Diesel Oil EN590 10ppm and Kerosene JET-A1 Buyer and Importer
DIESEL OIL EN590 SPECIFICATION
Aspect Colour Visual Inspection ASTM D 1500 Clear 2.0
Density @ 15oC EN ISO 3675:98 EN ISO 12185:96/C1:2001 Kg/m3 820.0 845.0
Flash Point EN ISO 2719:2002 oC 55(1)
Distillation:
• Recovered @ 150oC 85.0(2)% vol
• Recovered @ 250oC 2.0% vol
• Recovered @ 350oC 65.0(2)% vol
• Recovered @ oC 95% EN ISO 3405:2000 360.0
C.F.P.P (Summer) (3)
C.F.P.P (winter) (3) EN116:1997 oC
oC 50.0 212
CLOUD Point (summer)
CLOUD Point (winter) EN23015:1994 oC
Cetane Number EN ISO 5165:1998 no 51.0
Cetane Index EN ISO 4264: 1996 index 46.0
Viscosity @ 40oC EN ISO 3104:1996 mm2/s 2.00 4.50
Water Content EN ISO 12937:2000 mg/kg 200
Total Contamination EN ISO 12662:2002 mg/kg 15
Sulphur Content EN ISO 2160:1998 mg/kg 10.0
Copper Strip Corrosion (3 hr of 50oC) EN ISO 2160;1998 Indice 1st Class
Carbon Residue (on 10% distillation residue) EN ISO 10370:1995 % weight 0.15
Total Acidity ASTM D 974:2002 mgKOH/g 0.3
Ash Content 0.01
Lubricity, current wear scar 460
Oxidation Stability
Electrical Conductivity (4) 5.0
Polycyclic Aromatic Hydrocarbon9 11.0(6)
Biodiesel Content (5) EN 14078:2003 %vol 4.5 7.0
JET-A1 SPECIFICATION
1 Visual Appearance Clear & bright, free from solid matter& undissolved water at ambient temperature Clear & bright
2 Colour Report ASTM D156 or ASTM D6054 25
3 Particulate Contamination, at the point of manufacture IP 423 / ASTM D5425
4 Particulate, at the Point of manufacture
• ≥ 4 µµ(c) Report IP 564 or IP 565 2500
• ≥ 6 µµ(c) Report 950
• ≥ 14 µµ(c) Report 99
• ≥ 21 µµ(c) Report 22
• ≥ 25 µµ(c) Report 15
• ≥ 30 µµ(c) Report 10
2 COMPOSITION
1 Total Acidity, mg KOH/gm 0.015 Max ASTM D 3242 0.009
2 Aromatic Hydrocarbon Types
• Aromatics % v/v 25 Max IP 156 / ASTM D1319 18.5
• Total Aromatics % v/v 26.5 Max IP 436 / ASTM D6379 18.5
3 Sulphur, Total % m/m 0.3 Max ASTM D4294 0.25
Sulphur Mercaptan % m/m 0.003 Max ASTM D3227 0.0020
4 Doctor Test Doctor Negative IP 30
5 Refining Components at the point of manufacture
• Hydro-processed component, % v/v Report
• Severely Hydro processed component, % v/v Report
3 VOLATILITY
1 Distillation – IBP oC ASTM D 86 155
2 • Fuel recovered 10% by volume at oC 205 Max - 171
• Fuel recovered 50% by volume at oC Report - 195
• Fuel recovered 90% by volume at oC Report - 195
• Final Boiling Point oC 300 Max - 254
• Residue % volume 1.5 Max - 1.0
• Loss % volume 1.5 Max - 1.0
3 Flash Point oC 38 min. IP 170 42
4 Density @ 15oC kg/m3 Min 775
Max 840 IP 365 / ASTM D4052 799
4 FLUIDITY
1 Freezing Point oC Minus 47 Max IP 1 / ASTM D2386 Minus 52
2 Kin. Viscosity at minus 20oC, mm 8.00 Max IP 71 / ASTM D445 4.10
5 COMBUSTION
1 Smoke Point, mm or 25 Min. ASTM D1322 / IP 57 24
Smoke Point 19 Min. ASTM D1322 / IP 57
And Naphthalene, % vol. 3 Max. ASTM 1840 2.3
2 Specific Energy MJ/kg, Min 42.8 Annex C 43.27
6 CORROSION
Cu strip for 2 hours @ 100oC Not worse than No.1 ASTM D130 No.1
7 THERMAL STABILITY, JFTOT IP 323 / ASTM D3241
1 Thermal Stability, JFTOT
Test Temperature oC Min 260
2 Tube Rating, visual Less than 3 (no peacock) or abnormal colour Zero, no peacock20.0 845.0
Flash Point EN ISO 2719:2002 oC 55(1)
Distillation:
