FULL BENZOLE SYSTEM
Level Control
3.OIL TO VAPOURS
2E401/2.
4.OIL TO OILS
1/2E414.
5.FINAL HEATERS
2E403/4.
6.VAPOUR
BOX.2G402
7.BZ STILL120°c
90°c
11. Lean oil
in.(27°c).
1/2P406
1/2P405
1/2P404
1/2P401
1/2P401
1/2P402
1/2P407 1/2P408
1/2P409
10.Circulation Tank
9.CREOSOTE
COOLERS.
1/2E405/6/7/8
0P409/10
.
2P410
Cooling
Water in
Cooling
water out
2P412
20°c 82°c
18.CONDENSER 17.DEPHLEGMATOR
19.TALLBOY20.BZ
SEPERATOR
22.BENZOLE
RECIEVER
21.PHLEGM OIL
1P414
OP415/6
1/2T410
23.BENZOLE
STORAGE
24.TO OUTLOADING
CONDENSATE TO
0T415 TANK
MP STEAM 10.5 Bar
HEATING COIL
2P424
TO 0T412
SLUDGE TANK
2P414
30°c
12.PURIFIER
LP STEAM
1.1Bar
13.Xmas tree
1/2c401
1. BZ WASHER
.STRIPPEDOIL
14.PHLEGM OIL
FOW
15.OIL BLEED
FROM STILL
16.REFLUXED
LIGHT ENDS
1T404
2T404
170°c.
108°c
8.WEIR
WEIR
2C404
2G401
0G403
2E412/1E4112E411/1E412
2LIC-407
LEVEL CONTROL
0P435
1/2C402
2. BZ WASHER
1/2405
2C403
BENZOLE STILL
HAS 14 BUBBLE
TRAYS
1/2LIC-404
LEVEL CONTROL
RICH OIL TEMP
IN 28°c
RICH OIL TEMP
OUT FROM
1/2c401.( 29°c).
LEVEL CONTROL
1/2LIC-406
FLOW CONTROL
1/2FIC-404
2LIC-409
FLOW CONTROL
2FI-405
1/2P407
Transfer
1/2P408
Transfer
1/2P406
Re-circulation
Pump
1/2P405
Re-circulation
Pump
1/2P404
Re-circulation
Pump
1/2P401
Re-circulation
Pump
1/2P402
Re-circulation
Pump
1/2P403
Re-circulation
Pump
Level
Control
Level
Control
Gas from
Ammonia
Washers 27°c
BENZOLE SCRUBBERS OIL AND GAS FLOWS
COKE OVEN GASS TO THE
BOOSTERS 29°c
2 5
31/2C402 1/2C401
Lean oil flow control
Transfer
1/2P409
CAN OPERATE FOR
EITHER 1/2P407/8
1.
2.
1. 1C402 SCRUBBER
2. 1C401 SCRUBBER
3. LEAN OIL FLOW
4. RICH OIL FLOW
RICH OIL
TO STILL
Gas from
1c401. 28°c
1C402 1C401
28°c
GAS OUT
BENZOLE RICH OIL FLOW
1/2P401
1/2P402
1/2P403
1/2P408
Level
Control
LEAN OIL IN
29°c
1C401 SCRUBBER.
2P410
Level
Control
1.
2.
3.
4.
5.
6.
1. 1C401 SCRUBBER.
2. OIL TO VAPOURS.
3. OIL TO OILS.
4. FINAL HEATERS.
5. VAPOUR BOX.
6. 2C403 BZ STILL.
7. RICH OIL FLOW.
8. LEAN OIL FLOW.
BENZOLE STILL
HAS 14
BUBBLE TRAYS
OIL TO VAPOURS.
OIL TO OILS.
FINAL HEATERS.
VAPOUR BOX.
2C403
BZ STILL
Re-circulation Pump
Re-circulation Pump
Re-circulation Pump
VAPOUR EXITS AT
APPROX 108°c.
120°c
To
oil to oils
90°c
110°c
28°c
BENZOLE VAPOUR RECOVERY
1.
2
3. 4.
5.6.
7.8.
9.
2P414
1P414OP415/6
TO OUTLOADING
1. BENZOLE STILL 2C403.
2. OIL TO VAPOURS.
3. CONDENSOR.
4. DEPHLEGMATOR.
5. TALL BOY.
6. BENZOLE SEPERATOR.
7. PHLEGM OIL TANK.
8. BENZOLE RECIEVER.
9. BENZOLE STORAGE TANK
1/2T405.
10. VAPOUR FLOW.
11. PHLEGM OIL/CONDY.
12. PHLEGM OIL.
13. BENZOLE/CONDY.
14. BENZOLE.
15. COOLING WATER.
16. CONDENSATE.
20°c 82°c
COOLING WATER IN
COOLING WATER OUT
COOLING WATER IN
COOLING
WATER OUT
1/2T410
VAPOUR EXITS AT
APPROX 107/8°c.
BENZOLE STILL
HAS 14
BUBBLE TRAYS
BENZOLE STILL
OIL TO
VAPOURS
OIL TO
VAPOURS
CONDENSER DEPHLEGMATOR
BZ
SEPERATOR
TALLBOY
BENZOLE
RECIEVER
PHLEGM OIL
BENZOLE
STORAGE 2C403
Condensate to
0T415
90°c
Cooling Water in
Cooling water out
Creosote coolers
Circulation Tank
2P412
Flow
controller
1/2C402
scrubber
Oil to oil heat
exchangers
Level
control
2P410
2.
