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    Crude oil, Packaging Type : Drum, Glass Bottle

    • Supply TypeSupplier
    • Preferred Buyer Location All over the world

    Petroleum has mostly been recovered by oil drilling (natural petroleum springs are rare). Drilling is carried out after studies of structural geology (at the reservoir scale), sedimentary basin analysis, and reservoir characterization (mainly in terms of the porosity and permeability of geologic reservoir structures) have been completed. It is refined and separated, most easily by distillation, into a large number of consumer products, from gasoline (petrol) and kerosene to asphalt and chemical reagents used to make plastics and pharmaceuticals.
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    • calendar Member Since 9 Years
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    PropertiesUnitSpecificationTest Method
    Sp. Gr. 15.6/15.6 °C 0.8488ASTM D 5002
    API Gravity°API35.21ASTM D 5002
    Sulfur content%Wt1.69ASTM D 4294
    H2S Contentppm15IP 570
    Mercaptan Contentppm243UOP 163
    Nitrogen Content%Wt0.08ASTM D 5762
    Water & Sediment%Vol<0.05ASTM D 4007
    Water Content%Vol<0.025ASTM D 4006
    Salt ContentPTB4ASTM D 3230
    Kinematic Viscosity @10°Cmm²/s11.02ASTM D 445
    Kinematic Viscosity @20°Cmm²/s7.51ASTM D 445
    Kinematic Viscosity @40°Cmm²/s4.4ASTM D 445
    Pour Point°C-30ASTM D 5853
    RVPpsi8.5ASTM D 3230
    Asphaltene Content%Wt1.1IP 143
    Wax Content%Wt6.7BP 237
    Drop Melting Point of Wax°C52IP 133
    CCR%Wt3.4ASTM D 189
    Total Acid NumbermgKOH/g<0.05UOP 163
    Nickel Contentppm5ASTM D 5863
    Vanadium Contentppm11ASTM D 5863
    Iron Contentppm1ASTM D 5863
    Lead Contentppm<1ASTM D 5863
    Sodium Contentppm3ASTM D 5863
    Zinc Contentppm<1ASTM D 5863
    Copper Contentppm<1ASTM D 5863

    Iran Heavy Crude Oil

    PropertiesUnitSpecificationTest Method
    Sp. Gr. 15.6/15.6 °C 0.8592ASTM D 5002
    API Gravity°API33.19ASTM D 5002
    Sulfur content%Wt1.98ASTM D 4294
    H2S Contentppm18IP 570
    Mercaptan Contentppm25UOP 163
    Nitrogen Content%Wt0.13ASTM D 5762
    Water & Sediment%Vol<0.05ASTM D 4007
    Water Content%Vol<0.025ASTM D 4006
    Salt ContentPTB10ASTM D 3230
    Kinematic Viscosity @10°Cmm²/s16.4ASTM D 445
    Kinematic Viscosity @20°Cmm²/s9.59ASTM D 445
    Kinematic Viscosity @40°Cmm²/s5.58ASTM D 445
    Pour Point°C-24ASTM D 5853
    RVPpsi9.8ASTM D 3230
    Asphaltene Content%Wt1.5IP 143
    Wax Content%Wt5.5BP 237
    Drop Melting Point of Wax°C55IP 133
    CCR%Wt3.81ASTM D 189
    Total Acid NumbermgKOH/g<0.05UOP 163
    Nickel Contentppm12ASTM D 5863
    Vanadium Contentppm37ASTM D 5863
    Iron Contentppm1ASTM D 5863
    Lead Contentppm<1ASTM D 5863
    Sodium Contentppm7ASTM D 5863
    Zinc Contentppm<1ASTM D 5863
    Copper Contentppm<1ASTM D 5863

    Iraq Light Crude Oil

    PropertiesUnitSpecificationTest Method
    Density at 15°Ckg/L0.9011ASTM D 1298
    API Gravity at 60f °API25.44ASTM D 287
    Water by Distillation%Vol0.05ASTM D 4006
    Sediment by Extraction%Wt0.015ASTM D 473
    Sulfur%Wt3.705IP336
    Pour Point°C ASTM D5853
    Salt Contentlb/1000bbl4.6ASTM D3230
    Water KF%Wt1053ASTM D4928
    H2S Contentppm0.63UOP 163
    AciditymgKOH/g0.075ASTM D664
    Mercaptan Sulfurppm88.9ASTM D3227
    Kinematic Viscosity at 50°CcSt11.5581ASTM D445
    Asphalthenes%Wt5.5IP143
    IBP°C48ASTM D86
    Distillation at 5%°C82ASTM D86
    Distillation at 10%°C108ASTM D86
    Distillation at 20%°C169ASTM D86
    Distillation at 30%°C231ASTM D86
    Distillation at 40%°C282ASTM D86
    Distillation at 50%°C317ASTM D86
    Distillation at 60%°C332ASTM D86
    Distillation at 70%°C339ASTM D86
    Distillation at 80%°C350ASTM D86
    Distillation at 89%°C353ASTM D86
    FBP°C355ASTM D86

    Iraq Heavy Crude Oil Assays

    PropertiesUnitT-1AT-2T-4Test Method
    Density @15°Ckg/L0.90970.91530.9135ASTM D 5002
    Sp. Gr. @ 15.6/15.6°C 0.91020.91580.914Conversion
    API Gr. @15.6°C°API23.9623.0123.31Calculated
    Sulfur Content%Wt3.343.343.25ASTM D 4294
    Carbon Residue, Micro%Wt7.658.318.74ASTM D 4530
    Bottom Sediment & Water%Vol0.11.350.6ASTM D 4007
    Salt as NaClmg/L5.04156.3ASTM D 3230
    Ash Content @550°C%Wt0.0130.0490.012ASTM D 482
    Total Nitrogenppm0.14 0.13ASTM D 5762-01
    Copperppm<1<1<1IP 501 (Mod.)
    Ironppm11<1IP 501 (Mod.)
    Nickelppm121312IP 501 (Mod.)
    Vanadiumppm363736IP 501 (Mod.)
    Leadppm<1<1<1IP 501 (Mod.)
    Chromiumppm<1<1<1IP 501 (Mod.)
    Zincppm<11<1IP 501 (Mod.)
    Calciumppm5631IP 501 (Mod.)
    Magnesiumppm1<1<1IP 501 (Mod.)
    Sodiumppm15<1IP 501 (Mod.)
    Total Acid NumbermgKOH/g0.3020.0260.748ASTM D 664
    Vapor Pressure (DVPE)kPa11.220.76.6ASTM D 5191
    Pour Point (max/Upper)°C-39-24< -42ASTM D 5853
    Pour Point (min/Upper)°C< -42 < -42ASTM D 5853
    Flash Point°C< -5< -5< -5ASTM D 93 (Mod.)
    Asphaltenes%Wt5.24.825.5ASTM D 3279
    Wax Content%Wt 0.50.7 maxUOP 46
    Kinematic Viscosity @26.7°CcSt31.0340.1131.97ASTM D 445
    Kinematic Viscosity @37.8°CcSt19.3225.0919.55ASTM D 446
          
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