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| Refinery Expansion Projects |
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Shazand Arak
|
Project
|
Shazand Refinery expansion
|
|
Objectives
|
Refining capacity increment from 169,100 bpd to 250,100 bpd
Increasing Gasoline production
Changing feedstock composition, from 100% Ahwaz crude to a blend of 55% Ahwaz crude + 45% heavy crude from other fields
Quality improvement of oil products to meet Euro-V Standards
Observing environmental standards
|
|
Location
|
Arak, Shazand Refinery
|
|
Implemented by
|
NIOEC
|
|
Project Director
|
Mr. Rashid Seyedian
|
|
Contract date
|
July 29th 2006
|
|
Effective date
|
Sep 15th 2006
|
|
production date
|
June 14th 2010
|
|
Capacity (before and after expansion)
|
From 169,100 bpd to 250,000 bpd
|
|
Products
|
See Table 1
|
|
Feedstock
|
blend of 55% Ahwaz crude + 45% heavy crude from other fields
|
|
Units
|
See Table 2
|
|
Contractors
|
A consortium of Sazeh, ODCC from Iran and SEI from China
|
|
Consultants
|
Basic design: JGC from Japan
|
|
Project management
|
MAPSA and Enerchimi from Iran
|
|
License
|
RIPI (Iran), KTI (Italy), Technip (Italy), UOP (England), Axens (France)
|
|
Investment
|
€ 2.7 billion
|
|
Related Projects
|
Environmental Studies : Arzyaban Mohit
|
|
Project status
|
Detailed engineering: 78.33%
Procurement: 31.03%
Construction: 6.36%
Overall progress: 24.24%
|
|
Construction work
|
Earth work: 1,800,000 m3
|
|
Concrete work: 210,000 m3
|
|
Weight of equipment: 130,000 ton
|
|
Piping: 933 km
|
|
Cable work: 1,175 km
|
|
Contact Details
|
Tel: 021-88 80 26 47
Fax:021-88 90 17 33
Website: www.nioec.org
Email: R.seyedian@nioec.org
|
Table 1- Arak Shazand Refinery expansion project
|
Products
|
Existing capacity
(million liter)
|
Capacity after the expansion
(million liter)
|
Products increment after the expansion
(million liter)
|
|
LPG
|
.97
|
3.57
|
2.6
|
|
Propylene
|
0
|
1.23
|
1.23
|
|
Premium Gasoline
|
0.93
|
3.55
|
2.62
|
|
Gasoline
|
3.74
|
12.31
|
8.57
|
|
Kerosene (Jet Fuel)
|
4.18
|
5.95
|
1.77
|
|
Gas Oil
|
7.47
|
8.92
|
1.45
|
Table 2 –Arak Shazand Refinery expansion project
|
Unit
|
Licensor
|
Capacity (bpd)
|
|
ATM. Crude Distillation Unit
|
JGC (Japan)
|
80,000
|
|
No.2 Naphtha Hydrotreater Unit
|
Axens (France)
|
33,000
|
|
Octanizer Unit
|
Axens (France)
|
20,000
|
|
Isomerization Unit
|
RIPI (Iran)
|
8,500
|
|
Kerosene Hydrotreater Unit
|
Axens (France)
|
31,500
|
|
Gas Oil Hydrotreater Unit
|
Axens (France)
|
53,000
|
|
Reduced Crude Desulfurization Unit
|
UOP (England)
|
69,180
|
|
Residue Fluid Catalytic Cracking Unit
|
UOP (England)
|
94,387
|
|
RFCC LPG Merox Unit
|
UOP (England)
|
28,105
|
|
Propylene Recovery Unit
|
UOP (England)
|
28,105
|
|
Cracked Gasoline Hydrotreating Unit
|
Axens (France)
|
50,500
|
*It should be mentioned that RCD and RFCC units would be installed and operated for the first time in Iran and in the Middle East.
