There are (3) major Refineries in Iraq:
1 -Doura Refinery – built in the Fifties of the last Century with a
capacity of (70) kb1/d which was increased to (110) k b1/d by adding
4) 10 (k b1/d units.
2 -Basrah Refinery - built in the seventies of the last Century with a
capacity of (140) kb1/d which was increased to (180) k b1/d by adding
4) 10 (k b1/d units.
3 -Baiji Refinery- built in the seventies and eighties of the last Century
with a capacity of (290) kb1/d which was increased to (310) k b1/d by
adding 2 (10) k b1/d units.
All these refineries .were simple designed to produce white
products not exceeding (50 -55%) of the feed crude. Only
Baiji has a hydrocracker units of (30)kb1/d capacity.
All three refineries have lube oil plants of various capacities.
These refineries sustained severe damage during the 1991
gulf war . They were all fixed and put int operation within
2- 3 months from the end of the said war , but were not
restored to a healthy state . The long period of UN sanction
inflicted more damage due to disrepair&lack of maintenance.
Period April 2003 – Dec 2008 The operation of refineries was adversely affectedby the security situation.
Insurgent & terrorist attacks targeted crude oil& product pipe lines.Refineries suffered frequent stoppage of operation ,either due to lack of crude oil or inability to evacuate products. This applies to the period 2005 – 2007 .
In 2008 there is a definite improvement in the operation thus the daily average for refining has been gradually increasing coupled with decrease ofoil products imports .
Status End 20101- MIDLAND REFINERIES
A- Doura Refinery
Installed Capacity : 210kb 1/d.
- 2 new CDUs,each of 70 kb1/d - both in operation.
- A third Hydrotreater Reformer Unit 10 kb1/d – procurement phase.
- Isomerisation Unit 10 kb1/d – Civil work & supply of equipment phase.
- A power generation station 50 mw – under construction.
- One New Boiler 150 ton/h with Demin Water Unit –completed & in
operation. Second New boiler 150 ton/h under construction.
- An RFCC Unit 40 kb1/d – FEED Package awarded.
- New Cooling Tower – Contract awarded.
Lube Oil Plants
There are 3 Lube Oil plant:
-No:1 – completed 1959 by Foster wheeler - capacity 25 kton/y
present operation at 85% of capacity.
-No:2 – completed 1969 by Snam Projetee – capacity 36 kton/y present operation at 77% of capacity
-No:3 – completed 1978 by Nigata – capacity 60 kton/y- present operation at 94% of capacity
A- Doura Refinery
Future Plans -Replacement of 3 CDUs 70 kb1/d total capacity with one CDU
unit 70 kb1/d .
-Additional treatment of Industrial water including circulation of treated water.
-Improvement of Flare system to reduce emmissions.
-Complete renovation of lube oil plants.
-Replacement of old reformer units with new ones.
-New Gas Oil hydrotreater units
A- Doura Refinery
Status End 2010MIDLAND REFINERIES
B- Najaf Refinery:
- 3 Distillation Units , (10)kb1/d each – in operation.
- A Naphtha Hydrotreater & Reformer unit with all related utilities in the engineering phase.
- Asphalt unit – planned.
Status End 2010MIDLAND REFINERIES
C- Samawa Refinery
-3 Distillation Units , (10)kb1/d each – in operation.
- A Naphtha Hydrotreater & Reformer unit with all related utilities in the engineering phase.
- Asphalt unit – planned
Status End 20101 -MIDLAND REFINERIES
D- Diwanya Refinery
- One Distillation Unit , (10)kb1/d in operation.
- 2rd Distillation Unit , (10)kb1/d under fabrication.
Status End 20102 -NORTH REFINERIES
A- Baiji Refinery Complex – Capacity 310 kb1/d. - New Isomeration Unit – 19.6 kb1/d – Final stages of
construction. - 6 New boilers – 400 ton/hr total capacity -under construction.
