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Import Products Specification

Specification of GAS Oil (2500 mg/kg Max Sulphur) – Updated on 12th April 2013

Property/Test Test Method (ASTM D) Specifications
Appearance Clear and bright free from water & visible impurities
Density @15 0C kg/m 3 1298 820- 860
Colour 1500 Max 1.5
Distllation 86
IBP 0C Report
T10 0C Report
T50 0C Max 315
T80 0C Max 350
T95 0C Max 370
Cetane Index Or 976 / 4737 Min 46 (Note 1)
Cetane Number 613 Min 49
Cloud Point 0C 2500 Max 15.5
CFPP 0C 6371 Max 10
Sulphur Content mg/kg 4294 Max 2,500
Flash Point 0C 93 Min 60
Viscosity Kin. at 40 0C,cSt 445 2-4.5
Water Content mg/kg 6304 Max 500
CU – STRIP CORROSION 3 hrs AT 50 0C 130 Max 1
ASH % m/m 482 MAX. 0.01
CARBON RESIDUE % m/m 524 / 4530 Max 0.3
PARTICULATE CONTAMINANTS,TOTAL mg/kg 6217 Max 10
TOTAL ACID NUMBER. mg KOH/g 664 Max 0.15
CALORIFIC VALUE GROSS k cal/kg 240 Min 10,500
OXIDATION STABILITY g/m3 2274 Max 25
DSEP RATING 7261 50-100
FAME 7371 Nil (Note 2)
LUBRICITY
(HFRR wear scar dia.@600C) micron
6079 Max 400

Important:
Note 1: Not Applicable if any Cetane Improver Additive is present
Note 2: Addition of Bio Deisel or BioDiesel blends are not permitted

Specifications of GAS Oil(500 mg/kg Max Sulphur) – Updated on 12th April 2013

Property/Test Test Method (ASTM D) Specifications
Appearance Clear, bright and free from water & visible impurities
Density @15 0C kg/m3 1298 820- 860
Colour 1500 Max 1.5
Distllation 86
IBP DEG C Report
T10 0C Report
T50 0C Report
T85 0C Max 350
T95 0C Max 370
Cetane Index Or 976 / 4737 Min 46 (Note 1)
Cetane Number 613 Min 49
Cloud Point 0C 2500 Max 15
CFPP 0C 6371 Max 5
Sulphur Content mg/kg 4294 Max 500
Flash Point 0C 93 Min 55
Viscosity Kin. at 40 0C,cSt 445 2-4.5
Water Content mg/kg 6304 Max 200
CU – STRIP CORROSION 3 hrs AT 50 0C 130 Max 1
ASH % m/m 482 MAX. 0.01
CARBON RESIDUE % m/m 524 / 4530 Max 0.3
PARTICULATE CONTAMINANTS,TOTAL mg/kg 6217 Max 10
TOTAL ACID NUMBER. mg KOH/g 664 Max 0.08
CALORIFIC VALUE GROSS k cal/kg 240 Min 10,500
OXIDATION STABILITY g/m3 2274 Max 25
DSEP RATING 7261 50-100
FAME 7371 Nil (Note 2)
LUBRICITY
(HFRR wear scar dia.@600C) micron
6079 Max 400

Important:
Note 1: Not Applicable if any Cetane Improver Additive is present
Note 2: Addition of Bio Deisel or BioDiesel blends are not permitted

Specifications of Gasoline(90 UNL) – Updated on 17th January 2013

Property/Test Test Method (ASTM D) Specifications
Appearance bright, & Clear and free from water, visible impurities & Dyes (Note 1)
Density @15 0C kg/m3 1298 725-785
Reid Vapour Pressure @ 37.8 0C kPa 323 45-60
Research Octane Number 2699 Min 90
Distllation 86
IBP 0C Report
T10 0C 45-70
T50 0C 80-125
T90 0C Max 180
FBP 0C Max 205
Residue vol. % Max 2.0
E150 vol. % Min 70
Doctor Test IP 30/4952 Sweet or Less than 15 ppm RSH
Sulphur Content mg/kg 4294 Max 500
Lead Content g/l 5059 Max 0.013 (Note 2)
Unwashed Gums mg/100 ml 381 Max 70
WASHED GUMS mg/100 ml 381 Max 5
OXYGENATE % v/v 4815 Max 15
OXYGEN CONTENT % m/m (CALCULATED) MAX 2.7
OXIDATION STABILITY, Minutes 525 Min 480
COPPER CORROSION 3h @ 50 0C 130 MAX 1
BENZENE % v/v 3606 Max 2.5
TOTAL AROMATICS % v/v 5580 Max 40

Note 1: Specify tagging components, if any.
Note 2: No intentional addition of lead compounds.