Back to Up
Gasoline Production Increase Project in Bandar Abbas Refinery
|
Project
|
Gasoline production increase of Bandar Abbas Refinery
|
|
Objectives
|
New units such as gas oil hydrotreater, light and heavy naphtha hydrotreater, catalyst regeneration, isomerization, isomerization, sour water, amine, sulfur recovery (SRU), storage tanks, facility services and other related facilities will be installed in Bandar Abbas refinery in order to gasoline production increase up to 4.8 million liters/d besides the existing capacity and also the quality improvement of gas oil.
|
|
Location
|
Bandar Abbas Refinery
|
|
Implemented by
|
NIOEC, Mr. Seyed Ghasem Hoseini
|
|
Contract date
|
Nov 18th 2006
|
|
Effective date
|
March 15th 2007
|
|
Exploitation date (production date)
|
In the midst of 2010
|
|
Capacity (production)
|
Gasoline production increase up to 4.8 million liters/d 120,000 bpd
|
|
Products
|
See Table 1
|
|
Feedstock
|
Heavy crude from Khark Island and gas condensates
|
|
Units
|
See Table 2
|
|
Contractors
|
Main contractor: PIDEC for EPC contract
Sub contractors: Abb Lummus and PIECC (Iran)
|
|
Consultants
|
Basic design: Axens (France), Prosernat (France)
|
|
License
|
Axens (France), Prosernat (France)
|
|
Amount of investment
|
€ 400 million
|
|
Geotechnical investigations
|
Zamiran Company
|
|
Project status
|
Basic design :98.24%
Detailed Engineering : 20.78%
Procurement : 10.94%
Construction : 7.5%
Overall Progress : 14.18%
|
|
Construction work
|
Earth work: 200,000 m3
|
|
Concrete work: 60,000 m3
|
|
Weight of equipment: 27,500 ton
|
|
Piping: 800,000 inch/diameter (preliminary estimations)
|
|
Cable and instrument work: 880 km
|
|
Contact Details
|
Tel: +98-21-66 15 32 95
Fax:+98-21-88 90 40 35
Website: www.nioec.org
Email: nioecpr@nioec.org
|
Table 1- Gasoline production increase project in Bandar Abbas Refinery
|
Product
|
Existing Production (bpsd)
|
Percentage
|
Future Production (bpsd)
|
Percentage
|
|
LPG
|
7,100
|
3
|
10,700
|
3.5
|
|
Gasoline
|
46,100
|
20
|
82,400
|
27
|
|
Kerosene and Jet Fuel
|
36,200
|
16
|
33,500
|
11
|
|
Gas Oil
|
69,500
|
30
|
74,700
|
24.5
|
|
Fuel Oil
|
66,900
|
29
|
103,300
|
34
|
|
Sulfur (ton in working days)
|
124
|
|
234
|
|
Table 2- Gasoline production increase project in Bandar Abbas
|
Units
|
Unit No.
|
Train No.
|
Volume
|
Volume Unit
|
Licenser
|
|
Two New Naphtha Splitter in Existing Distillation Units
|
01 & 71
|
|
38,550
|
Bpd
|
Axens
|
|
Heavy Naphtha Hydrotreater Unit
|
72
|
2
|
25,000
|
Bpd
|
Axens
|
|
Continuous Catalyst Regeneration Unit
|
700
|
Kg/Hr
|
Axens
|
|
Octanizer Unit
|
25,000
|
Bpd
|
Axens
|
|
Light Naphtha Hydrotreater Unit
|
18
|
1
|
16,000
|
Bpd
|
Axens
|
|
Light Naphtha Isomerization Unit
|
16,000
|
Bpd
|
Axens
|
|
Gas Oil (Diesel) Hydrodesulfurization Unit
|
74
|
1
|
50,000
|
Bpd
|
Axens
|
|
Sulfur Recovery Unit
|
79
|
2
|
120
|
Ton/d
|
Prosernat
|
|
Amine Gas Treating Unit
|
58
|
3
|
230
|
Ton/d
|
Non licensed (by Prosernat)
|
|
Sour Water Stripping Unit
|
88
|
3
|
500
|
Ton/d
|
Non licensed (by Prosernat)
|
|
Sulfur Solidification Unit
|
59
|
1
|
250
|
Ton/d
|
PIDEC
|
|
15 Storage Tanks
|
|
|
2,830,000 (total capacity)
|
BBL
|
PIDEC
|
Back to Up
Process Optimization and Product Quality Improvement of Tehran Refinery
|
Project
|
process optimization and products quality improvement of Tehran Refinery
|
|
Objectives
|
Decreasing sulfur in Gas Oil and Kerosene according to EURO 2009 standards (EURO-V) up to 10 PPM
|
|
Location
|
Tehran Refinery utility site
|
|
Implemented by
|
NIOEC, Mr. Tofigh Azarmgin
|
|
Contract date
|
August 5th 2007
|
|
Effective date
|
October 16th 2008
|
|
Completion date
|
June 16th 2010
|
|
Capacity (before and after expansion)
|
No changes in existing capacity ( 250000 bpd )
|
|
Products
|
See Table 1
|
|
Feedstock
|
See Table 2
|
|
Units
|
See Table 3
|
|
Contractors
|
Ehsan Consortium : Design & Construction Co.