3.
4.
5.
BENZOLE LEAN OIL FLOW
1.
1. 2C403 BZ STILL.
2. OIL TO OILS.
3. CREOSOTE COOLERS.
4. 1/2T405.
5. 1/2C402 SCRUBBER.
6. LEAN OIL FLOW.
1/2T405.
2C403 BZ STILL.
BENZOLE STILL
HAS 14
BUBBLE TRAYS
2P411
CAN OPERATE FOR EITHER 2P410/12
30°c
PURIFIER AND STILL SET UP
2C403 BZ STILL.
PURIFIER
4. LP STEAM
1.1 Bar
6. RICH OIL IN
VAPOUR OUT
5. MP STEAM 10.5 Bar
HEATING COIL
2P424
8. TO 0T412
SLUDGE TANK
1.
2.
3.
1. VAPOUR BOX.
2. 2C403 BZ STILL.
3. 2C404 PURIFIER.
4. LP STEAM. 1.1 Bar
5. MP STEAM.
6. RICH OIL.
7. XMAS TREE.
8. HEAVY ENDS.
7. XMAS TREE
Level
Control
BENZOLE STILL
HAS 14
BUBBLE TRAYS
2C404
VAPOUR BOX
120°c
170°c
108°c
3. ODT
2.Seal pot
Main
Naphthalene
Washer
1
Demister pad
17.Heating coil
LP 1.1Bar
1/2p202
1/2p201
1/2P215
COMMON
PUMP
000000
8
8
6
6
SEPERATOR
0G202
NAPTHALENE
STORAGE TANK
0T204 40°c
18.Heating coil
LP 1.1Bar.
Oc202
NAPHTHALENE
STILL
CONDENSOR.40°c
0E202
120°c
TO BENZOLE
PRODUCT TANK
CONDENSATE
TO 0T415.7 BUBBLE
TRAYS
7 BUBBLE
TRAYS
14.TO 0T412 SLUDGE TANK
115°c
1/2P211,
0P212 8.LEAN OIL TO MAIN
NAPHTHALENE WASHER
19.Cooling water
coil
Divide tank
0T203
FULL NAPHTHALENE SYSTEM
5.
6.
12.
10
7.
9.
11
13
15.
16.
MAIN HEATER.
MP STEAM 140°c
0E201
4. RICH OIL FROM
MAIN NAPHTHALENE
WASHERS. 42°c
22.
21. GAS TO
AMMONIA
WASHERS 43°c
23.LP STEAM
1.1Bar
120oc
45oc
COOLING
WATER IN.
COOLING
WATER OUT.
2P424
GAS IN FROM
DETARRERS
38-40°c
LEVEL CONTROL
MP STEAM 10.5 Bar
CONTROL VALVE
FLOW CONTROL
FLOW CONTROL
0P218
0C202
1/2T201
LEVEL
CONTROL
1. 1/2C201 NAPHTHALENE WASHER.
2. SEAL POT.
3. OIL DECANTER TANK.
4. DEWATERING POINT.
GAS FLOW.
OIL FLOW.
LEAN OIL.
RICH OIL.
Seal pot
Main
Naphthalene
Washer
1/2P202
6. Petroleum oil
circulation
1/2P201
petroleum oil
circulation
5. Gas in from
detarrer,s
10.Gas to ammonia
washers
1
24
Demister pad
9. Heating coil
LP 1.1Bar
MAIN NAPHTHALENE WASHER FLOWS
7. LEAN OIL FROM
DIVIDE TANK
8. RICH OIL TO STILL
Aim is 1-2°c higher than
entry temperature
OIL DECANTER TANK
1/2T201
3
.
Dewatering point
1/2p215
Operates for either
1/2p201/2
4
1/2P211,
0P212
Divide tank
MP steam 10.5 BAR
Temperature
control Valve
140 ° C
1.
2.
3.
Naphthalene vapour
Condensate to
fire fighting
pump house heating
Cooling water
coil
5. LEAN OIL TO MAIN
NAPHTHALENE WASHER
4. RICH OIL FROM
MAIN NAPHTHALENE
WASHERS. 42°c
NAPHTHALENE STILL 0C202 OIL FLOWS
1. 0C202 NAPHTHALENE STILL
2. DIVIDE TANK.
3. MAIN HEATER. 140°c
4. RICH OIL FLOW
5. LEAN OIL FLOW
0C202
NAPHTHALENE
STILL
MAIN HEATER.
140°c
120°c
115°c
120°c
7 BUBBLE
TRAYS
7 BUBBLE
TRAYS
NAPHTHALENE VAPOUR FLOW
column
1.
NAPHTHALENE
STILL
7. Naphthalene vapour
000000
8
8
6
6
CONDENSOR . 40°c
5.
2.
3.
6.