Important:
* There shall be no intentional addition of metal compounds containing Ferrous, Manganese & Phosphorus.
* Addition of alcohols are not permitted.

Specifications of Gasoline(95 UNL) – Updated on 17th January 2013

Property/Test Test Method (ASTM D) Specifications
Appearance bright, Clear and free from water, visible impurities & Dyes (Note 1)
Density @15 0C kg/m3 1298 725-785
Reid Vapour Pressure @ 37.8 0C kPa 323 45-60
Research Octane Number 2699 Min 95
MOTOR OCTANE NUMBER (MON) 2700 Min 85
Distllation 86
IBP 0C Report
T10 0C 45-70
T50 0C 80-125
T90 0C Max 180
FBP 0C Max 215
Residue vol. % Max 2.0
E150 vol. % Min 75
Doctor Test IP 30/4952 Sweet or Less than 15 ppm RSH
Sulphur Content mg/kg 4294 Max 500
Lead Content g/l 5059 Max 0.013 (Note 2)
Unwashed Gums mg/100 ml 381 Max 70
WASHED GUMS mg/100 ml 381 Max 5
OXYGENATE % v/v 4815 Max 15
OXYGEN CONTENT % m/m (CALCULATED) MAX 2.7
OXIDATION STABILITY, Minutes 525 Min 480
COPPER CORROSION 3h @ 50 0C 130 MAX 1
BENZENE % v/v 3606 Max 2.5
TOTAL AROMATICS % v/v 5580 Max 40

Note 1: Specify tagging components, if any.
Note 2: No intentional addition of lead compounds.

Important:
* There shall be no intentional addition of metal compounds containing Ferrous, Manganese & Phosphorus.
* Addition of alcohols are not permitted.

Low Sulphur Fuel Oil 180 CST

Property/Test Test Method ASTM-D CPC Specifications
DENSITY @ 15DEG C kg/m3 160 1298 900 – 970
FLASH POINT PM CC, Deg C 34 93 Min 60
POUR POINT Deg C 15 97 Max 21.1
TOTAL SULPHUR CONTENT % (w/w) 61 4294 Max 1.8
VISCOSITY KINEMATIC @ 50Deg C, Cst 71 445 90-175
WATER CONTENT % (v/v) 74 95 Max 1.0
ASH % (w/w) 4 482 Max 0.1
CONDRADSON CARBON % (w/w) 189 Max 12
SEDIMENT BY EXTRACTION % wt. 53 473 Max 0.1
TOTAL SEDIMENT POTENTIAL % m/m 375 4870 Max 0.1
CALORIFIC VALUE GROSS, Kcal/kg 12 240 Min 10,300
STRONG ACID KOH mg/g 1 974 Nil
Metal Contaminants
V 288 3605 Max 65 ppm
Pb 3605 Max 1 ppm
A1 + SI 501/377 Max 80 ppm
Na + K 3605 Max 30 ppm
Zn 501/470 Max 5 ppm
PHOSPHORUS 501/500 Max 15 ppm
Ca 501/470 Max 10 ppm
Fe 3605 Max 5 ppm