- New power generation plants (85)mw – contracted. - New LPG unit for North Refinery , 400 tons/d – Award of
contract under processing. - Upgrading of Waste Water Treatment System – under
implementation. - Re-construction of (51) storage tanks – 9 Nos complete, 80%
completion of remaining tanks. - Rehabilitation & De- bottle necking of Hydro- Cracker Unit –
under evaluation with Designer & Supplier. - New FCC unit 50 kb1/d – Feasibility Completed
Status End 20102 -NORTH REFINERIES
A-Baiji Refinery Complex -Lube Oil Plant , 250 kton/y – at present one train 125 kton/y is
in operation. Second train is under rehabilitation. B- Kirkuk Refinery
- 3 CDU 10kb1/d each – in operation.
C- Kasak Refinery - one 10 kb1/d unit – in operation.
- Second 10 kb1/d unit - civil work construction. - Waste Water Treatment Unit – under construction.
- New Storage Tanks – under construction.
Status End 20102 -NORTH REFINERIES
D- Qayarah Refinery - 4 Old Asphalt Units, one 180 cum /d & three 360 cum/d each -
only one unit 360 cum/d is in operation at 50% capacity. other units are under rehabilitation.
- A new Asphalt Unit is planned . - One 10kb1/d CDU operating on Kirkuk Crude - installed.
- 2rd 10kb1/d CDU operating on Kirkuk Crude - under installation. - 8 storage tanks –under construction.
E- Seeniyah Refinery - Three 10 kb1/d units – in operation
- 10 storage tanks – under construction. - Waste Water Treatment unit – under construction.
Status End 20102 -NORTH REFINERIES
F- Haditha Refinery - 2 units , 16 kb1/d total capacity – in operation.
- 12 storage tanks – under construction. - Waste Water Treatment Unit – planned.
Future Plans - Rehabilitation of Gas Oil Hydrotreating Units.
- Rehabilitation & upgrading of lube plant. - Replacement of old reformer units .
Status End 20103 -SOUTH REFINERIES
A- Basrah Refinery
- New (70) kb1/d Distillation Units with an LPG unit (300) ton/d- under construction.
- Third Hydrotreater Platformer Unit 10kb1/d -under construction.
- New LPG unit (200) ton for Train(1) – procurement phase
- New Isomeriation Unit (11) kb1/d - Delivery of equipment & Site preparation.
- 3 New Boilers , 100 ton/h each – under installation.
- New Waste Water Treatment Plant – Awarded.
- New cooling Tower – under construction.
- New FCC Unit 30 kb1/d – FEED package preparation phase.
- Replacement of old reformer units .
Future Plans
-New Utility Package.
-New Gas oil Hydrotreatment Unit- Design completed.
-New Naphtha hyrotreater unit 15 kb1/d.
-Upgrading of Instrumentation & Control.
-Improvement of Flare System to reduce emmissions.
-Up grading of waste water system & recirculation of treated water.
Status End 20103 -SOUTH REFINERIES
B – Nasiriyah Refinery
- 3 Distillation Units , (10)Kb1/d each in operation.
- A Hydrotreater Reformer unit with all related utilities- Engineering phase .
- A Waste Water Treatment unit – Evaluation of offers.
- An Ro unit 50m3/h completed & in operation.
- Expansion of utilities & tankage – planned.
C- Missan Refinery
- 3 CDUs , 10 kb1/d each – installed & in operation
-year : 2004 404 k b1/d : = -2005 377= : = -2006 356= : = -2007 329= : = -2008 443 = : = -2009 447 =
: = -2010 523= ( Jan- Oct)
Year ton/d Total Value
2004 3658.6 1731.2 million $
2005 7706.3 4517.2= =
2006 2302.7 3517.9= =
2007 2402.5 1749.8= =
2008 2603.4 2345.6= =
2009 2016.0 1272.4= =
2010 1472.0 1077.0= =
End of Aug
*Import for Ministry of Electricity is not included
Consumption of white Products
3000
5000
7000
9000
11000
13000
15000
17000
19000
21000
1975 1980 1985 1990 1995 2000 2005 2010
LegendGasoline
Gas Oil Kerosene
NEW REFINERIES
11 - -Karbala RefineryKarbala Refinery
Capacity 140 000 BPSDCapacity 140 000 BPSD
SITE INFORMATION :
Kerbala Refinery is located about (110) KM South west Of Baghdad.
Area : 4 X 3 Km2 Coordinate U.T.M : .