1. 0C202 NAPHTHALENE STILL
2. KNOCKOUT POT.
3. CONDENSOR.
4. ADJUSTABLE WEIR.
5. SEPERATOR.
6. NAPTHALENE STORAGE TANK.
7. VAPOUR FLOW.
8. REFLUX LINE.
9. LOW PRESSURE STEAM.1.1bar.
10. HEATING COIL.
11. CONDENSATE/NAP OIL.
12. NAPHTHALENE OIL.
13. CONDENSATE.
4
8.
9. LP STEAM
1.1 Bar
10.Heating coil.
11.
TO 0T412 SLUDGE TANK
TO BENZOLE PRODUCT TANK
13. CONDENSATE TO 0T415.
NAPTHALENE
STORAGE TANK
0T204
SEPERATOR
0G202
0C202
40°c
7 BUBBLE
TRAYS
7 BUBBLE
TRAYS
120°c
LIQUID REFLUXED
BACK INTO THE STILL
0P205/6
1/2p311/2
1/2p314/5
To lime
sump
GAS TO BENZOLE
WASHERS 27°c
COOLING
WATER IN
COOLING
WATER OUT
VAPOUR OUT
DEPHLEGMATOR
1/2E304
85°c
Heat exchangers
1/2e306
PLATE COOLER
1/2E308
TO INCINERATOR
1/2F301
1/2T301
1/2C302 1/2C301
GAS FROM NAPHTHALENE
WASHERS 40°c
1/2337
1/2P303
1/2P302
1/2P301/7
1/2P308
1/2P309
1/2P310
COMMON PUMP
1/2P319
GAS OUT 28°C
COOLING
WATER IN
SECONDARY
COOLERS
KNOCKOUT POT
AMMONIA STRONG LIQUOR FLOW
1/2p306
1/2p304
1/2p305
LEVEL
CONTROL
STRONG LIQUOR
STORAGE
AMMONIA
STILL
1/2C303
LEVEL
CONTROL
18m³/HR.
1c302
18m³/HR.
2c302
INTO SUCTION
OF 1/2P306
LEVEL
CONTROL
FLOW CONTROL
40m³/HR.
1/2T305
STRONG LIQUOR TANKS
1/2t301
1.
2.
1.
3.
1.
6.
5.
4.
10.
8.
7.
9.
11.
12.
13.
14.
15 VALVE
TRAYS
15.
1/2p306
1/2p305
1/2p304
1/2p337
1/2p307
1/2p302
1/2p303
AMMONIA SCRUBBERS
1/2P308
1/2P310
1/2P309
TO 1/2T301
GAS FROM MAIN
NAP WASHERS
40°
GAS TO
BENZOLE SCRUBBERS
27°c
1/2c302
1/2c301
FROM 1/2C303
28°c
SECONDARY
COOLERS
LEVEL
CONTROL
LEVEL
CONTROL
FLOW
CONTROL
1/2C303 FREE STILL STRONG LIQUOR FLOW
DEPLEGMATOR 85°c
K/O POT
1/2C303
15 VALVE
TRAYS
HEAT EXCHANGERS
1/2E306
COOLING WATER IN
PLATE COOLERS
1/2E308
COOLING WATER OUT COOLING WATER IN
COOLING WATER OUT
18m³/HR STRIPPED LIQUOR
TO 1C302
18m³/HR STRIPPED LIQUOR
TO 2C302
1/2T301 STRONG
LIQUOR STORAGE
40m³/HR STRONG
LIQUOR
TO 1/2C303
40m³/HR STRONG
LIQUOR
36m³/HR STRIPPED
LIQUOR OUT
VAPOUR TO 1/2F301
INCINERATOR
REFLUX LINE
LP STEAM IN.
1.1Bar
APPROX 4m³/HR STRIPPED
LIQUOR TO LIME SUMP
1/2P319
1/2p314/5
1/2p311/2
1/2C304 AND 0C305 FIXED AND FREE STILLS
LP STEAM
1.1 Bar
FIXED SECTION
FREE SECTION
CAUSTIC IN
FIXED AMMONIA
VIRGIN LIQUOR INVIRGIN LIQUOR INCAUSTIC IN
VAPOUR OUT
TO 1/2F301
INCINERATOR
VAPOUR OUT
TO 1/2F301
INCINERATOR
STRIPPED LIQUOR
TO LIME SUMP
STRIPPED LIQUOR
TO LIME SUMP
8 BUBBLE TRAYS
9 BUBBLE TRAYS
0C305 1/2C304
LP STEAM
1.1 Bar
19 VALVE TRAYS
BLEED TO ANALYSERS
0C305 FIXED AND FREE STILL FLOWS
COOLING WATER IN
COOLING WATER OUT
VAPOUR TO 1/2F301
INCINERATOR
K/O POT
REFLUX LINE
LP STEAM
1.1 Bar
LEVEL
CONTROL STRIPPED LIQUOR
TO LIME SUMP
BLEED TO ANALYSERS
DEPLEGMATOR 85°c
0C305
0/1/2T105, 0T112
VIRGIN LIQUOR STORAGE
TRANSFER PUMPS
0P126,1/2P117,1/2P312
CAUSTIC PUMP
CAUSTIC TANK
0T312/3
+30°c
HEATING COIL
LP 1.1Bar
CAUSTIC FROM
TANKER OFFLOADING
POINT
TAR AND LIQUOR FLOWS
0T112
VIRGIN LIQUOR
DOWNCOMER
SPIRAL COOLER LIQUOR FLOW
BIOLOGICAL EFFLUENT PLANT
SLUDGE
TO
RECYCLE
SLUDGE
TO
RECYCLE
INSTRUMENTS ON PLANT
INSTRUMENT AIR
BY-PRODUCTS PLANT EQUIPMENT
PLATE COOLER 1E308
Hot
liquor in
Cooled
liquor out
Cold water
In from cooling
tower
Hot water
out to cooling
tower
SPIRAL SECONDARY COOLER
HOT IN FROM
1/2P301/7
COLD IN FROM
COOLING TOWER
TO 1/2C302
COOLED LIQUOR OUT
HEATED WATER
OUT TO COOLING
TOWER
SHELL AND TUBE HEAT EXCHANGER
Vapour In
Vapour
Out
COOLING
Water Out
Product
Out
COOLING
Water In
End Views 4 Pass Tube and Shell
1.