General Iranian Contractor,design and inspect
|
|
Consultants
|
-
|
|
License
|
TPKTI , Technip , Axens , Intertek
|
|
Amount of investment
|
-
|
|
Related projects
|
-
|
|
Project status
|
Detailed engineering(21.7%) , Procurement(9.3%),Construction (3.5%)
Overall Progress: 10.98%
|
|
Construction work
|
Earth work: 38,000 m3
|
|
Concrete work: 25,000 m3
|
|
Piping : 265,000 Inch / diameter (underground and overground )
|
|
Weight of equipment: 9,465 ton
|
|
Cable work: 10,000 m
|
|
Contact Details
|
Tel: +98-21-66 15 26 83
+98-21-88 87 00 17-20
Fax: +98-21-88 87 00
+98-21-88 90 70 63
Website: www.nioec.org
Email: AZARMGIN@nioec.org
|
Table 1:
Product Status of Tehran Refinery
|
Product
|
Current (BPSD )
|
|
Gasoline
|
45,000
|
|
Kerosene
|
41,500
|
|
Fuel Oil
|
50,100
|
|
Gas Oil
|
60,600
|
|
Sulphur (Ton per day )
|
35
|
Table 2- Crude Sources of Tehran Refinery
|
Crude Oil
|
Volume ( BPD )
|
Volumetric percentage
|
|
Maroon
|
80,300
|
23.46
|
|
Abtisoor
|
7,000
|
192
|
|
Ahvaz Bangestan
|
4,500
|
1.87
|
|
Ahvaz Asmari
|
4,500
|
16.04
|
|
North Dezfool
|
70,300
|
33.04
|
|
Middle East
|
30,400
|
12.67
|
|
Total
|
240,000
|
100.00
|
Table 3 - New Units of Tehran Refinery
|
New Units
|
Capacity
|
|
Kerosene Desulphurization Unit ( KHT )
|
31,500 ( BPSD )
|
|
Gas Oil Desulphurization Unit ( GHT )
|
53,000 ( BPSD )
|
|
Hydrogen Production Unit
|
42 (MMSCF)
|
|
Sulphur Recovery Unit ( SRP )
|
110 T/hr
|
|
Electricity Production Unit ( GTC )
|
5×13 MW
|
|
Storage Tanks
|
2×120,000 BBL
|
|
3×96,000 BBL
|
Back to Up
Capacity increment of Bandar Abbas Refinery
|
Project
|
Capacity increment of Banadar Abbas Refinery
|
|
Objectives
|
debottlenecking and capacity increment from 232,000 bpd up to 320,000 bpd
Basic design , Detailed engineering, purchasing, construction and installation of some units ( detailed in a,b,c sections ) is done by NIOEC
a - Vacuum Distillation units
b – Pumps , pipelines for transferring crude oil and condensate from relevant tanks to the distillation units
c – distillation units product transferring system
|
|
Location
|
Bandar Abbas refinery
|
|
Implemented by
|
NIOEC, Mr. Ghasem Hoseini
|
|
Contract date
|
August 5th 2007
|
|
Effective date
|
October 16th 2008
|
|
Completion date
|
June 16th 2010
|
|
Capacity (before and after expansion)
|
Capacity increment of distillation units from 232,000 bpd up to 320,000 bpd
|
|
Products
|
See Table 1
|
|
Feedstock
|
See Table 2
|
|
Units
|
Distillation unit No. 01 and 71 along with Unit No. 20 ( Tnkage)
|
|
Contractors
|
Iranian public contractor and ODCC
|
|
Consultants
|
Basic design consultant : Snamproggetti
Workshop supervising consultant : Nargan co.
