Technical Specification : Import Products
[:en]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[:de]
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 Lanka Petrol – 95 Octane EURO 4 – Updated on 1st July 2018
Property/Test | Test Method (ASTM D) | Specifications |
---|---|---|
Appearance | bright, Clear and free from water, visible impurities & Dyes (Note 1) | |
Density @15 0C kg/m3 | ASTM D 1298 | 720-775 |
Reid Vapour Pressure @ 37.8 0C kPa | ASTM D 323 | 45-60 |
Research Octane Number (RON) | ASTM D 2699 | Min 95 |
MOTOR OCTANE NUMBER (MON) | ASTM D 2700 | Min 85 |
Distllation | ASTM D 86 | |
IBP 0C | Report | |
E100, Vol %, MIN-MAX | 46-71 | |
E150, Vol %, MIN | 75 | |
FBP, 0C , MAX | 210 | |
RESIDUE vol % | Max 2.0 | |
Doctor Test | IP 30/ASTM D 4952 | Sweet or Less than 15 ppm RSH |
Sulphur Content mg/kg | ASTM D 5453 ASTM D 2622 |
Max 50 |
Lead Content g/l | ASTM D 5059/ASTM D 3237 | Max 0.005 (Note 2) |
TOTAL AROMATICS % v/v | ASTM D 5580 | Max 35 |
WASHED GUMS mg/100 ml | ASTM D 381 | Max 5 |
OXYGENATE % v/v | ASTM D 4815 | Max 15 |
OXYGEN CONTENT % m/m (CALCULATED) | MAX 2.7 | |
OXIDATION STABILITY, Minutes | ASTM D 525 | Min 360 |
COPPER CORROSION 3h @ 50 0C | ASTM D 130 | MAX 1 |
BENZENE % v/v | ASTM D 3606/ASTM D 5580 | Max 1 |
OLEFINS CONTENT % v/v | ASTM D 1319/ASTM D 6730 | Max 18 |
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[:nl]
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[:]