• Recovered @ 150oC 85.0(2)% vol
• Recovered @ 250oC 2.0% vol
• Recovered @ 350oC 65.0(2)% vol
• Recovered @ oC 95% EN ISO 3405:2000 360.0
C.F.P.P (Summer) (3)
C.F.P.P (winter) (3) EN116:1997 oC
oC 50.0 212
CLOUD Point (summer)
CLOUD Point (winter) EN23015:1994 oC
Cetane Number EN ISO 5165:1998 no 51.0
Cetane Index EN ISO 4264: 1996 index 46.0
Viscosity @ 40oC EN ISO 3104:1996 mm2/s 2.00 4.50
Water Content EN ISO 12937:2000 mg/kg 200
Total Contamination EN ISO 12662:2002 mg/kg 15
Sulphur Content EN ISO 2160:1998 mg/kg 10.0
Copper Strip Corrosion (3 hr of 50oC) EN ISO 2160;1998 Indice 1st Class
Carbon Residue (on 10% distillation residue) EN ISO 10370:1995 % weight 0.15
Total Acidity ASTM D 974:2002 mgKOH/g 0.3
Ash Content 0.01
Lubricity, current wear scar 460
Oxidation Stability
Electrical Conductivity (4) 5.0
Polycyclic Aromatic Hydrocarbon9 11.0(6)
Biodiesel Content (5) EN 14078:2003 %vol 4.5 7.0
JET-A1 SPECIFICATION
1 Visual Appearance Clear & bright, free from solid matter& undissolved water at ambient temperature Clear & bright
2 Colour Report ASTM D156 or ASTM D6054 25
3 Particulate Contamination, at the point of manufacture IP 423 / ASTM D5425
4 Particulate, at the Point of manufacture
• ≥ 4 µµ(c) Report IP 564 or IP 565 2500
• ≥ 6 µµ(c) Report 950
• ≥ 14 µµ(c) Report 99
• ≥ 21 µµ(c) Report 22
• ≥ 25 µµ(c) Report 15
• ≥ 30 µµ(c) Report 10
2 COMPOSITION
1 Total Acidity, mg KOH/gm 0.015 Max ASTM D 3242 0.009
2 Aromatic Hydrocarbon Types
• Aromatics % v/v 25 Max IP 156 / ASTM D1319 18.5
• Total Aromatics % v/v 26.5 Max IP 436 / ASTM D6379 18.5
3 Sulphur, Total % m/m 0.3 Max ASTM D4294 0.25
Sulphur Mercaptan % m/m 0.003 Max ASTM D3227 0.0020
4 Doctor Test Doctor Negative IP 30
5 Refining Components at the point of manufacture
• Hydro-processed component, % v/v Report
• Severely Hydro processed component, % v/v Report
3 VOLATILITY
1 Distillation – IBP oC ASTM D 86 155
2 • Fuel recovered 10% by volume at oC 205 Max - 171
• Fuel recovered 50% by volume at oC Report - 195
• Fuel recovered 90% by volume at oC Report - 195
• Final Boiling Point oC 300 Max - 254
• Residue % volume 1.5 Max - 1.0
• Loss % volume 1.5 Max - 1.0
3 Flash Point oC 38 min. IP 170 42
4 Density @ 15oC kg/m3 Min 775
Max 840 IP 365 / ASTM D4052 799
4 FLUIDITY
1 Freezing Point oC Minus 47 Max IP 1 / ASTM D2386 Minus 52
2 Kin. Viscosity at minus 20oC, mm 8.00 Max IP 71 / ASTM D445 4.10
5 COMBUSTION
1 Smoke Point, mm or 25 Min. ASTM D1322 / IP 57 24
Smoke Point 19 Min. ASTM D1322 / IP 57
And Naphthalene, % vol. 3 Max. ASTM 1840 2.3
2 Specific Energy MJ/kg, Min 42.8 Annex C 43.27
6 CORROSION
Cu strip for 2 hours @ 100oC Not worse than No.1 ASTM D130 No.1
7 THERMAL STABILITY, JFTOT IP 323 / ASTM D3241
1 Thermal Stability, JFTOT
Test Temperature oC Min 260
2 Tube Rating, visual Less than 3 (no peacock) or abnormal colour Zero, no peacock
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- Posted On:15 Apr, 2024
- Company Name:Show
- Contact Number:Show
- Purchaser:Iwan Prasetya
- Quantity Required1,000,000 Barrel
- Buying FrequencyMonthly
- Destination Port Rotterdam, Fujairah, Houston, ASWP
- Time of Validity1 Year
- Preferred Payment Method:T/T,L/C