4.
2.
Flange Flange
Dividers
Dividers
3.
Tubes
chandelier
Insulator
Turrets (3 of)
Vent
Gas seal pot
To 0A102
low level sump
1
6
TOP FLUSH
BOTTOM FLUSH
Gas In From
Exhauster 30°c
Gas out to main
Naphthalene washer
40°c
Flow Control Valve
Flow Control Valve
Tar Loaded
Coke Oven Gas
Nitrogen In
HV Rectifier
Power In
Flushing Liquor
Turret temperature
maintained between
30°c and 70°c
1V101 AND 2V102 DETARRERS
Electrode wires
Tension Weights
DETARRED INTERNAL VIEW OF CHANDELIER
DETARRER CASING
CHANDELIER WIRES
TENSION WEIGHTS
139 HEXAGONAL TUBES
ENCORPORATING ELECTRODE WIRE
ELECTRODE WIRE
FROM CHANDELIER
PRIMARY COOLERS 1/2C101/2
8 No tar sprays
Only 4 in service
At any time
9 No Liquor Sprays
9 No Liquor Sprays
Liquor In
Liquor In
Liquor Out
Liquor Out
1p103/2p101
Spiral Coolers
1/2p102
1/2p112
Gas In
Tar In 5m³/hr.
Gas Out
Common
Standby
1p101/2p119
Low Level
Sump
Tar & Liquor
Decanters
Desludging Point
Rodding
Point
Syphon Breaker
Overflow
Gas In
726m³/HR.
28oC
From
downcomer
(all units)
From primary
coolers
(all units)
From low level
sump 0A102
Spiral coolers hot flush
discharge line
(1 & 3 only
Sludge scraper
Tar weir
Liquor
overflow
Sludge skip
Chute
Baffles
To 1/2T102
pump tank
To 0T104/111
Liquor receiving
tank
TAR & LIQUOR DECANTERS
Xmas
tree
Desired tar level
SLUDGE SKIP EMPTIED
INTO TAR POND ROT
To Tar Storage
Excess Liquor
to 0,1,2T105/
0T112 Virgin Tanks
1/2p121/2
Gas Booster 1/2B501/0B502
Electric Motor
Fluid Coupling Oil Filter
Aux. Lube
Pump/Motor
Lube Oil
Cooler
Gas
Inlet
Outlet
Booster
Gear
Box
Fluid
Coupling
Motor
Speed Control Unit
FLUID DRIVE
Heaters &
Thermostats
Water
Oil Filters
Instrument
Panel
Auxiliary oil pump pressure 2.2 barg
Auxiliary oil pump stops & main pump takes over at 2.75 barg
Auxiliary oil pump restarts at 2.15 barg
Oil temperature trip set at 10 DegC
AUTO / MANUAL
HP STEAM TURBINE
17.5Bar COUPLING
COKE OVEN GAS
TURBINE
GOVENOR
AUTO/ MANUAL
STATION .
CONTROL PANEL
OIL TANK
HP STEAM 17.5Bar
IN
LP STEAM 1.1Bar
OUT
HP STEAM GAS EXHAUSTER.
1.Auxiliary oil pump cuts out at approximately 4.9 barg
2.Auxiliary oil pump cuts in at approximately 4.2 barg
3.Auxiliary oil pump outlet pressure is approx 4.4 barg
4.Main oil pressure is 5.3 barg
5.Lube oil pressure is 2.0 barg
6.Bearing oil pressure is
7.Low oil pressure trip is
1.2 barg
0.9 barg
TYPES OF PUMP ON PLANT
CENTRIFUGAL PUMP
ELECTRIC MOTOR PUMP SECTION
DRIVE SHAFT
CASINGPOWER SUPPLY
BED PLATE
POSITIVE DISPLACEMENT/ RECIPROCATING PUMP
BASIC BALL VALVE
1.
2.
3.
4.
5.
6.
8.
7.
GATE VALVE
BOLTS
BLAGDON PUMP
1
2.
3.
4.
5.
9.
7.
6.
8. 9.
10.
11.
12.
