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New Refineries

Grass Roots Refineries Projects

Persian Gulf Star Condensate Refinery

Objectives

·       Processing 360,000 bpd of South Pars gas condensate

·       Producing clean fuels according to Euro5 quality standards

·       Creating added value for South Pars gas condensate

Location

25 km west of Bandar Abbas

Shareholders

NIORDC (17.9%), TaminPetroleum and Petrochemical Investment Corporation (TAPPICO) (49%), Iran Oil Pension Fund Investment Company (OPIC)(33.1%)

Contract Date

May 2007

Capacity

360,000 bpd

Feedstock

South Pars gas condensate

Products and Production Rate

·       Gasoline: 36,500 m3/d (Euro5)

·       Jet fuel: : 3,300 m3/d

·       Gas oil: 13,350 m3/d (Euro5)

·       LPG: 4,500 m3/d

Process Units and Numbers

·       Distillation: 3

·       Continuous Catalytic Reforming: 3

·       Isomerization: 3

·       Gas oil hydrotreater: 2

·       Kerosene hydrotreater: 1

Investment

€ 3,800 million

Estimated Production Date

2017

Physical Progress(July2016)

89.14 %

 

 

Project Achievements

Product

Production Increase/Decrease (million lit/d)

Standard

Gasoline

36.5

Euro-V

Kerosene/ Jet Fuel

3.3

International standards

Gas Oil

13.4

Euro-V

LPG

4.5

NIORDC Standards


 Process Units

 

Unit

No.

Capacity (bpd)

Distillation

3

120,000

LPG merox

2

13,000

LPG recovery

2

15,000

Naphtha hydrotreater (NHT)

3

78,000

Continuous catalytic reforming (CCR)

3

45,000


Isomerization (ISOM)

3

30,000

Kerosene hydrotreater (KHT)

1

25,000

Gas oil hydrotreater (GOHT)

2

42,000

Sulfur recovery

2

85 (tpd)

Sour water stripper (SWS)

2

46.2 (m3/h)

Amine treating (ATU)

2

180 (m3/h)

 

 

Goureh-Jask Crude Oil Pipeline Project

Objectives

·       Supply crude oil for Jask oil terminal

Capacity

1,000,000 bpd

Implemented by

National Iranian Oil Engineering and Construction Company (NIOEC)

Investment

1250 mm$

 

Jask Oil Storage Terminal Project

Objectives

·       Safeguarding the economy of crude export

·       Helping national and consumers security

·       Offering customers maximum flexibility

Capacity

20,000,000 barrels of crude oil

Investment Method

Private sectorand NIOC will sign lease agreement to store crude oil

 

 

Anahita Refinery

Objectives

  • Supplying oil products for western part of Iran and export reminder products to neighbor countries, according to latest clean fuels standards.
  • Technologic  development of Kermanshah  province
  • Providing new opportunities for petrochemical industry establishment in the region and drivingprivateSector investment in this Field.

Description

  • Production of oil products (LPG, Gasoline, Kerosene, Jet fuel, Gas oil) according to latest clean fuel specification, through updated refining …..Technology and heavy oil upgrading.

 

Products

Type

Production Rate (tpd)

LPG

347

Regular gasoline (RON 90)

3,895

Premium gasoline (RON 95)

982

Kerosene

4,124

Gas oil

7,171

Fuel oil

2,484 (upgraded Feed)*

Bitumen

840

Sulfur

288

Capacity: 150,000 bpd

*Upgraded Feed should be added to the production rate.

 

Units

Unit

Capacity (bpd)

Licensor

Atmospheric distillation (CDU)

150,000

-

Vacuum distillation (VDU)

68,000

-

Naphtha hydrotreating (NHT)

39,000

UOP

Mid distillate hydrotreating (MDHT)

45,000

Topsoe

Isomerization (PENEX)

16,000

UOP

Hydrocracking (HCU)

35,000

UOP

Continuous catalytic regenerator (CCR)

25,000

UOP

LPG recovery and treating

1,000

RIPI

Upgarded feed

25,000

KBC - Nargan

Sulfur recovery (SRU)

380 (tpd)

Technip-KTI

Hydrogen production (HPU)

220 (tpd)

Topsoe


BahmanGeno Refinery (Hormoz)

Objectives

·       Processing 300,000 bpd of Iranian heavy and extra heavy crude oil

·       Maximizing the production of gas oil and jet fuel

·       Minimizing the production of heavy products

·       Production of petroleum products according to Euro-V emission standards

·       Observing the environmental obligations

Implemented by

BahmanGeno Refining Company

Location

Jask free economic zone

Total Investment

$ 7,470 million

Construction Duration

42 months

First Phase Investment

$ 2,193 million

Construction Duration

36 months

Licensors for Basic Design

Sinopec:Coker

Linde:H2 Plant

KBC : CDU, VDU, LPG

Axens: NHT, CCR, ISOM, HCR, MHC , GHT, FCC, DHDT

UOP : KeroseneNerox , Alkyl

Technip: SWS, Amine ,SRU ,TGT









 

First Phase Products

Type

Capacity

LPG

153 (tpd)

Gasoline

49,500 (bpd)

Fuel oil

162,500 (bpd)

Gas oil

69,985 (bpd)

Bitumen

2,466 (tpd)

Capacity: 300,000 bpd of heavy and extra heavy export crudes of Soroush, Norouz fields and heavy crudes of Forouzan field

 

Products

Type

Capacity

LPG

2,400 (tpd)

Gasoline

94,350 (bpd)

Propylene

200 (tpd)

Jet fuel

18,870 (bpd)

Gas oil

144,670 (bpd)

Sulfur

850 (tpd)

Coke

5,800 (tpd)

Shareholders: Tadbir (80%), NIORDC (20%)

Executive Summary of Refinery Projects

Refinery Name

Estimated Investment (billion)

Currency

Physical Progress (%)

Status

Anahita

3.1

-

Basic design

BahmanGeno

7.47

$

-

Basic design

 

Status of Main Licenses, Studies and Basic Measures Taken


Activity

Anahita Refinery

BahmanGeno Refinery

Obtaining NIORDC approval

Obtaining MOP licensor workgroup

Preliminary feasibility studies

Detailed feasibility studies

Joint company registration

Topography and survey studies

-

Basic design and licensor

Environmental studies

Geotechnical studies

-

Land acquisition for pipeline

-

-

Land acquisition for refinery

-

Excavation

-

-

Ground clearance and mine sweeping

-

-

Attracting finance

-

-