Notes:
(I) The fuel shall not include any added substances or chemical waste, which jeopardizes the safety of installations or adversely affects the performances of the machines or is harmful to personnel or contributes overall to air pollution.
(Ii) This fuel is used in power plants having heavy duty gas turbines which are connected to the national grid of the country’s electricity supply. As such the seller must take every precaution to supply low sulphur fuel oil 180 cst. as per the tender specifications and he is responsible to supply merchantable grade of products.
(iii) The product should be loaded from shore tanks to meet the said specifications, preferable ex-refinery and should always avoid ship to ship transfers or other type of fuel oil blending, to avoid blending with condensate.
(iv) Seller is hereby made responsible for the quality of low sulphur fuel oil cargo purchased from other suppliers and supplied to cpc.
(v) The independent inspector mutually appointed by the seller and the buyer should certify that the product loaded is free from used lubricating oil ((ulo) as described in annex. h of the iso 8217:2005 (e) standards for petroleum products – fuels (class f) – specifications of marine fuels).
(vi) The independent inspector mutually appointed by the seller and the buyer shall forward the analysis report and the tank inspection certificate before loading, to both parties.
(vii) Under no circumstances the cargo should be loaded to the vessel without obtaining the prior approval from CPC for quality and ship tank inspection report.

High Sulphur Fuel Oil 180 CST

 

Property/Test Test Method ASTM-D CPC Specifications
DENSITY @ 15DEG C kg/m3 160 1298 Max 970
FLASH POINT PM CC, Deg C 34 93 Min 60
POUR POINT Deg C 15 97 Max 21.1
TOTAL SULPHUR CONTENT % (w/w) 61 4294 Max 3.5
VISCOSITY KINEMATIC @ 50Deg C, Cst 71 445 165-175
WATER CONTENT % (v/v) 74 95 Max 1.0
ASH % (w/w) 4 482 Max 0.1
CONDRADSON CARBON % (w/w) 189 Max 12
SEDIMENT BY EXTRACTION % wt. 53 473 Max 0.25
ASPHALTENES m/m % 143 6560 Max 4.0
CALORIFIC VALUE GROSS, Kcal/kg 12 240 Min 10,200
STRONG ACID KOH mg/g 1 974 Nil
Metal Contaminants
V 288 3605 Max 200 ppm
Pb 3605 Max 15 ppm
A1 + SI 501/377 Max 80 ppm
Na + K 3605 Max 30 ppm
Zn 501/470 Max 15 ppm
Ca 501/470 Max 30 ppm
PHOSPHORUS 501/500 Max 15 ppm
Fe 3605 Max 15 ppm

Notes:
(i) This fuel is used in heavy duty marine engines to generate power of which the supply is directly cnnected to the national grid. As such the seller must take every precaution to supply high sulphur fuel oil 180 cst. as per the tender specifications. As such the supplier is responsible to supply merchantable grade of products.

(ii) This fuel shall not include any added substances or chemical waste, which jeopardizes the safety of installations or adversely affects the performances of the machines or is harmful to personnel or contributes to overall air pollution.

(iii) The product should be loaded from shore tanks to meet the said specifications, preferable ex-refinery and should always avoid ship to ship transfers or other type of fuel oil blending, to avoid blending with condensate.

(iv) Seller is hereby made responsible for the quality of high sulphur fuel oil cargo purchased from other suppliers and supplied to CPC.

(v) The independent inspector mutually appointed by the seller and the buyer should certify that the product loaded is free from used lubricating oil ((ulo) as described in annex. h of the iso 8217:2005 (e) standards for petroleum products – fuels (class f) – specifications of marine fuels.

(vi) The independent inspector mutually appointed by the seller and the buyer shall forward the analysis report and the tank inspection certificate before loading, to both parties.

(vii) Under no circumstances the cargo should be loaded to the vessel without obtaining the prior approval from CPC for quality and ship tank inspection report.

Specification for Lanka SBP – 17th January 2013

Property/Test Test Method ASTM-D CPC Specifications
Density @15◦C kg/m3 160 1298 Max 725
Colour Saybolt 156 Min 60
Distillation
I.B.P. ◦C Min 60
10% Evaporated ◦C Report
30% Evaporated ◦C Report
50% Evaporated ◦C 85-105
70% Evaporated ◦C Report
90% Evaporated ◦C 105-130
95% Evaporated ◦C Max 145
98.5% Evaporated ◦C Max 160
Residue % vol Max 1
Sulphur Content ppm 243 4294 Max 50
Aromatic Content % vol 156 1319 Max 16
Cu Strip Corrosion 3 hrs @ 50◦C 154 130 Max 1

Specification of JET A-1

As per the AVIATION FUEL QUALITY REQUIREMENTS FOR JOINTLY OPERATED SYSTEMS (AFQRJOS) – Issue 27 – February 2013

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