1. Fri Jul 17 14:31:50 2015Case: H:OSum09 - Simulations & Simulation SummariesJack- simulationOSUM 9000 BPD OF PHASE 1 - CURRENT OPERATING REV Aa.HSCFlowsheet: Case (Main)
T
Bitumen
Treating
T
PG
System
T
De-Oiling
T
Water
Treatment
T
BFW &
Steam
T
Diluent
& Dilbit
T
Fuel
Gas
T
VRU
T
Glycol
T
Emulsion
Annulus
Gas
Diluent
Produced
Vapours
Phase 1- Current
Operating Conditions
The WSR will be
confirmed and Adjusted.
Base Case: WSR 1.03,
SOR 3.30, GOR 20 ,
Rev A
Produced
Gas
Dilbit
Design
Check
HP
Steam
BFW
92
4916
C
tonne/d
Slop
Oil
De-Oiled
Water
Waste
Water to
Disposal
Well
Pads
Hidden Streams:
1. <slop oil> from De-Oiling to
Bitumen Treating
2. <Dilbit/Diluent Tank Vent>
from Diluent & Dilbit to VRU
3. <De-Oiled Vent> from
De-Oiling to VRU
4. <Recovered Vapours> from
VRU to PG System
5. <Flashed Vapours> from
BFW&Steam to PG System
6. <BD Condensate> from
BFW&Steam to De-Oiling
7. <Recovered Diluent> from
PG System to Diluent & Dilbit
8. <Pump Seal Flush> from
BFW&Steam to De-Oiling
9. <Seal Flush to Evap> from
BFW&Steam to Water
Treatment
10. <Dilution Water> from
BFW&Steam to De-Oiling
11. <Makeup Water> from
De-Oiling to Water Treatment
12. <PW from PG Sep> from
PG System to De-Oiling
13. <Condensed Water> from
Water Treatment to De-Oiling
14. <VRU Water> from VRU to
De-Oiling
15. <Rec. Diluent> from VRU
to Diluent & Dilbit
BD
Condensate
Excess
PW
ADJ-Steam
Rate
A
Rec.
Diluent
Utility
Water
153
Oily
Water
MB-114
2. Fri Jul 17 14:32:28 2015Case: H:OSum09 - Simulations & Simulation SummariesJack- simulationOSUM 9000 BPD OF PHASE 1 - CURRENT OPERATING REV Aa.HSCFlowsheet: Well Pads (TPL1)
905
Dry
Annulus
Gas
Emulsion
in Heel
Annulus
Gas
Emulsion
Dry AG
to
Annulus
Produced
Water
Bitumen
PG
Sub-Cool
S
-14.2 C
MIX-101 TEE-102
MIX-103
Well
Pads
XXXbpd
-
Bitumen
Reservoir
Design
Basis
Table
E-100
P-9010/9011
Produced
Gas Lab
Data
Saturated
steam
V-9001
VLV-101 VLV-103
MIX-102
2 4 5
904
7
VLV-104
MIX-104
TEE-100
3
11
Aajust the
Operating
temperature
to match
Current
Operation
Conditions
of the Group
Sep.
3. Fri Jul 17 14:18:32 2015Case: H:OSum09 - Simulations & Simulation SummariesJack- simulationOSUM 9000 BPD OF PHASE 1 - CURRENT OPERATING REV Aa.HSCFlowsheet: Bitumen Treating (TPL2)
Emulsion
VLV-100 VLV-101
101A 3
V-1000
V-1002
MIX-100
MB-101 5
103 Dilbit
Emulsion
PW
from
FWKO
MIX-101VLV-102
8
MB-103
10
106
104
E-1023/1024
7
VLV-103
MIX-102
VLV-104
116
14
15 Produced
Water
16
VLV-105
105
VLV-106
MB-112
VLV-107
MB-113
123-PRODUCED
GAS
712
TEE-100
713
714
Carryover:
33% water
in dilbit to
match the
current
operating
conditions;
2500ppm
oil in PW
Carryover:
0.50%
water in
dilbit,
2500ppm
oil in PW
Bitumen
Treating
109.4 C
Slop
Oil RCY-1
R
203
E-1029/1030
E-1043/1044/1045/1046
722 tonne/d
VLV-108
200
E-1017/1018/1019
1
MIX-103
P-1102/1101
DB-6
Q-100
ADJ-1
A
E-100 TEMP LOSS ON THE PIPEL INE
Q-101
2
Current
Operating
Temperature
at 105C
4. Fri Jul 17 14:22:06 2015Case: H:OSum09 - Simulations & Simulation SummariesJack- simulationOSUM 9000 BPD OF PHASE 1 - CURRENT OPERATING REV Aa.HSCFlowsheet: Diluent & Dilbit (TPL7)
Diluent
Tank
()
Dilbit Tanks
T-6001/6002/6003 Shipping
Booster
Pumps
GC
Diluent
Tank
Vent
3
Dilbit
Tank
Vent
712
Diluent
Pumps
702
2
711
701
MIX-100
5
MIX-101
HP
Diluent
Pumps
TEE-100
HP
Dilbit
Pumps
105Dilbit
MIX-102
919
Dilbit
Vent
Dilbit &
Diluent
Systems
dummy
stream
109
No Sales
Oil Trim
Diluent
During
Truck Out
Operations
Phase
1 DBM
Diluent
5. Fri Jul 17 14:20:14 2015Case: H:OSum09 - Simulations & Simulation SummariesJack- simulationOSUM 9000 BPD OF PHASE 1 - CURRENT OPERATING REV Aa.HSCFlowsheet: De-Oiling (TPL4)