|
|
License
|
|
|
Amount of investment
|
€ 40 million
|
|
Related projects
|
Completion and repairmen of communication routs of Bandar Abbas refinery and lowering the undergroung waters surface
|
|
Project status
|
Detailed Engineering: 99.7%
Procurement: 100%
Construction: 98.5%
Overall EPC progress: 99.59%
|
|
Construction work
|
Earth work:
|
|
Concrete work: 40,000 m3
|
|
Piping : 112,000 inch / diameter
|
|
Weight of equipment: 1,450 ton
|
|
Cable and instrument work: 58,000 m
|
|
Contact Details
|
Tel: +98-21-66 15 32.95
Fax:+98-21-88 90 40 35
Website: www.nioec.org
Email: nioecpr@nioec.org
|
Table 1- Products ton/d (Atmospheric Distillation Unit)
|
Product
|
Existing capacity
|
After the debottlenecking
|
Difference
|
|
Unstabilized LPG
|
283.44
|
307.2
|
23.76
|
|
Light SR Naphtha
|
672.48
|
1,310.4
|
637.92
|
|
Heavy SR Naphtha
|
1,867.2
|
3,136.8
|
1,269.6
|
|
Blending Naphtha
|
774.72
|
648
|
-126.7
|
|
Kerosene
|
2,360.16
|
2,880
|
519.84
|
|
Atm. Gas Oil
|
1,942.08
|
2,640
|
697.92
|
Table 2 - Products ton/d (Vacuum Distillation Unit)
|
Product
|
Existing capacity
|
After the debottlenecking
|
Difference
|
|
Light Vacuum Gas Oil
|
1,004.4
|
744
|
-260.4
|
|
Medium Vacuum Gas Oil
|
833.8
|
624
|
-209.8
|
|
Light Lube Cut
|
901.7
|
1,416
|
514.3
|
|
Heavy Lube Cut
|
1,254.5
|
2,208
|
953.5
|
|
Vacuum slops
|
334.8
|
794.4
|
459.6
|
|
Vacuum Residue
|
3,644.9
|
5,335.2
|
1,690.3
|
Table 3 - Feedstock (bpd)
|
Type
|
Existing capacity
|
After the debottlenecking
|
Difference
|
|
Heavy Crude Oil
|
220,000
|
294,000
|
74,000
|
|
Sarkhoon Gas Condensates
|
12,000
|
10,400
|
1,600
|
|
Paznan Gas Condensates
|
-
|
15,600
|
15,600
|
|
Total
|
232,000
|
320,000
|
88,000
|
Back to Up
Process Optimization and Refining Capacity Improvement of Esfahan Refinery
|
Project
|
Process optimization and refining capacity improvement of Esfahan Refinery
|
|
Objectives
|
Reduction of heavy products like fuel oil and increase of light products like gasoline through the installation of new units
Quality improvement of main products (gasoline, kerosene and gas oil) to meet Europe oil product standards
Stabilization of optimized refining capacity of 360,000 bpd and operation flexibility increase through the installation of a new distillation units
Debottlenecking of existing units
Changing the existing pneumatic control system into advanced DCS system
Reduction or elimination of environmental polluters
|
|
Location
|
Esfahan Refinery
|
|
Implemented by
|
NIOEC, Mr. Abbas Salehinejad
|
|
Contract date
|
Aug 27th 2007
|
|
Effective date
|
Dec 24th 2007
|
|
Completion date
|
Dec 24th 2011
|
|
Capacity (before and after expansion)
|
360,000 bpd
|
|
Products
|
See Table 1
|
|
Feedstock
|
Light crude oil from Iran (Maroun)
|