BUTTERFLY VALVE
ATEX CERTIFIED
ELECTRIC MOTOR HELICAL
CASING
DISK
STEM
PINION SPRING PACK
POWER IN
TORQUE SWITCH
DRIVE SLEEVE
WORM YOKE
FLANGE
AUTOMATIC CONTROL VALVE
RETURN SPRING
DIAPHRAGM
ACTUATOR STOP
STEM
AIR INLET FROM
POSITIONER
RETURN SPRING
STEM SEALS
CONTROLLER SIGNAL
ACTUATOR STOP
COMPRESSED
AIR SUPPLY
PNEUMATIC CONTROL VALVE
BUTTERFLY VALVE
FLANGE
AMMONIA STILL HINDLE VALVE
Pivot Point
Open Solid
Hindle valve in
online position.
Vapour pipework
Spectacle section of hindle
Locking nut
GAS HOLDER SEALANT PUMP TANK

Complete plant equipment and flow drawings

  • 1.
    FULL BENZOLE SYSTEM LevelControl 3.OIL TO VAPOURS 2E401/2. 4.OIL TO OILS 1/2E414. 5.FINAL HEATERS 2E403/4. 6.VAPOUR BOX.2G402 7.BZ STILL120°c 90°c 11. Lean oil in.(27°c). 1/2P406 1/2P405 1/2P404 1/2P401 1/2P401 1/2P402 1/2P407 1/2P408 1/2P409 10.Circulation Tank 9.CREOSOTE COOLERS. 1/2E405/6/7/8 0P409/10 . 2P410 Cooling Water in Cooling water out 2P412 20°c 82°c 18.CONDENSER 17.DEPHLEGMATOR 19.TALLBOY20.BZ SEPERATOR 22.BENZOLE RECIEVER 21.PHLEGM OIL 1P414 OP415/6 1/2T410 23.BENZOLE STORAGE 24.TO OUTLOADING CONDENSATE TO 0T415 TANK MP STEAM 10.5 Bar HEATING COIL 2P424 TO 0T412 SLUDGE TANK 2P414 30°c 12.PURIFIER LP STEAM 1.1Bar 13.Xmas tree 1/2c401 1. BZ WASHER .STRIPPEDOIL 14.PHLEGM OIL FOW 15.OIL BLEED FROM STILL 16.REFLUXED LIGHT ENDS 1T404 2T404 170°c. 108°c 8.WEIR WEIR 2C404 2G401 0G403 2E412/1E4112E411/1E412 2LIC-407 LEVEL CONTROL 0P435 1/2C402 2. BZ WASHER 1/2405 2C403 BENZOLE STILL HAS 14 BUBBLE TRAYS 1/2LIC-404 LEVEL CONTROL RICH OIL TEMP IN 28°c RICH OIL TEMP OUT FROM 1/2c401.( 29°c). LEVEL CONTROL 1/2LIC-406 FLOW CONTROL 1/2FIC-404 2LIC-409 FLOW CONTROL 2FI-405
  • 2.
    1/2P407 Transfer 1/2P408 Transfer 1/2P406 Re-circulation Pump 1/2P405 Re-circulation Pump 1/2P404 Re-circulation Pump 1/2P401 Re-circulation Pump 1/2P402 Re-circulation Pump 1/2P403 Re-circulation Pump Level Control Level Control Gas from Ammonia Washers 27°c BENZOLESCRUBBERS OIL AND GAS FLOWS COKE OVEN GASS TO THE BOOSTERS 29°c 2 5 31/2C402 1/2C401 Lean oil flow control Transfer 1/2P409 CAN OPERATE FOR EITHER 1/2P407/8 1. 2. 1. 1C402 SCRUBBER 2. 1C401 SCRUBBER 3. LEAN OIL FLOW 4. RICH OIL FLOW RICH OIL TO STILL Gas from 1c401. 28°c 1C402 1C401 28°c GAS OUT
  • 3.
    BENZOLE RICH OILFLOW 1/2P401 1/2P402 1/2P403 1/2P408 Level Control LEAN OIL IN 29°c 1C401 SCRUBBER. 2P410 Level Control 1. 2. 3. 4. 5. 6. 1. 1C401 SCRUBBER. 2. OIL TO VAPOURS. 3. OIL TO OILS. 4. FINAL HEATERS. 5. VAPOUR BOX. 6. 2C403 BZ STILL. 7. RICH OIL FLOW. 8. LEAN OIL FLOW. BENZOLE STILL HAS 14 BUBBLE TRAYS OIL TO VAPOURS. OIL TO OILS. FINAL HEATERS. VAPOUR BOX. 2C403 BZ STILL Re-circulation Pump Re-circulation Pump Re-circulation Pump VAPOUR EXITS AT APPROX 108°c. 120°c To oil to oils 90°c 110°c 28°c
  • 4.
    BENZOLE VAPOUR RECOVERY 1. 2 3.4. 5.6. 7.8. 9. 2P414 1P414OP415/6 TO OUTLOADING 1. BENZOLE STILL 2C403. 2. OIL TO VAPOURS. 3. CONDENSOR. 4. DEPHLEGMATOR. 5. TALL BOY. 6. BENZOLE SEPERATOR. 7. PHLEGM OIL TANK. 8. BENZOLE RECIEVER. 9. BENZOLE STORAGE TANK 1/2T405. 10. VAPOUR FLOW. 11. PHLEGM OIL/CONDY. 12. PHLEGM OIL. 13. BENZOLE/CONDY. 14. BENZOLE. 15. COOLING WATER. 16. CONDENSATE. 20°c 82°c COOLING WATER IN COOLING WATER OUT COOLING WATER IN COOLING WATER OUT 1/2T410 VAPOUR EXITS AT APPROX 107/8°c. BENZOLE STILL HAS 14 BUBBLE TRAYS BENZOLE STILL OIL TO VAPOURS OIL TO VAPOURS CONDENSER DEPHLEGMATOR BZ SEPERATOR TALLBOY BENZOLE RECIEVER PHLEGM OIL BENZOLE STORAGE 2C403 Condensate to 0T415 90°c
  • 5.
