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.
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
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
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
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