AEA Technology OHT presentation...
Transcript of AEA Technology OHT presentation...
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Production Planning Department
MIDOR Refinery
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Tiered Margin
MIDOR Refinery
Configuration
Hydro-cracking
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Production Planning Department
MIDOR Refinery
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Midor refinery configuration AL/AH 50/50 @ 100%
CRUDE
DISTILL.
UNIT
VACUUM
DISTILL.
UNIT
NAPHTHA
HDT SPLITTER
ISOM.
CCR
KERO
MEROX
DIESEL
HDS
HYDRO
CRACKER
DELAYED
COKER
HYDROGEN
AMINE &
SULPHUR
PREMIUM &
REGULAR
GASOLINE RON 95/98
KERO/JET
DIESEL
COKE
SULPHUR
CRUDE
ISOMERATE
REFORMATE
KEROSENE
DIESEL OIL
COKE
LPG
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Production Planning Department
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CDU Case (Topping Scheme)
CRUDE
DISTILL.
UNIT
VACUUM
DISTILL.
UNIT
KERO
MEROX
NAPHTHA
KERO/JET
DIESEL
CRUDE
KEROSENE
LPG
LVGO
HVGO
VR
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Production Planning Department
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NHT Case (Hydro skimming Scheme)
CRUDE
DISTILL.
UNIT
VACUUM
DISTILL.
UNIT
NAPHTHA
HDT SPLITTER
ISOM.
CCR
KERO
MEROX
DIESEL
HDS
HYDROGEN
AMINE &
SULPHUR
PREMIUM &
REGULAR
GASOLINE RON 95/98
KERO/JET
DIESEL
CRUDE
ISOMERATE
REFORMATE
KEROSENE
DIESEL OIL
LPG
LVGO
HVGO
VR
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Production Planning Department
MIDOR Refinery
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HC Case (Conversion Scheme)
CRUDE
DISTILL.
UNIT
VACUUM
DISTILL.
UNIT
NAPHTHA
HDT SPLITTER
ISOM.
CCR
KERO
MEROX
DIESEL
HDS
HYDRO
CRACKER
HYDROGEN
AMINE &
SULPHUR
PREMIUM &
REGULAR
GASOLINE RON 95/98
KERO/JET
DIESEL
CRUDE
ISOMERATE
REFORMATE
KEROSENE
DIESEL OIL
LPG
VR
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Production Planning Department
MIDOR Refinery
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Coker Case (Full Conversion)
CRUDE
DISTILL.
UNIT
VACUUM
DISTILL.
UNIT
NAPHTHA
HDT SPLITTER
ISOM.
CCR
KERO
MEROX
DIESEL
HDS
HYDRO
CRACKER
DELAYED
COKER
HYDROGEN
AMINE &
SULPHUR
PREMIUM &
REGULAR
GASOLINE RON 95/98
KERO/JET
DIESEL
COKE
SULPHUR
CRUDE
ISOMERATE
REFORMATE
KEROSENE
DIESEL OIL
COKE
LPG
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Production Planning Department
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180
300
210
405
0
50
100
150
200
250
300
350
400
450
Top
ping
Hyd
rosk
imm
ing
Con
version
Full conve
rsion
Production (TPD)
LPG
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Production Planning Department
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0 0 00
19602140
2540
1790
0
500
1000
1500
2000
2500
3000
Toppin
g
Hyd
rosk
imm
ing
Conve
rsio
n
Full
Convers
ion
Naphtha Gasoline
Production (TPD)
Gasoline / Naphtha
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Production Planning Department
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1,260
2,950
1,320
3,320
0
500
1000
1500
2000
2500
3000
3500
Toppin
g
Hyd
rosk
imm
ing
Conve
rsio
n
Full
Convers
ion
Production (TPD)
Jet
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Production Planning Department
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3,570
4,350
3,070
5,800
2000
2500
3000
3500
4000
4500
5000
5500
6000
Toppin
g
Hyd
rosk
imm
ing
Conve
rsio
n
Full
Convers
ion
Production (TPD)
Diesel
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• Product Sales 11,251 11,380 11,870 11,993
Topping Hydro skimming Conversion Full Conversion
• Gross Margin 357 496 956 1,080
• Feedstock
Purchases 10,894 10,884 10,914 10,913
Economic Summary Analysis (000,US$/Day)
• Volume
Expenses 26 46 76 100
• Net Operating
Margin 331 450 880 980
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Production Planning Department
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34.0
11.0
43.0
13.0
Topping Hydroskimming (Nap) Conversion (HCR) Full Conversion (CKR)
Contribution to Refinery Margin %
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Production Planning Department
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0123456789
101112
Toppin
g
Hyd
rosk
imm
ing
Conve
rsio
n
Full C
onve
rsio
n
US
$/B
L
Gross Margin Vol-EXP OPT Margin
Non-Vol EXP Net Margin
Gross ,Opt and Net Margins
MIDOR REFINERY
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Production Planning Department
MIDOR Refinery
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Hydrocracker is the heart
Of MIDOR Refinery