    Cooling Water in Coolingwater out Creosote coolers Circulation Tank 2P412 Flow controller 1/2C402 scrubber Oil to oil heat exchangers Level control 2P410 2. 3. 4. 5. BENZOLE LEAN OIL FLOW 1. 1. 2C403 BZ STILL. 2. OIL TO OILS. 3. CREOSOTE COOLERS. 4. 1/2T405. 5. 1/2C402 SCRUBBER. 6. LEAN OIL FLOW. 1/2T405. 2C403 BZ STILL. BENZOLE STILL HAS 14 BUBBLE TRAYS 2P411 CAN OPERATE FOR EITHER 2P410/12 30°c
  • 6.
    PURIFIER AND STILLSET UP 2C403 BZ STILL. PURIFIER 4. LP STEAM 1.1 Bar 6. RICH OIL IN VAPOUR OUT 5. MP STEAM 10.5 Bar HEATING COIL 2P424 8. TO 0T412 SLUDGE TANK 1. 2. 3. 1. VAPOUR BOX. 2. 2C403 BZ STILL. 3. 2C404 PURIFIER. 4. LP STEAM. 1.1 Bar 5. MP STEAM. 6. RICH OIL. 7. XMAS TREE. 8. HEAVY ENDS. 7. XMAS TREE Level Control BENZOLE STILL HAS 14 BUBBLE TRAYS 2C404 VAPOUR BOX 120°c 170°c 108°c
  • 7.
    3. ODT 2.Seal pot Main Naphthalene Washer 1 Demisterpad 17.Heating coil LP 1.1Bar 1/2p202 1/2p201 1/2P215 COMMON PUMP 000000 8 8 6 6 SEPERATOR 0G202 NAPTHALENE STORAGE TANK 0T204 40°c 18.Heating coil LP 1.1Bar. Oc202 NAPHTHALENE STILL CONDENSOR.40°c 0E202 120°c TO BENZOLE PRODUCT TANK CONDENSATE TO 0T415.7 BUBBLE TRAYS 7 BUBBLE TRAYS 14.TO 0T412 SLUDGE TANK 115°c 1/2P211, 0P212 8.LEAN OIL TO MAIN NAPHTHALENE WASHER 19.Cooling water coil Divide tank 0T203 FULL NAPHTHALENE SYSTEM 5. 6. 12. 10 7. 9. 11 13 15. 16. MAIN HEATER. MP STEAM 140°c 0E201 4. RICH OIL FROM MAIN NAPHTHALENE WASHERS. 42°c 22. 21. GAS TO AMMONIA WASHERS 43°c 23.LP STEAM 1.1Bar 120oc 45oc COOLING WATER IN. COOLING WATER OUT. 2P424 GAS IN FROM DETARRERS 38-40°c LEVEL CONTROL MP STEAM 10.5 Bar CONTROL VALVE FLOW CONTROL FLOW CONTROL 0P218 0C202 1/2T201 LEVEL CONTROL
  • 8.
    1. 1/2C201 NAPHTHALENEWASHER. 2. SEAL POT. 3. OIL DECANTER TANK. 4. DEWATERING POINT. GAS FLOW. OIL FLOW. LEAN OIL. RICH OIL. Seal pot Main Naphthalene Washer 1/2P202 6. Petroleum oil circulation 1/2P201 petroleum oil circulation 5. Gas in from detarrer,s 10.Gas to ammonia washers 1 24 Demister pad 9. Heating coil LP 1.1Bar MAIN NAPHTHALENE WASHER FLOWS 7. LEAN OIL FROM DIVIDE TANK 8. RICH OIL TO STILL Aim is 1-2°c higher than entry temperature OIL DECANTER TANK 1/2T201 3 . Dewatering point 1/2p215 Operates for either 1/2p201/2 4
  • 9.
    1/2P211, 0P212 Divide tank MP steam10.5 BAR Temperature control Valve 140 ° C 1. 2. 3. Naphthalene vapour Condensate to fire fighting pump house heating Cooling water coil 5. LEAN OIL TO MAIN NAPHTHALENE WASHER 4. RICH OIL FROM MAIN NAPHTHALENE WASHERS. 42°c NAPHTHALENE STILL 0C202 OIL FLOWS 1. 0C202 NAPHTHALENE STILL 2. DIVIDE TANK. 3. MAIN HEATER. 140°c 4. RICH OIL FLOW 5. LEAN OIL FLOW 0C202 NAPHTHALENE STILL MAIN HEATER. 140°c 120°c 115°c 120°c 7 BUBBLE TRAYS 7 BUBBLE TRAYS
  • 10.