N : 3580000E : 415000
PROCESS UNITS
1- Atmospheric Distillation Unit (140.000 BPSD)
2- Vacuum Distillation Unit (72.000 BPSD)
3- Naphtha HDS Unit (41.500 BPSD)
4- Reforming Unit (CCR ) (25.500 BPSD)
6- Kerosene HDS Unit (20.000 BPSD)
7- Gas Oil Hydro-Treating Unit (28.000 BPSD)
8- Vacuum Gas Oil Hydrotreater Unit (36.000 BPSD)
9- Fluid Catalytic Cracking Unit (FCC) (31.500 BPSD)
10-Polynaphtha Unit (11.500 BPSD)
11- Hydrogen Production Unit (2X36000 M3/HR )
12- Sulphur Recovery Unit (2 X 180 TPSD)
13- Blown Asphalt Unit (1000 TPSD)
5- C5/C6 Isomerization Unit (12.500 BPSD)
Products Specification will be according to EURO-4 as minimum required.Gasoline , Kerosene &Gas oil with (10 ppm ) Sulphur content .
PRODUCTSPRODUCTS
LPGLPG
GASOLINE (Unleaded Premium, Regular)GASOLINE (Unleaded Premium, Regular)
KEROSENE & ATKKEROSENE & ATK
GAS OIL (Diesel)GAS OIL (Diesel)
HEAVY GAS OIL (Heavy Diesel)HEAVY GAS OIL (Heavy Diesel)
BLOWN ASPHALT (Paving & Many Types of Industrial Blown Asphalt)BLOWN ASPHALT (Paving & Many Types of Industrial Blown Asphalt)
FUEL OIL ( less than 15% vol . of crude)FUEL OIL ( less than 15% vol . of crude)
SULPHURSULPHUR
ELECTRICAL POWER 400 MWELECTRICAL POWER 400 MW
Expected Product Quantities :
PRODUCTSTh.M3/SD
LPG160 T/SD
GASOLINE8.750
ATK/KEROSENE3.000
DIESEL3.85
HEAVY DIESEL0
FUEL OIL3.7
ASPHALT1000 T/SD
SULPHUR175 T/SD
ELECTRICITY100 MW
22--Maissan RefineryMaissan Refinery Capacity 150 000 Capacity 150 000
BPSDBPSD
SITE INFORMATION :
Maissan Refinery is located about )400( KM South Of Baghdad.
Area :) 2 X 3( Km2 Coordinate U.T.M : .
N : 3537000E : 730000
PROCESS UNITS
1- Atmospheric Distillation Unit (150.000 BPSD)
2-Vacuum Distillation Unit (82,300 BPSD)
3-Naphtha Hydro-Treating Unit (31,800 BPSD)
4- Reforming Unit (CCR) (22,500 BPSD)
5-C5/C6 Isomerisation Unit (11,600 BPSD)
6-Saturated LPG Treatment Unit (2,200 BPSD)
7-Kerosene Hydro-Treating Unit (16,700 BPSD)
8-Gas Oil Hydro-Treating Unit (30,300 BPSD)
9-Vacuum Gas Oil Hydro-Cracking Unit (56,300 BPSD)
10-Solvent De-Asphalting Unit (46,700 BPSD)
11-Deasphalted Oil HDT Unit (27,600 BPSD)
12-Fluid Catalytic Cracking (FCC) (42,300 BPSD)
13-Unsaturated LPG Treatment Unit (9,800 BPSD)
14-C3/C4 Alkylation Unit (9,800 BPSD)
15-N C4 Isomerisation Unit (4,000 BPSD)
16-Hydrogen Production Unit (125,000 M3/Hr )
17-Sulphur Recovery Unit (490 TPSD)
18- Blown Asphalt Unit (490 TPSD)
Products Specification will be according to EURO-4 as minimum required.Gasoline , Kerosene &Gas oil with (10 ppm ) Sulphur content .