|
Units
|
See Table 2
|
|
Contractors
|
Technip (Italy)
Mapna (Iran), Uhde (Germany), Lorgee (Italy), Dilem (Korea), Nargan, Chegalesh and Namvaran companies participation
|
|
Consultants
|
Snamproggetti
|
|
License
|
Axens (France), UOP (England), Topsoe (Denmark), Technip-KTI (Italy), Linde (Germany)
|
|
Amount of investment
|
€ 2.5 billion
|
|
Related projects
|
|
|
Project status
|
Basic design and detailed engineering licensor receiving: completed
Detailed Engineering: 5.85%
Overal Progress: 4.36%
|
|
Construction work
|
Earth work:
|
|
Concrete work:
|
|
Piping :
|
|
Weight of equipment:
|
|
Cable and instrument work:
|
|
Contact Details
|
Tel: +98-21-88 90 50 57
Fax:+98-21-88 89 97 09
Website: www.nioec.org
Email: nioecpr@nioec.org
|
Table 1 – Product Status of Esfahan Refinery
|
|
Existing Capacity
|
Future Capacity
|
|
Products
|
Bpd
|
Percentage
|
Bpd
|
Percentage
|
|
LPG
|
17,000
|
5%
|
30,000
|
8%
|
|
Propylene
|
|
|
7,400
|
2%
|
|
Premium Gasoline
|
|
|
28,000
|
8%
|
|
Gasoline
|
41,000
|
12%
|
98,000
|
27%
|
|
Kerosene
|
61,000
|
18%
|
44,600
|
12%
|
|
Gas Oil
|
109,000
|
33
|
115,000
|
32
|
|
Fuel Oil
|
89,000
|
27%
|
19,000
|
5%
|
|
Asphalt
|
17,000
|
5%
|
17,000
|
5%
|
|
Sulfur (ton/d)
|
80
|
|
600
|
|
Table 2- New Units of Esfahan Refinery
|
Package
|
Units
|
Execution
|
Contractor
|
Effective Date
|
Duration (months)
|
|
A1
|
RHU
|
EP Mark up
|
Deilim + Namvaran
|
Dec 22, 2007
|
48
|
|
A2
|
Propylene Recovery
|
EP
|
SEI
|
Dec 22, 2007
|
|
|
C
|
Water, power and steam utilities
|
EPC
|
Mapna
|
Dec 24, 2007
|
34
|
|
D1
|
SWS + Amine Treater
|
EP Mark up
|
Chegalesh
|
|
|
|
D2
|
Gas Oil Hydrotreater, Gasoline hydrotreater, LPG treating,Sulfur Recovery, TGT
|
EP Mark up
|
Nargan
|
|
|
|
E
|
H2
|
EP Mark up
|
Nargan
|
|
|
|
B
|
Other
|
EPC
|
Implementation by the refinery
|
|
|
Back to Up
Stabilization of Current Capacity of Abadan Refinery
|
Project
|
Stabilization of current production capacity of Abadan Refinery
|
|
Objectives
|
Implementation of a new refining train with the capacity of 210,000 bpd
Maximizing the gasoline production
Qualifying of oil products to meet 2009 Europe Standards (Euro-V)
Observing the environmental standards
Supplying the feedstock for downstream (Bandar Imam Petrochemical Company, oil and asphalt plant)
|
|
Location
|
Abadan Refinery
|
|
Implemented by
|
NIOEC, Mr. Ahmad Rahimi
|
|
Contract date
|
Basic design and licensor: Sep 15th 2007
|
|
Effective date
|
Sep 15th 2007
|
|
Completion date
|
Winter 2012
|
|
Capacity (before and after expansion)
|
360,000 bpd
|
|
Products
|
See Table1
|
|
Feedstock
|
Crude oil from Ahwaz Asmari, Darkhovin, Ahwaz Bangestan, Ab Teimour, Mansoor Bangestan
|
|
Units
|
See Table 2
|
|
Contractors
|
|
|
Consultants
|
Namvaran co.