    NAPHTHALENE VAPOUR FLOW column 1. NAPHTHALENE STILL 7.Naphthalene vapour 000000 8 8 6 6 CONDENSOR . 40°c 5. 2. 3. 6. 1. 0C202 NAPHTHALENE STILL 2. KNOCKOUT POT. 3. CONDENSOR. 4. ADJUSTABLE WEIR. 5. SEPERATOR. 6. NAPTHALENE STORAGE TANK. 7. VAPOUR FLOW. 8. REFLUX LINE. 9. LOW PRESSURE STEAM.1.1bar. 10. HEATING COIL. 11. CONDENSATE/NAP OIL. 12. NAPHTHALENE OIL. 13. CONDENSATE. 4 8. 9. LP STEAM 1.1 Bar 10.Heating coil. 11. TO 0T412 SLUDGE TANK TO BENZOLE PRODUCT TANK 13. CONDENSATE TO 0T415. NAPTHALENE STORAGE TANK 0T204 SEPERATOR 0G202 0C202 40°c 7 BUBBLE TRAYS 7 BUBBLE TRAYS 120°c LIQUID REFLUXED BACK INTO THE STILL 0P205/6
  • 11.
    1/2p311/2 1/2p314/5 To lime sump GAS TOBENZOLE WASHERS 27°c COOLING WATER IN COOLING WATER OUT VAPOUR OUT DEPHLEGMATOR 1/2E304 85°c Heat exchangers 1/2e306 PLATE COOLER 1/2E308 TO INCINERATOR 1/2F301 1/2T301 1/2C302 1/2C301 GAS FROM NAPHTHALENE WASHERS 40°c 1/2337 1/2P303 1/2P302 1/2P301/7 1/2P308 1/2P309 1/2P310 COMMON PUMP 1/2P319 GAS OUT 28°C COOLING WATER IN SECONDARY COOLERS KNOCKOUT POT AMMONIA STRONG LIQUOR FLOW 1/2p306 1/2p304 1/2p305 LEVEL CONTROL STRONG LIQUOR STORAGE AMMONIA STILL 1/2C303 LEVEL CONTROL 18m³/HR. 1c302 18m³/HR. 2c302 INTO SUCTION OF 1/2P306 LEVEL CONTROL FLOW CONTROL 40m³/HR. 1/2T305 STRONG LIQUOR TANKS 1/2t301 1. 2. 1. 3. 1. 6. 5. 4. 10. 8. 7. 9. 11. 12. 13. 14. 15 VALVE TRAYS 15.
  • 12.
    1/2p306 1/2p305 1/2p304 1/2p337 1/2p307 1/2p302 1/2p303 AMMONIA SCRUBBERS 1/2P308 1/2P310 1/2P309 TO 1/2T301 GASFROM MAIN NAP WASHERS 40° GAS TO BENZOLE SCRUBBERS 27°c 1/2c302 1/2c301 FROM 1/2C303 28°c SECONDARY COOLERS LEVEL CONTROL LEVEL CONTROL FLOW CONTROL
  • 13.
    1/2C303 FREE STILLSTRONG LIQUOR FLOW DEPLEGMATOR 85°c K/O POT 1/2C303 15 VALVE TRAYS HEAT EXCHANGERS 1/2E306 COOLING WATER IN PLATE COOLERS 1/2E308 COOLING WATER OUT COOLING WATER IN COOLING WATER OUT 18m³/HR STRIPPED LIQUOR TO 1C302 18m³/HR STRIPPED LIQUOR TO 2C302 1/2T301 STRONG LIQUOR STORAGE 40m³/HR STRONG LIQUOR TO 1/2C303 40m³/HR STRONG LIQUOR 36m³/HR STRIPPED LIQUOR OUT VAPOUR TO 1/2F301 INCINERATOR REFLUX LINE LP STEAM IN. 1.1Bar APPROX 4m³/HR STRIPPED LIQUOR TO LIME SUMP 1/2P319 1/2p314/5 1/2p311/2
  • 14.
    1/2C304 AND 0C305FIXED AND FREE STILLS LP STEAM 1.1 Bar FIXED SECTION FREE SECTION CAUSTIC IN FIXED AMMONIA VIRGIN LIQUOR INVIRGIN LIQUOR INCAUSTIC IN VAPOUR OUT TO 1/2F301 INCINERATOR VAPOUR OUT TO 1/2F301 INCINERATOR STRIPPED LIQUOR TO LIME SUMP STRIPPED LIQUOR TO LIME SUMP 8 BUBBLE TRAYS 9 BUBBLE TRAYS 0C305 1/2C304 LP STEAM 1.1 Bar 19 VALVE TRAYS BLEED TO ANALYSERS
  • 15.
    0C305 FIXED ANDFREE STILL FLOWS COOLING WATER IN COOLING WATER OUT VAPOUR TO 1/2F301 INCINERATOR K/O POT REFLUX LINE LP STEAM 1.1 Bar LEVEL CONTROL STRIPPED LIQUOR TO LIME SUMP BLEED TO ANALYSERS DEPLEGMATOR 85°c 0C305 0/1/2T105, 0T112 VIRGIN LIQUOR STORAGE TRANSFER PUMPS 0P126,1/2P117,1/2P312 CAUSTIC PUMP CAUSTIC TANK 0T312/3 +30°c HEATING COIL LP 1.1Bar CAUSTIC FROM TANKER OFFLOADING POINT
  • 16.