PRODUCTSPRODUCTS
LPGLPG
GASOLINE (Unleaded Premium, Regular & Super)GASOLINE (Unleaded Premium, Regular & Super)
KEROSENE & ATKKEROSENE & ATK
GAS OIL (Diesel)GAS OIL (Diesel)
HEAVY GAS OIL (Heavy Diesel)HEAVY GAS OIL (Heavy Diesel)
ASPHALT (Paving & Many Types of Industrial Blown Asphalt) ASPHALT (Paving & Many Types of Industrial Blown Asphalt)
FUEL OIL ( less than 15% vol . of crude)FUEL OIL ( less than 15% vol . of crude)
SULPHURSULPHUR
ELECTRICAL POWER 500 MWELECTRICAL POWER 500 MW
Expected Product Quantities :
PRODUCTSTh.M3/SD
LPG250 T/SD
GASOLINE9.000
KEROSENE / ATK2.650
DIESEL7.650
HEAVY DIESEL0.8
FUEL OIL0.432
ASPHALT490 T/SD
SULPHUR490 T/SD
ELECTRICITY500 MW
33 - -Al-Nassiriya RefineryAl-Nassiriya Refinery Capacity 300 000 BPSDCapacity 300 000 BPSD
SITE INFORMATION :
Al-Nassiriya Refinery is located about )400( KM South Of Baghdad.
Refinery Area 5.6 Km2 Coordinates U.T.M : .
N : 3413750E : 622900
PROCESS UNITS (ALTERNATIVE ONE)
1- Atmospheric Distillation Unit
2- Naphtha Hydro Desulphurization Unit
3- Catalytic Reforming Unit (CCR)
4- Light Naphtha Isomerization Unit
5- Kerosene Hydro-Desulphurization Unit
6- Light Gas Oil Hydro-Desulphurization
7- Vacuum Distillation Unit
8- Vacuum Gas Oil Hydro-Desulphurization Unit
9- Vacuum Gas Oil Catalytic Cracking Unit (FCC)
10- Vacuum Gas Oil Hydorcracking Unit
11- Blown Asphalt Production Unit
12- C3, C4 Olefins Alkylation Unit
13- NC4 Isomerization Unit
14- Hydrogen Production Unit
15- Gas Sweetening Unit
16- Sulphur Recovery Unit
17- LPG Production Unit
PROCESS UNITS (ALTERNATIVE TWO)
1- Atmospheric Distillation Unit
2- Naphtha Hydro Desulphurization Unit
3- Catalytic Reforming Unit( CCR)
4- Light Naphtha Isomerization Unit
5- Kerosene Hydro-Desulphurization Unit
6- Light Gas Oil Hydro-Desulphurization
7- Vacuum Distillation Unit
8- Vacuum Gas Oil Hydro-Desulphurization Unit
9- Vacuum Gas Oil Fluid Catalytic Cracking Unit(FCC)
10- Vacuum Gas Oil Hydorcracking Unit
11- Vacuum Residue Solvent Deasphalting Unit (SDA)
12-DAO Hydro-Desulphurization Unit
13- C3, C4 Olefins Alkylation Unit
14- NC4 Isomerization Unit
15- Hydrogen Production Unit
16- Gas Sweetening Unit
17- Sulphur Recovery Unit
18 -LPG Production Unit
19-Blown Asphalt Production Unit
PROCESS UNITS (ALTERNATIVE THREE)
1- Atmospheric Distillation Unit
2- Naphtha Hydro Desulphurization Unit
3- Catalytic Reforming Unit (CCR)
4- Light Naphtha Isomerization Unit
5- Kerosene Hydro-Desulphurization Unit
6- Light Gas Oil Hydro-Desulphurization
7- Vacuum Distillation Unit
8- Vacuum Gas Oil Hydro-Desulphurization Unit
9- Vacuum Gas Oil Fluid Catalytic Cracking Unit (FCC)
10- Vacuum Gas Oil Hydrocracking Unit
11- Vacuum Residue H.Oil Unit
12- Blown Asphalt Production Unit
13- C3,C4 Olefins Alkylation Unit
14- NC4 Isomerization Unit
15- Hydrogen Production Unit
16- Gas Sweetening Unit
17- Sulphur Recovery Unit
18- LPG Production Unit