|
|
License
|
Axens (France), UOP (England), Topsoe (Denmark), Technip-KTI (Italy)
|
|
Amount of investment
|
€ 1.4 billion
|
|
Related projects
|
Installation of 11 storage tanks and collecting of worn-out storage tanks
|
|
Project status
|
Basic design and detailed engineering licensor receiving: completed
Refinery Units: Basic Design(62.4%)
Storage Tanks: Overall Progress(37.7%)
|
|
Construction work
|
Earth work:
|
|
Concrete work:
|
|
Piping :
|
|
Weight of equipment:
|
|
Cable and instrument work: m
|
|
Contact Details
|
Tel: +98-21-66 15 32 97
Fax:+98-21-88 89 15 89
Website: www.nioec.org
Email: nioecpr@nioec.org
|
Table1- Product Status of Abadan Refinery
|
Products
|
Existing Capacity (bpd)
|
Future Capacity (bpd)
|
|
Gasoline
|
54,000
|
76,600
|
|
Premium Gasoline
|
|
19,200
|
|
Gas Oil
|
105,000
|
49,790
|
|
Kersone + Jet Fuel
|
25,500
|
50,420
|
|
Fuel Oil
|
155,000
|
107,000
|
|
LPG
|
9,000
|
20,600
|
|
Sulfur (ton/d)
|
|
180
|
|
Naphtha
|
|
16,000
|
|
Petrochemical Feedstock
|
19,000
|
19,000
|
|
Lube Oil
|
2,000
|
3,000
|
Table 2 – New Units of Abadan Refinery
|
Units
|
Capacity (bpd)
|
|
CDU
|
210,000
|
|
VDU
|
103,000
|
|
HVGO
|
56,000
|
|
FCC
|
45,000
|
|
Gas Oil Hydrotreating Unit
|
90,000
|
|
Kerosene Hydrotreating Unit
|
45,000
|
|
NHT
|
65,000
|
|
ISM
|
22,000
|
|
CCR
|
43,000
|
|
HPU
|
67,000 Nm3/h
|
|
AMT
|
Hold
|
|
N2
|
Hold
|
|
LPG Treating Unit (ton/d)
|
750
|
|
Sulfur (ton/d)
|
140
|
Back to Up
Gasoline Production Increase Project in Esfahan Refinery
|
Project
|
Gasoline Production Increase
|
|
Objectives
|
Gasoline Production Increase After Implementation:25000 bpd
|
|
Location
|
Esfahan Refinery
|
|
Project Director
|
Mr. Aghanejad
|
|
Effective date
|
December 15th 2005
|
|
Exploitation Year
|
2009
|
|
New Units
|
Naphtha Hydrotreater, Catalytic Reformer,Isomerization
|
|
Contractors
|
Namvaran co. from Iran and Participation of AKPJ(India) and Dorriz co.(Iran)
|
|
Project status
|
Detailed engineering: 51.4%
Procurement: 27%
Civil:13.3%
Overall Progress: 23.20%
|
Back to Up
Gasoline Production Increase Project in Tehran Refinery
|
Project
|
Gasoline Production Increase
|
|
Objectives
|
Gasoline Production Increase After Implementation:11000 bpd
|
|
Location
|
Tehran Refinery
|
|
Project Director
|
Mr. Tathesari
|
|
Effective date
|
November 8th 2006
|
|
Exploitation Year
|
2009
|
|
New Units
|
Light Naphtha Hydrotreater, Catalytic Reformer
|
|
Contractors
|
Chegalesh co. from Iran and Participation of Petrolinvest(Bosnia) and Radira co.(Iran)
|
|
Project status
|
Overall Progress: 27.76%
|
Back to Up
Gasoline Production Plant in Abadan Refinery
|
Project
|
Gasoline Production Plant
|
|
Objectives
|
Gasoline Production Increase After Implementation:37000 bpd
|
|
Location
|
Abadan Refinery
|
|
Project Director
|
Mr. Mehraban
|
|
Effective date
|
May 13th 2006
|
|
Exploitation Year
|
2009
|
|
New Units
|
Cat Cracker, Alkylation, Isomerization, LPG Recovery, Soar Gas Hydrotreating, Sulfur Recovery,Propylene Recovery, Amine Treater
|
|
Contractors
|
PIDEC,Erection and Construction Company(ECC)(both from Iran), ABB Lummus
|
|
Project status
|
Engineering Design: 91.62%
Procurement: 57.16%
Overall Progress: 50.58%
|
Back to Up
Expansion and Optimization of Lavan Refinery
|
Project
|
Expansion and Optimization of Lavan Refinery
|
|
Objectives
|
Gasoline Production Increase After Implementation:11000 bpd
|
|
Location
|
Lavan Refinery
|
|
Project Director
|
Mr. Namvar
|
|
Effective date
|
February 27th 2007
|
|
Exploitation Year
|
2012
|
|
New Units
|
Vacuum Distillation , Kerosene and Gas Oil Treater, Isomerization , Sulfur Recovery
|
|
Contractors
|
Namvaran co. and Mehvar Sazan co. (both from Iran)
|
|
Project status
|
Overall Progress: 30%
|
Back to Up
|
|
|
|
|
|
|
|