MIX-100
30
MB-203
2
50%
slop
Skim
Tank
T-2000
204
Carryover:
50% water
in oil,
250 ppmv
oil in PW
IGF
Vessel
(V-
2031)
10%
slop
5
IGF
Water
Carryover:
90% water
in oil,
25 ppmv oil
in PW
VLV-100
Skim
Tanks
Skim
Slop
Oil
Tank
T-
2002
3
Slop
Oil
Slop
PW
Slop Oil
Pumps P-
2020/2021
207
Slop
PW
Pump
7
Carryover:
25% water
in slop oil,
250 ppmv
oil in Slop
PW
MIX-101
918
Deoiled
Vent
IGF Froth
Pump (P-
2016/2017)
VLV-101
202
De-oil
Water
Tank
(T-2026)
IGF Discharge
Pumps
(P-2010/2011)
157
VLV-102
13
14
15
De-oiled
Water Pumps
(P-2033/2034)
209
VLV-103
6
RCY-2
R
172
TO
ORF
MIX-103
X-100
171
22
23
SET-1
S
Brackish
Water
TankT-5503
Source
Water
from
Well
TEE-100
29
Make-up Water
Pumps
P-5504/5505/5506
From
Brakish
Water
Wells
Skim Oil
Pumps
P-2014/2015
201
TEE-102
32
<176>
Excess
PW
161VRU
WATER
1
31
Utility Water
Tank(T-5556)
36
UW Pumps
(P-5557/5558)
TEE-103
38
953Pump
Seal
Flush-
950
TEE-105
MB-212
FWKO
Treater
Quench
<empty>
188 tonne/d
Utility
Water
222 tonne/d
UW
to
VRU
88
5177
C
tonne/d
ORFs
(2
Units-)
0.74 tonne/d
UW
stations
& other
users
MIX-102
9
10
167
NNF
NNF
DUMMY
QDUMMY
PUMP
SEAL
FLUSH
MB-201
MB-214
200
4
MIX-106
TBD
MIX-107
MB-203A
MIX-105
MIX-104
TBD
206
MIX-108
6. Fri Jul 17 14:21:09 2015Case: H:OSum09 - Simulations & Simulation SummariesJack- simulationOSUM 9000 BPD OF PHASE 1 - CURRENT OPERATING REV Aa.HSCFlowsheet: Water Treatment (TPL5)
MIX-100
175
dummy
heater
Evaporator
6
7
Blowdown
TEE-100
9
10
dummy
cooler2
Waste Water
Tank(TK-101/105)
ADJ-BD
Rate
A
Evap
Distillate
VLV-102
20
13
14
P-3838/3839
Brine Disposal
Pumps
(P-3835/3836)
15
302
VLV-103
300
Water
Treatment
MB-209
88.6
4859.2
C
tonne/d
RCY-1
R
17
336.2 tonne/d
RCY-2
R
8
0.0 tonne/d
dummy
cooler1
18
Vent
Condenser
Vent
to
Atm.
176
Excess
PW
MIX-101
301
105 C
4916 tonne/d
92 C
16A
MB-212
MIX-1021A
RCY-3
R
BD
Condensate
TK-102/103
1
2
MIX-103
Waste
Water to
Disposal
T-3005
3
4
P-3010/3011/3012
11
Q-100
VLV-101
12
7. Fri Jul 17 14:23:12 2015Case: H:OSum09 - Simulations & Simulation SummariesJack- simulationOSUM 9000 BPD OF PHASE 1 - CURRENT OPERATING REV Aa.HSCFlowsheet: Fuel Gas (TPL8)
510
From
Alta
Gas
Fuel Gas
Heater
(E-5100)TEE-100
512
511
To
Others
MP
Letdown
904
ESDV
Others
TEE-101
6
LP
Letdown
TEE-102
FG to
Drum
Boilers
8
V-5105
MIX-100
514
10
516
517
MP
FG
12
Utility
FG
Letdown
905
Utility
FG
MB-111
Fuel
Gas
System
NNF
NNF
521
The
Natural
Gas
Source
Changed
VLV-100
1
8. Fri Jul 17 14:26:03 2015Case: H:OSum09 - Simulations & Simulation SummariesJack- simulationOSUM 9000 BPD OF PHASE 1 - CURRENT OPERATING REV Aa.HSCFlowsheet: Glycol (TPL10)
960
P-7001/7002
3 1
No need to
connect loop
(to aid
simulation
convergance)
Cooling
Supply
Header
702
702B
701 701B
PW Cooler
E-1029/1030
Emulsion Cooler
E-1017/1018/1019
704
Dilbit Cooler
E-1043/1044/1045/1046
High
Level
Heat
969
704B
10
Heating
Supply
Header
713
713B
Fuel
Gas
Heater
MIX-100
12
Hot
Header
Bypass
VRU Suction
Coolers
E-5203/5223
706 706B
Combustion
Air Heaters
Combustion
Air In
Combustion
Air To
Boilers
971 16
Heating
Bypass
13
MIX-101
14
MIX-102
977
975
MIX-103
Glycol
System
Tanks
Heating
Building
Heaters
715 715B
714 714B
If heating
supply
header
bypass
shows
negative
flow, then
the
Combustion
Air Heaters
outlet
temperature
must be
reduced
Glycol
Coolers
QGlycol
Coolers
709
709B
Evap.
Vent
Cooler
Glycol
Heater
708 708B
Utility
Cooling
703
Diluent
Recovery
Cooler E-
1039/1040
703B
705
705B
Boiler
Blowdown
Trim
Cooler E-
4155/4255
707 707B
VRU
Discharge
Coolers
E-5204/5224
E-5100
The Glycol Flow Rate is Smaller than
DCS, It will be further investagated.