PROCESS UNITS (ALTERNATIVE FOUR)
1- Atmospheric Distillation Unit
2- Naphtha Hydro Desulphurization Unit
3- Catalytic Reforming Unit (CCR)
4- Light Naphtha Isomerization Unit
5- Kerosene Hydro-Desulphurization Unit
6- Light Gas Oil Hydro-Desulphurization
7- Vacuum Distillation Unit
8- Vacuum Gas Oil Hydro-Desulphurization Unit
9- Vacuum Gas Oil Fluid Catalytic Cracking Unit (FCC)
10- Vacuum Gas Oil Hydrocracking Unit
11- Vacuum Residue Coking Unit
12- C3,C4 Olefins Alkylation Unit
13- NC4 Isomerization Unit
14- Hydrogen Production Unit
15- Gas Sweetening Unit
16- Sulphur Recovery Unit
17- LPG Production Unit
18- Blown Asphalt Production Unit
PROCESS UNITS (ALTERNATIVE FIVE)
1- Atmospheric Distillation Unit
2- Naphtha Hydro Desulphurization Unit
3- Catalytic Reforming Unit (CCR)
4- Light Naphtha Isomerization Unit
5- Kerosene Hydro-Desulphurization Unit
6- Light Gas Oil Hydro-Desulphurization
7- Atmospheric Residue Hydro-Desulphurization Unit
8- Atmospheric Residue RFCC Unit (for gasoline production)
9- Atmospheric Residue RFCC Unit (for diesel production)
10- C3,C4 Olefins Alkylation Unit
11- NC4 Isomerization Unit
12- Hydrogen Production Unit
13- Gas Sweetening Unit
14- Sulphur Recovery Unit
15- LPG Production Unit
18- Blown Asphalt Production Unit
PROCESS UNITS (ALTERNATIVE SIX)
1- Atmospheric Distillation Unit
2- Naphtha HDs Unit
3- Catalytic Reforming Unit (CCR)
4- Light Naphtha Isomerization Unit
5- Kerosene Hydro-Desulphurization Unit
6- Light Gas Oil Hydro-Desulphurization
7- Vacuum Distillation Unit
8- (VGO / DAO) Catalytic Cracking Unit
9- Vacuum Residue SDA Unit
10- (VGO / DAO) Hydorcracking Unit
11- VGO / DAO HDS
12- C3, C4 Olefins Alkylation Unit
13- NC4 Isomerization Unit
14- Hydrogen Production Plant
15- Gas Sweetening Unit
16- Sulphur Recovery Unit
17- LPG Production Unit
18- Blown Asphalt Production Unit
Products Specification will be according to EURO-4 as minimum required.Gasoline , Kerosene &Gas oil with (10 ppm ) Sulphur content .
PRODUCTSPRODUCTS
LPGLPG
GASOLINE Unleaded (Premium, Regular & Super)GASOLINE Unleaded (Premium, Regular & Super)
KEROSENE & ATKKEROSENE & ATK
GAS OIL (Diesel)GAS OIL (Diesel)
HEAVY GAS OIL (Heavy Diesel)HEAVY GAS OIL (Heavy Diesel)
ASPHALT (Paving & Many Types of Industrial Blown Asphalt)ASPHALT (Paving & Many Types of Industrial Blown Asphalt)
FUEL OIL ( less than 15% vol . of crude)FUEL OIL ( less than 15% vol . of crude)
SULPHURSULPHUR
ELECTRICAL POWER 600 MWELECTRICAL POWER 600 MW
Expected Product Quantities :
PRODUCTSTh.M3 /D
LPG1200 T/D
GASOLINE14.000
KEROSENE /ATK7.000
DIESEL12.000
HEAVY DIESEL4.000
REFINERY FUEL OIL6.500
ASPHALTT/D
SULPHURT/D
ELECTRICITY400-600 MW
44--Kirkuk RefineryKirkuk Refinery Capacity 150 000 BPSDCapacity 150 000 BPSD
SITE INFORMATION :
Kirkuk Refinery is located about )300( KM North Of Baghdad.
Area :) 2 X 3( Km2 Coordinate U.T.M : .
