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| New Refinery Projects |
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Khuzestan Extra Heavy Crude Oil Refinery
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Project
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Khoozestan extra heavy crude oil new refinery installation
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Objectives
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Maximizing gas oil production
Applying HRH new process for the first time to refine extra heavy crude oil
Utilizing the extra heavy crude oil from Azadegan and Yadavaran fields
Qualifying of oil products to meet 2005 Europe Standards
Energy, wastes and polluters management in production process
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Location
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Abadan
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Implemented by
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NIOEC
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Project Director
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Mr. Mohammad Zali
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Contract date
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production date
|
2012
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Capacity (production)
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180,000 bpd
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Products
|
See Table 1
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Feedstock
|
Blend of oil from Azadegan, Yadavaran and Jofeir fields in different ratio
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Units
|
See Table 2
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Investment
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€ 2.9 billion
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Contractors
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EIED, GSA , Topsoe
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License
|
Topsoe (GHDS,HCR,H2 Units)
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Project status
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Basic Design: 25%
Overall Progress: 1.02%
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Contact Details
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Tel: +98-21-88 91 24 63
Fax:+98-21-66 15 36 91
Website: www.nioec.org
Email: nioecpr@nioec.org
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Table 1- Products of Khoozestan extra heavy crude oil refinery
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Products
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Future capacity (bpsd)
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Percentage
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LPG
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11,766
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6.5
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Gasoline
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59,208
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32.9
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Kerosene
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48,915
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27.2
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Gas Oil
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75,078
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41.7
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Fuel Oil
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3,030
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1.7
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Sulfur (ton/d)
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410
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Table 2- Units of Khoozestan extra heavy crude oil refinery
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Units
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Capacity (bpsd)
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Atmospheric Distillation Unit
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165,000
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Vacuum Distillation Unit
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14,500
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LPG Treating and Recovery Unit
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12,500
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Naphtha Hydrotreater Unit
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84,000
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CCR Unit
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44,500
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Kerosene Hydrotreater Unit
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55,000
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Isomerization Unit
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23,500
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Hydro Cracker Unit
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5,700
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H2 (m3/d)
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9,500
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Amine Gas Treating Unit (ton/d)
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1,189
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Soar Water Stripper Unit (ton/d)
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410
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HRH Unit
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18,000
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Water, Power, Steam, Sewage and N2 Utilities
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|
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Storage Tanks
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Back to Top
Hormoz Extra Heavy Crude Oil Refinery Project
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Project
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Extra heavy crude oil refinery installation in Bandar Abbas
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Objectives
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Refining of heavy and extra heavy export crude oil up to 300,000 bpd
Increase of gasoline production
Qualifying of oil products to meet 2009 Europe Standards (Euro-V)
Observing the environmental standards
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Location
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West of Bandar Abbas existing refinery
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Implemented by
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Hormoz Refining Co.
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Project Director
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Mr. Mohammad Hosein Ardashiri
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Contract Date
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March 26th 2008
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Effective Date
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June 15th 2008
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Completion date
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Winter 2012 (anticipated)
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Capacity
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300,000 bpd
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Products
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See Table 1
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Feedstock
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See Table 2
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Units
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See Table 3
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Contractors
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A Consortium of Sazeh , PIDEC, SEI (Basic Design and EPC of Unlicense Process Units)
A Consortium of Dextron,EIED, ODCC,OIED (Basic Design and EPC of Water,Power,Steam Units)
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Consultants
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KBC (England) for Refining pattern investigations, feasibility study and basic design for LPG, VDU and CDU units
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License
|
H2 Plant basic design: Linde (Germany)
Sinopec
Axens(France)(HT,CCR,ISOM,DHDT,HCR,MHC,FCC)
KBC (CDU,VDU,SGP)
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Investment
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€ 4.3 billion
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Related projects
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Environmental investigations: Amayeshgaran Pouyaye Mohit co.
Earth work: Sarig Bandar co.
