. 17

CONV. 18CONV. 15CONV. 16

SSCSSCSSCSSC

VIB.SCN &CRUSHER

VIB.SCN &CRUSHER

VIB.SCN &CRUSHER

Collect.DDCC

Collect.DDCC

Collect.DDCC

1ST & 2NDTRANSF DDCC

1ST & 2NDTR. DDCC

1ST & 2NDTR. DDCC

CHAINCONV. A

CHAINCONV. B

COND.U/L 1A

CONVU/L. 2A

CONVU/L. 1B

COND.U/L. 2B

FLY ASH CONV. A

FLY ASH CONV. B

Dust HopperDust Hopper

C O N V

. 2 B

C O N V

. 1 B

C O N V

. 8

Mill RejectMill Reject Mill Reject

Mill Reject

Mill Reject

Mill Reject Mill Reject Mill Reject

Dust HopperDust Hopper

C O N V

. 1 0 A

Dust Collector Dust Collector Dust Collector Dust Collector

ELECTROSTATICPRECIPITATOR #4




JUMBOTRANPORTERS

ASH VALLEY

CONCRETESILO

BACK

ASH HANDLING SYSTEM


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S I S T E M P E M B U A N G A N A B U


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ELECTROSTATIC PRECIPITATOR

GAS

FLOW

CLEAN

GASEXIT

DISCHARGEELECTRODE

COLLECTINGPLATE

+ +

+ +

- - - - -


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ASH VALLEY At a Glance


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ASH VALLEY


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Tophografi suralaya

Radiant Boiler


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Radiant Boiler


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CAROLINA TYPE, RADIANT BOILER

FROM HTX 8

FROM HP TURBINE

TO HP TURBINE

TO LP TURBINE

SDCC

DDCC

4 BUAH COLLECTINGDDCC

Steam coil air

preheater

Primary Air heater

Economizer & Primary

Superheater

Reheater

Tumpukanabu

EP

Serpihan elemenPAH ditemukan diunit 5 tgl 09 Jan03

stack


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Fouling Pada Boiler Unit 5


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30.0

31.0

32.0

33.0

34.0

35.0

36.0

37.0

38.0

1998 1999 2000 2001 2002 2003

Tahun

( % )

EFISIENSI THERMAL NETTO (%) 1997 ~ 2003


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Equivalent Force Outage Rate (EFOR) 1997 ~ 2003

01

2345

67

1998 1999 2000 2001 2002 2003

Tahun

( %


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Equivalent Availability Factor (EAF) 1997 ~ 2003

70

75

80

85

90

95

100

1998 1999 2000 2001 2002 2003

Tahun

( %

peta pembangkit pt indonesia power

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