    TAR AND LIQUORFLOWS 0T112 VIRGIN LIQUOR DOWNCOMER
  • 17.
  • 18.
  • 19.
  • 20.
    BY-PRODUCTS PLANT EQUIPMENT PLATECOOLER 1E308 Hot liquor in Cooled liquor out Cold water In from cooling tower Hot water out to cooling tower
  • 21.
    SPIRAL SECONDARY COOLER HOTIN FROM 1/2P301/7 COLD IN FROM COOLING TOWER TO 1/2C302 COOLED LIQUOR OUT HEATED WATER OUT TO COOLING TOWER
  • 22.
    SHELL AND TUBEHEAT EXCHANGER Vapour In Vapour Out COOLING Water Out Product Out COOLING Water In End Views 4 Pass Tube and Shell 1. 4. 2. Flange Flange Dividers Dividers 3. Tubes
  • 23.
    chandelier Insulator Turrets (3 of) Vent Gasseal pot To 0A102 low level sump 1 6 TOP FLUSH BOTTOM FLUSH Gas In From Exhauster 30°c Gas out to main Naphthalene washer 40°c Flow Control Valve Flow Control Valve Tar Loaded Coke Oven Gas Nitrogen In HV Rectifier Power In Flushing Liquor Turret temperature maintained between 30°c and 70°c 1V101 AND 2V102 DETARRERS Electrode wires Tension Weights
  • 24.
    DETARRED INTERNAL VIEWOF CHANDELIER DETARRER CASING CHANDELIER WIRES TENSION WEIGHTS 139 HEXAGONAL TUBES ENCORPORATING ELECTRODE WIRE ELECTRODE WIRE FROM CHANDELIER
  • 25.
    PRIMARY COOLERS 1/2C101/2 8No tar sprays Only 4 in service At any time 9 No Liquor Sprays 9 No Liquor Sprays Liquor In Liquor In Liquor Out Liquor Out 1p103/2p101 Spiral Coolers 1/2p102 1/2p112 Gas In Tar In 5m³/hr. Gas Out Common Standby 1p101/2p119 Low Level Sump Tar & Liquor Decanters Desludging Point Rodding Point Syphon Breaker Overflow Gas In 726m³/HR. 28oC
  • 26.
    From downcomer (all units) From primary coolers (allunits) From low level sump 0A102 Spiral coolers hot flush discharge line (1 & 3 only Sludge scraper Tar weir Liquor overflow Sludge skip Chute Baffles To 1/2T102 pump tank To 0T104/111 Liquor receiving tank TAR & LIQUOR DECANTERS Xmas tree Desired tar level SLUDGE SKIP EMPTIED INTO TAR POND ROT To Tar Storage Excess Liquor to 0,1,2T105/ 0T112 Virgin Tanks 1/2p121/2
  • 27.
    Gas Booster 1/2B501/0B502 ElectricMotor Fluid Coupling Oil Filter Aux. Lube Pump/Motor Lube Oil Cooler Gas Inlet Outlet Booster Gear Box Fluid Coupling Motor Speed Control Unit FLUID DRIVE Heaters & Thermostats Water Oil Filters Instrument Panel Auxiliary oil pump pressure 2.2 barg Auxiliary oil pump stops & main pump takes over at 2.75 barg Auxiliary oil pump restarts at 2.15 barg Oil temperature trip set at 10 DegC
  • 28.
    AUTO / MANUAL HPSTEAM TURBINE 17.5Bar COUPLING COKE OVEN GAS TURBINE GOVENOR AUTO/ MANUAL STATION . CONTROL PANEL OIL TANK HP STEAM 17.5Bar IN LP STEAM 1.1Bar OUT HP STEAM GAS EXHAUSTER. 1.Auxiliary oil pump cuts out at approximately 4.9 barg 2.Auxiliary oil pump cuts in at approximately 4.2 barg 3.Auxiliary oil pump outlet pressure is approx 4.4 barg 4.Main oil pressure is 5.3 barg 5.Lube oil pressure is 2.0 barg 6.Bearing oil pressure is 7.Low oil pressure trip is 1.2 barg 0.9 barg
  • 29.
    TYPES OF PUMPON PLANT CENTRIFUGAL PUMP ELECTRIC MOTOR PUMP SECTION DRIVE SHAFT CASINGPOWER SUPPLY BED PLATE
  • 30.
  • 31.
  • 32.
  • 33.
  • 34.
  • 35.
    ATEX CERTIFIED ELECTRIC MOTORHELICAL CASING DISK STEM PINION SPRING PACK POWER IN TORQUE SWITCH DRIVE SLEEVE WORM YOKE FLANGE AUTOMATIC CONTROL VALVE
  • 36.
    RETURN SPRING DIAPHRAGM ACTUATOR STOP STEM AIRINLET FROM POSITIONER RETURN SPRING STEM SEALS CONTROLLER SIGNAL ACTUATOR STOP COMPRESSED AIR SUPPLY PNEUMATIC CONTROL VALVE BUTTERFLY VALVE FLANGE
  • 38.
    AMMONIA STILL HINDLEVALVE Pivot Point Open Solid Hindle valve in online position. Vapour pipework Spectacle section of hindle Locking nut
  • 40.