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Project status
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Licensor contract: concluded
EPC suggestions under estimation
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Construction work
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Earth work: 488,950 m3
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Contact Details
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Tel: +98-21-88 905234-7
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Table 1 – Products of Hormoz Refinery
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Products
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Capacity
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LPG (bpd)
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2,400(bpd)
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Propylene
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211 ton/d
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Gasoline
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98,660 (bpd)
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Jet Fuel
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19,651 (bpd)
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Diesel
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147,243 (bpd)
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Sulfur
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840 (ton/d)
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Coke
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5,792 (ton/d)
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Table 2 – Feedstock of Hormoz Refinery
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Feedstock
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Capacity (bpd)
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Blend of crude oil from Soroush, Norouz and South Pars oil fields
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200,000
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Iran Heavy export crude oil
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70,000
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Forouzan Heavy crude oil
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30,000
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Table 3 – Units of Hormoz Refinery
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Unit
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Capability(bpd)
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Atmospheric Distillation Unit
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300,000
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Vacum Distillation Unit
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100,000 each
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Delayed Coking Unit (DCU)
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100,000
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LPG Recovery
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Naphtha Treating Unit (with naphtha splitter)
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90,000
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Catalytic Reforming Unit
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58,000
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Isomerization Unit (with DIP and DIH)
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35,000
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Kerosene Merox Unit
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45,000
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Gas Oil HTU with Aromatic Saturation Unit(ASU)
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126,000
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FluidCatalytic Cracking (FCC)
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51,000
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Unsaturated Gas Plant
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7,000
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Propyiene Unit
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9,000
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HF Alkylation
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9,500
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Mild Hydrocracker (MHCK)
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70,000
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Hydrocracker (HCK)
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40,000
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H2 Plant
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155,000 each
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Sulfure Recovery
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475 ton/d each
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Amine Treating Unit
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8,400 m3/d
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Back to Top
Caspian Refinery Project
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Project
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Caspian Refinery implementation
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Objectives
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Implementation of a Refinery in north of the country with Employing Advanced Refining Technologies,Utilization all readily available feed stock,Growing presence in regional markets , Attraction the participation of local and foreign private sectors in refining projects
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Location
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Golestan Province
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Project Director
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Mr.Ali Hadjirasouliha
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Production Year
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2013
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Capacity
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300,000 bpd
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Products
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Gasoline, gas oil, LPG, kerosene, sulfur, bitumen, propylene
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Feedstock
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Crude oil from Caspian Sea Region Countries
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Products
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Table 1
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Investment
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$ 4 billin
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Project Status
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Site selection report is already prepared.
1000 hc land is purchased for the refinery’s site.
Geotechnical investigation is performed.
Environmental , social and health impact assessment is prepared.
A pre-feasibility study has been prepared.
Bankable feasibility study is being done by KBC.
Discussion for partnership of Russian and Kazakh companies is continuing.
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Contact Details
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Tel: +98-21-88930560-4
Fax: +98-21-88930569
Website: www.nioec.org
Email: nioecpr@nioec.org
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Table 1- Products of Caspian Refinery
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Products
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Capacity ( bpd)
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LPG
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28,000
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Propylene
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6,000
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Gasoline
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130,000
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Kerosene/Jet A-1
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30,000
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Gas Oil
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70,000
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Fuel Oil
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36,000
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Sulfur
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208 ton/day
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Back to Top
Anahita Refinery Project
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Project
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Anahita Refinery implementation with 150,000 bpd capacity in Kermanshah
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Objectives
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supplying energy needs of the region
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Location
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Kermanshah-Hamedan highway, 15th km
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production date
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2012
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Capacity
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150,000 bpd
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Products
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Gasoline, gas oil, LPG, kerosene, fuel oil, sulfur, bitumen
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Feedstock
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Blend of crude oil from North Dezful, Naftshahr, Maleh Kooh (Kerman)
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Products
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Table 1
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Units
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Distilation, LPG recovery, visbreaker, CCR, FCC, asphalt, sulfur recovery, gas oil hydrodesulfurization, naphtha hydrotreater, isomerization, H2, N2, propylene, soar water, amine gas treating, industrial swage treating
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Contractors
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Basic design: Sazeh (Iran), APS (Italy)
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Investment
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€ 1.3 billion
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Project Status
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Basic Design is in Progress, Licensors contract:in progress to sign.
