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BOILER FEED WATER(BFW) & STEAM
SYSTEM
•BFW ini berasal dari demineralized dari Utilitas.
•Energi panas yang dihasilkan di beberapa
penukar panas akan dimamfaatkan untuk
memanaskan BFW yang akan dijadikan steam.
**Alat-2 penukar panas yang menghasikan
steam al:
101-BU,101-CA/CB,102-C,103-C,104-
C,114- C,123-C & BFW Coil (di P-II/III/IV).
101-BU,101-C,103C1/2,123C1/2(di P.IB)
DATA-2 STEAM DI PABRIK
AMONIAK.
• HIGH STEAM (HS): 105 KG/CM2
DENGAN TEMPERATUR
450o
C,510o
C(P.IB)
• STEAM MEDIUM(MS) : 42KG/CM2
DENGAN TEMPERATUR 350-375o
C
• STEAM(S): 7KG/CM2 (DI P.II)
• STEAM LOW(LS):3,5KG/CM2 DENGAN
TEMPERATUR 200o
C
PENGGUNAAN STEAM DI PABRIK
AMONIAK
• Steam HS digunakan untuk penggerak
turbin syngas compressor (103-
JAT),P.IB:penggerak 103-J & 101JT
• Steam MS digunakan untuk penggerak
turbin-2 condensing,turbin-2
extraksi,steam proses,steam sparger &
reboiler glycol.
• Steam LS digunakan untuk: Reboiler,seal
steam, purging,ejektor & stripping.
rev-01
MZH-2-Jan-2001
114-C
1106-C
123-C
BFW
COIL
STEAM
DRUM
101-F
AUXILLIARY
BOILER
SUPERHEATER
COIL(106 K)
(315 o
C)
VE
MS
(40 K)
(350 o
C)
HS (102 K)
460 o
C
PROSES
VE
REBOILER
LS (3.5 K)
IMPORT MS
(0 T/H)
DARI / KE
OFFSITE
REBOILER
CW
VE
SURFACE
CONDENSER
CONDENSATE
POLISHER
DM
MAKE UP
DEAERATOR
1107-C
1155-C
BFW & STEAM SYSTEM
DIAGRAM
OPERASI AMONIAK P-III
(255 o
C)
WHB
101-CA/B
102-C
103-C FUEL GAS
BLOW DOWN
TURBINETURBINE
103-J
TURBINE LPHP
(111 K)
(115 o
C)
(248.5 T/H)
(124 o
C)
(300 o
C)
(298 o
C)
(101.6)
mmHgA
(7.2 K)
(105 o
C)
(105 o
C)
0.7 K
(226 o
C)
253.4 T/H
DSH &
Inst Flush
 
PEDOMAN ANALISA
STEAN SYSTEM
PARAMETER 101-F 101-U 101-JC 102-U DM 123-C
PH 9,5-10,2 8,5-9,2 9-9,5 Non
aktif
6,5-
7,0
8,8-9,2
COND <100 <10 <10 <0,5 <10
PO4 8-12
SiO2 <1,0
N2H4 0,02
BAGAN ALIR PEMBANGKIT STEAM

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Boiler feed water(bfw) & steam system revisi

  • 1. BOILER FEED WATER(BFW) & STEAM SYSTEM •BFW ini berasal dari demineralized dari Utilitas. •Energi panas yang dihasilkan di beberapa penukar panas akan dimamfaatkan untuk memanaskan BFW yang akan dijadikan steam. **Alat-2 penukar panas yang menghasikan steam al: 101-BU,101-CA/CB,102-C,103-C,104- C,114- C,123-C & BFW Coil (di P-II/III/IV). 101-BU,101-C,103C1/2,123C1/2(di P.IB)
  • 2. DATA-2 STEAM DI PABRIK AMONIAK. • HIGH STEAM (HS): 105 KG/CM2 DENGAN TEMPERATUR 450o C,510o C(P.IB) • STEAM MEDIUM(MS) : 42KG/CM2 DENGAN TEMPERATUR 350-375o C • STEAM(S): 7KG/CM2 (DI P.II) • STEAM LOW(LS):3,5KG/CM2 DENGAN TEMPERATUR 200o C
  • 3. PENGGUNAAN STEAM DI PABRIK AMONIAK • Steam HS digunakan untuk penggerak turbin syngas compressor (103- JAT),P.IB:penggerak 103-J & 101JT • Steam MS digunakan untuk penggerak turbin-2 condensing,turbin-2 extraksi,steam proses,steam sparger & reboiler glycol. • Steam LS digunakan untuk: Reboiler,seal steam, purging,ejektor & stripping.
  • 4. rev-01 MZH-2-Jan-2001 114-C 1106-C 123-C BFW COIL STEAM DRUM 101-F AUXILLIARY BOILER SUPERHEATER COIL(106 K) (315 o C) VE MS (40 K) (350 o C) HS (102 K) 460 o C PROSES VE REBOILER LS (3.5 K) IMPORT MS (0 T/H) DARI / KE OFFSITE REBOILER CW VE SURFACE CONDENSER CONDENSATE POLISHER DM MAKE UP DEAERATOR 1107-C 1155-C BFW & STEAM SYSTEM DIAGRAM OPERASI AMONIAK P-III (255 o C) WHB 101-CA/B 102-C 103-C FUEL GAS BLOW DOWN TURBINETURBINE 103-J TURBINE LPHP (111 K) (115 o C) (248.5 T/H) (124 o C) (300 o C) (298 o C) (101.6) mmHgA (7.2 K) (105 o C) (105 o C) 0.7 K (226 o C) 253.4 T/H DSH & Inst Flush  
  • 5.
  • 6. PEDOMAN ANALISA STEAN SYSTEM PARAMETER 101-F 101-U 101-JC 102-U DM 123-C PH 9,5-10,2 8,5-9,2 9-9,5 Non aktif 6,5- 7,0 8,8-9,2 COND <100 <10 <10 <0,5 <10 PO4 8-12 SiO2 <1,0 N2H4 0,02
  • 7.