N : 3937794E : 431192
PROCESS UNITS
1- Atmospheric Distillation Unit (150.000 BPSD)
2-Vacuum Distillation Unit (60,000 BPSD)
3- Naphtha Hydro-Treating Unit (42,900 BPSD)
4- Reforming Unit (CCR) (29,600 BPSD)
5-C5/C6 Isomerisation Unit (13,200 BPSD)
6-Saturated LPG Treatment Unit (5,000 BPSD)
7-Kerosene Hydro-Treating Unit (15,700 BPSD)
8-Gas Oil Hydro-Treating Unit (35,900 BPSD)
9-VGO Hydro-Cracking Unit (MHC) (36,300 BPSD)
11-Unsaturated LPG Treatment Unit (9,100 BPSD)
12-C3/C4 Alkylation Unit (9,100 BPSD)
14-Hydrogen Production Unit (50,000 M3/Hr )
15-Sulphur Recovery Unit (292 TPSD)
16- Blown Asphalt Unit (490 TPSD)
13-N C4 Isomerisation Unit (3,100 BPSD)
10-Fluid Catalytic Cracking (FCC) (23,900 BPSD)
PRODUCTSPRODUCTS
LPGLPG
GASOLINE Unleaded ( Premium, Regular & Super)GASOLINE Unleaded ( Premium, Regular & Super)
KEROSENE &ATKKEROSENE &ATK
GAS OIL (DIESEL)GAS OIL (DIESEL)
HEAVY GAS OIL (HEAVY DIESEL)HEAVY GAS OIL (HEAVY DIESEL)
ASPHALT (Paving & Many Types of Industrial Blown Asphalt)ASPHALT (Paving & Many Types of Industrial Blown Asphalt)
SULPHURSULPHUR
FUEL OIL ( less than 15% vol . of crude)FUEL OIL ( less than 15% vol . of crude)
ELECTRICAL POWER 400 MWELECTRICAL POWER 400 MW
Products Specification will be according to EURO-4 as minimum required.Gasoline , Kerosene &Gas oil with (10 ppm ) Sulphur content .
Expected Product Quantities :
PRODUCTSTh.M3 /SD
LPG225 T/SD
GASOLINE10.250
KEROSENE /ATK3.450
DIESEL6.150
HEAVY DIESEL0.8
FUEL OIL0.265
ASPHALT490 T/SD
SULPHUR292 T/SD
ELECTRICITY400 MW
-Rehabilitation of the second train in Khor al Zubair –
South gas – under way.
-Rehabilitation of Sour gas treatment units at NGL
North Rumailah – under way.
-Studies for New slug catchers at khor al Zubair & NGL&
Sulphur recovery unit at North Rumailah –
under way.
Future Plans -Third Train in North Gas – Studies & Evaluation.
-Expansion of existing compressor stations for Rumailah,Zubair&West Qurna Fields to match future production levels from these fields.
-Expansion of NGL capacity of South Gas from present 1050 mmscf/d to 2500 mmscf/d.
-Implementing Sour Gas treatment & Sulphur recovery Units at Khor al Zubair.
-Building Power generation at Khor al Zubair.
-Rehabilitation of LPG & Ng Export Terminal at Khor al Zubair.
Present Installed Refining Capacity1 -Salah al Din Complex – Baiji – 310 mb1/d
2 -Doura Refinery – Baghdad – 210 mb1/d
3 -Basrah Refinery – Basrah -140 mb1/d +
70mb1/d under construction
4 - -6 small refineries , 30mb1/d – 180 mb1/d
Kirkuk,Syniah-Baiji , Najaf,Samawa,Nasiriyah,Maisan
- 1 small refinery at Diwaniyah – 20 mb1/d
- 1 = = = Kasak –Neinewah – 10 mb1/d
- 1 = = = Haditha – Anbar – 16 mb1/d
Total- 886 mb1/d
+70 mba under construction
Operating Capacity
The average operating capacity is in the 580 – 620 mb1/d.
The short fall in refining capacity is due to
- Shortage in delivery of crude oil
- Frequent stoppages due to operational
problems
- Accumulation of fuel oil or Naphtha in small refineries .
Main Projects in Existing Refineries -3 Ismerisation Units at Baiji , Doura &
Basrah – under construction.-2 Gasoline Reformers at Doura & Basrah- Procurement &
Construction Phases. -Fcc unit at Basrah –FEED phase.