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Contact Details
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Tel: +98-21-88 875955
Fax: +98-21-88 875956
Website: www.anorc.org
Email: info@anorc.ir
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Table 1- Products of Anahita Refinery
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Products
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Capacity ( bpd)
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LPG
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12,500
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Gasoline
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52,000
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Kerosene Jet Fuel (ATK)
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27,000
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Gas Oil
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35,000
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Fuel Oil
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11,000
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Shahriar Refinery Project
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Project
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Tabriz (Shahriar) New Refinery Installation
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Objectives
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New refinery installation (capacity 150,000 bpd) in cooperation with the existing refinery for products quality improvement
Refining pattern determination regarding to the crude oil mixture from North Dezful and Maroon fields in Iran and Kashagan field in Kazakhstan
Applying the proper pattern for maximum gasoline production
Qualifying of oil products to meet 2009 Europe Standards (Euro-V)
Observing the maximum environmental standards regarding to the geographical position of the project
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Location
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Tabriz
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Implemented by
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NIOEC
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Project Director
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Mr. Seyed Hasan Ghasemzadeh
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Contract date
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Sep 25th 2007 (basic design and licensor)
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Effective date
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Nov 16th 2007 (basic design and licensor)
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production date
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March 2012 (anticipated)
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Capacity (production)
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150,000 bpd
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Products
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See Table 1
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Feedstock
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Crude oil from North Dezful and Maroon fields in Iran and Kashagan field in Kazakhstan
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Units
|
See Table 2
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Consultants
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Basic design: Nargan (Iran) and KBC (UK)
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License
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Axens (France), Technip-KTI (Italy),.Topsoe (Denmark), RIPI (Iran)
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Investment
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€ 1.2 billion
|
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Project status
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Basic design: 43.8%
Overall Progress: 2.35%
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Contact Details
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Tel: 021-88 96 58 64
Fax:021-88 95 53 34
Website: www.nioec.org
Email: ghasemzadeh@nioec.org
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Table 1- Products of Shahriar refinery
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Product
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Existing (Future)
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Shariar
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Total
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LPG
|
2,274
|
8,545
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10,819
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Propylene
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0
|
2,364
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2,364
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Naphtha to TPC
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7,700
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0
|
7,700
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Gasoline
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12,714
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72,238
|
84,952
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Kerosene
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22,400
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0
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22,400
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Gas Oil
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10,980
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78,832
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89,812
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Fuel Oil
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20,660
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11,133
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31,793
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| Coke |
|
322 |
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| Sulfur |
|
198 |
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Asphalt
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5,000
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5,000
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10,000
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Table 1- Units of Shahriar refinery
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Units
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Capacity (bpd)
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Atmospheric Distillation Unit
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150,000
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Vacuum Distillation Unit
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55,000
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LPG Treating Unit
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3,500
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LPG Recovery Unit
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3,500
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Propylene Recovery Unit
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3,000
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Whole Naphtha Hydrotreater Unit
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34,000
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CCR Reforming Unit
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20,000
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Gas Oil Hydrotreater Unit
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80,000
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FCCU Feedstock Hydrotreating Unit (VGO-HT)
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40,000
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Fluid Catalytic Cracking Unit (FCCU)
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35,000
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Back to Top
Pars Refinery Project
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Project
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Shiraz (Pars) new refinery installation
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Objectives
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Increasing the refining capacity of the country
Increasing production of gasoline and gas oil
Foreign investment attraction and establishing economical added value
Qualifying of oil products to meet 2009 Europe Standards (Euro-V)
Energy management and reducing fuel consumption and wastes
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Location
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Shiraz
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Implemented by
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NIOEC
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Project Director
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Mr. Hamid Sharifrazi
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Contract Date
|
May 2007
|
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production date
|
2012
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Capacity (production)
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120,000 bpd
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Products
|
See Table1
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Feedstock
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South Pars field gas condensates
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Units
|
See Table 2
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Consultants
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Basic design: PIDEC (Iran)
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License
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Axens (France), KTI (Italy),.Topsoe (Denmark), UOP (England), RIPI
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Investment
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€ 800 million
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Related projects
|
16” pipeline installation from Assaluyeh to Shiraz
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Project status
|
Basic Design :19%
Overall Progress: 2.9%
|
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Contact Details
|
Website: www.nioec.org
Email: nioecpr@nioec.org
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Table 1- Products of Pars refinery
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Products
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Capacity (bpd)
|
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LPG
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10,000
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Kerosene
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16,000
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Gasoline
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75,000
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Gas Oil
|
42,000
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Fuel Oil
|
4,000
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Sulfur
|
56 (tons per day)
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Table 2- Units of Pars refinery
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Units
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Capacity (bpd)
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Distillation Unit
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120,000
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Naphtha Hydrotreater Unit
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78,000
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Isomerization Unit
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30,000
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Kerosene Hydrotreater Unit
|
16,000
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Gas Oil Hydrotreater Unit
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42,000
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Heavy Naphtha Catalytic Cracking Unit (CCR)
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45,000
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H2 Unit
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30
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Sulfur Recovery Unit
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62 (tons per day)
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Amine Hydrotreating Unit
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6,700
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LPG Treating and Recovery Unit
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8,500
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Back to Top
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