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 peacock Show More

  • 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

Indonesia

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