:: PARTEX PETRO ::

Few Words About Us

Partex Petro

Partex Petro Ltd intends to construct Condensate Refinery (Fractionation, KNHT, CRU, Product Tanks and Utilities) with capacity 10,000 Barrels per day (BPD).

Partex Refinery Ltd technical, operational and logistic strengths act as the fulcrum to leverage its refineries' asset utilization and optimization, the key components of the Refining & marketing business model. These strengths, coupled with our highly integrated plants and automated processes, augment our R&M business's operating efficiencies. Moreover, our refineries are strategically located on South of Bangladesh, offering the benefits of low transportation costs for feedstock and proximity to high-growth markets.

Our refinery at Chiitagong will be processed a wide variety of petroleum products from imported as well local condensate for supply in the Bangladesh market.

Product Application

Products	Application
Liquefied Petroleum Gas (LPG)	Domestic and industrial fuel
Diesel	Transportation and Industrial fuel
JET A-1	Aviation fuel
Motor Spirit	Transportation fuel
Premium Octane	Transportation fuel
Heavy Naphtha	Feedstock for KNHT and CRU
Light Naphtha	Feedstock for KNHT and CRU

SPECIFICATION OF PETROL

SL	TESTS	METHOD	LIMIT
1	Density at 15°C, Kg/L	ASTM D 1298	To be reported
2	Colour, visual	--	Orange
3	Reid Vapour Pressure at 38°C, psi	ASTM D 323	Max. 10
4	Copper Strip Corrosion (3 hours at 50°C)	ASTM D 130	Max. No. 1
5	Octane Number, Research method	ASTM D 2699	Min. 80
6	Lead content (as Pb), gm/L	ASTM D 2599	Max. 0.013
7	Oxidation Stability, minutes	ASTM D 525	Min. 240
8	Residue on Evaporation, mg/100ml	ASTM D 381	Max. 4
9	Sulphur_total, % mass	ASTM D 1266/ ASTM D 4294	Max. 0.1
10	Doctor Test or Sulphur_mercaptan, % mass	ASTM D 4952 ASTM D 3227/ IP 104	Negative Max. 0.001
11	Distillation: Initial Boiling Point, °C 10% vol. recovery, °C 50% vol. recovery, °C 90% vol. recovery, °C Final Boiling Point, °C Residue, % vol.	ASTM D 86	To be reported Max. 75 Min. 80 - Max. 125 Max. 180 Max. 210 Max. 2.0

SPECIFICATION OF OCTANE

SL	TESTS	METHOD	LIMIT
1	Density at 15°C, Kg/L	ASTM D 1298	To be reported
2	Colour, visual	-	Red
3	Reid Vapour Pressure at 38°C, psi	ASTM D 323	Max. 10
4	Copper Strip Corrosion (3 hours at 50°C)	ASTM D 130	Max. No. 1
5	Octane Number, Research method	ASTM D 2699	Min. 95
6	Lead content (as Pb), gm/L	ASTM D 2599	Max. 0.013
7	Oxidation Stability, minutes	ASTM D 525	Min. 240
8	Residue on Evaporation, mg/100ml	ASTM D 381	Max. 4
9	Sulphur_total, % mass	ASTM D 1266/ ASTM D 4294	Max. 0.1
10	Doctor Test or Sulphur_mercaptan, % mass	ASTM D 4952 ASTM D 3227/ IP 104	Negative Max. 0.001
11	Distillation: Initial Boiling Point, °C 10% vol. recovery, °C 50% vol. recovery, °C 90% vol. recovery, °C Final Boiling Point, °C Residue, % vol.	ASTM D 86	To be reported Max. 75 Min. 80 - Max. 125 Max. 180 Max. 210 Max. 2.0

SPECIFICATION OF JET A-1

SL	TESTS	METHOD	LIMIT
	Appearance		Clear, bright, visually free From solid matter and un- Dissolved water at normal Ambient temperature.
A	Visual	Visual
B	Colour (Saybolt)	ASTM D 156/6045	Report
C	Particulate contamination at point of Manufacture, mg/ I	IP423/ ASTM D 5452	Max. 1.0
	Composition:
A	Total Acidity, mg KOH/g	ASTM D 445	Max. 0.015
B	Aromatics, %vol.	ASTM D 1319 /D2425 / D6379 / IFP 9409	Max. 20
C	Olefins Content, %vol.	Covenin 887	Max. 5.0
D	Sulfur, Total, % wt	ASTM D 445	Max. 0.25

SPECIFICATION OF DIESEL

* Winter shall be the period from November to February (both months inclusive) and rest of the months the year shall be called as Summer.

SL	TESTS	METHOD	LIMIT
1	Density at 15°C, kg/L	ASTM D 1298	Min. 0.82 Max. 0.87
2	Colour, ASTM	ASTM D1500	Max. 3.0
3	Neutralization Value: Strong Acid No., mg KOH/gm Total Acid No., mg KOH/mg	ASTM D 664/ASTM D 974	Nil Max. 0.2
4	Ash content, % wt	ASTM D 482	Max. 0.01
5	Carbon Residue (Conrad son) on 10% Bottom, %wt	ASTM D 489	Max. 0.2
6	Cetane Number	ASTM D 613	Min. 45
7	Cetane Index (calculated)	ASTM D 976	Min. 45
8	Pour Point, °C	ASTM D 97	Max. 9 (Winter*); Max. 12 (Summer)
9	Copper Strip Corrosion (3 hour at 100 °C)	ASTM D 130	Max. No.1
10	Flash Point PM (cc)/ Abel, °C	ASTM D 93/ IP 170	Min. 32
11	Kinematic Viscosity at 38 °C, cst	ASTM D 445	Max. 9.0
12	Sulphur total, % wt	ASTM D 4294	Max. 0.5
13	Sediment, % wt vol	ASTM D 473	Max. 0.01
14	Water content, % vol.	ASTM D 95	Max. 0.1
15	Distillation: 90% vol. recovery, °C	ASTM D 86	Max. 375

SPECIFICATION OF LPG

SL	TESTS	METHOD	LIMIT
1	Density at 15°C,KG/L	ASTM D 1657	Min,0.55;Max,0.60
2	Vapour Pressure at 40°C,psi	ASTM D 1267	Max.100
3	Copper Strip Corrosion (1 hour at 37.8°C)	ASTM D 1838	Max.No.1
4	Volatility: Evaporation Temperature for 95%vol,°C(°F)	ASTM D 1837	Max. 2.2(36)
5	Total Volatile Sulphur,% wt	ASTM D 2784	Max. 0.02
6	Hydrogen Sulphide	UOP 212	NIL

Products

Contact

Office

Rubel Aziz
Managing Director
rubelaziz@partex.net

Subir kumar Ghose
CEO
subir@partex.net

Corporate Office:
74 Bir Uttam A.K. Khandaker Sarak, Mohakhali C/A
Dhaka - 1212, Bangladesh.
Phone: +880 2 222 262888 / Fax: +880 2 984 3888
www.partex.net

Factory

Address

Dangarchar Road 3, Ward 1 (KA), Julda Union Parishad,
Karnaphuli, Chittagong, Bangladesh

Welcome

Energy. Power. Progress.

Few Words About Us

Partex Petro

Products

MS/Petrol

Octane

Jet A-1

Diesel

LPG

Contact

Address