-Fcc unit at Doura–FEED phase. -Fcc unit at Baiji – Feasibility Completed.
-2Gas Oil Desulphurisation Units at Basrah & Doura- Bidding Stage .
-3 small Gasoline Reformer units at Najaf ,Samawa& Nasiriyah- Engineering phase.
-Power Generation Units at Doura & Baiji – under construction
Nassiryah Refinery Process UnitsDesign Capacity & Licensors
Unit nameLicensor
Saturated LPG Treater Units UOP
Naphtha Complex
Naphtha Hydrotreating Units UOP
Light Naphtha Isomerisation Units UOP
Continuous Catalytic Reforming Units UOP
Total for Naphtha Complex
FCC Complex
Vacuum Gas oil HydrotreatingUOP
Fluidised Catalytice Cracking Unit UOP
Unsaturated Gas Plant UOP
FCC Unsaturated LPG Treating Unit UOP
Nassiryah Refinery Process UnitsDesign Capacity & Licensors
Unit nameLicensor
FCC ComplexUOP
Full Range Catalytic Naphtha Treating Unit UOP
Heavy Catalytic Naphtha Hydrodesulphurisation Unit UOP
Total for FCC Complex
C4 Isomerisation Unit Axens
H2so4 Alkylation Unit DuPont)Stratco(
Sulphuric Acid Regeneration Unit DuPont)Stratco(
Total
Hydrocracker Unit CLG
Nassiryah Refinery Process UnitsDesign Capacity & Licensors
Unit nameLicensor
Hydrogen Production Units Tecnimont KT
Sulphur Recovery & Tail Gas Treating Units Tecnimont KT
Bitumen Blowing Unit Poerner
Kerosene Hydrotreater Units Axens
Gaoil Hydrotreater Units Axens
Total
Residue Hydrocracker Units Axens
Flue Gas Desulphurisation Unit SGS
Total
Karbala Refinery Process UnitsDesign Capacity & Licensors
Unit nameLicensor
Crude and Vacuum Distillation Basic Design by Technip
Naphtha Hydrotreating UOP
Isomerization UOP
Catalytic Reforming UOP
Kerosene Hydrodesulfurization Axens
Diesel Hydrodesulfurization Axens
VGO Hydrotreating UOP
Fluid Catalytic Cracking UOP
Poly Naphtha Axens
Asphalt Blowing Poerner
LPG Production Basic Design by Technip
Hydrogen Production Unit – Train 1 & 2 Haldor Topsoe
Gas Sweetening and Amine Regeneration Basic Design by Technip
Sour Water Stripper Basic Design by Technip
Sulphur Recovery – Train 1 & 2 KTI
Tail Gas TreatmentKTI
Missan Refinery Process UnitsDesign Capacity & Licensors
Unit nameLicensor
Fluid Catalytic Cracking –Unit 190 KBR USA LLC
Vacuum Residue Solvent De- asphalting ))ROSE(( –Unit 190 KBR USA LLC
Blown Asphalt –Unit 250 POERNER NGENIEUEGESLLSCHAFT MBH
Naphtha Hydrodesulphurization –Unit 120 AXENS
Continuous Catalytic Reformer –Unit 130 AXENS
Vacuum Gas Oil Hydro cracker–Unit 180 AXENS
De-Asphalted Oil Hydrdesulphurisation –Unit 240 AXENS
C5 & C6 Isomerisation Process –Unit 140 UOP Limited
C4 Isomerisation Process –Unit 270 UOP Limited
Saturated LPG Treatment ))SULFREX(( –Unit 155 AXENS
Unsaturated LPG Treatment ))SULFREX(( –Unit 210 AXENS
Kerosene Hydrodesulphurisation –Unit 160 HALDOR TOPSOE A/S
Light Gas Oil Hydrodesulphurisation –Unit 170 HALDOR TOPSOE A/S
Missan Refinery Process UnitsDesign Capacity & Licensors
Unit nameLicensor
Hydrogen Production –Unit 280 HALDOR TOPSOE A/S
C 3/ C4 Alkylation –Unit 260E.I du Pont Nemours and Company