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1 Products availableOur offered Product range includes Bitumen All Grades, Fuel Oil CST 380, Bitumen 6070, Gasoil D2 0.5-0.7% sulfur and Bitumen.
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Asphalt , also known as Bitumen is a sticky, black and highly viscous liquid or semi-solid form of petroleum. It may be found in natural deposits or may be a refined product; it is a substance classed as a pitch. The primary use (70%) of asphalt/bitumen is in road construction, where it is used as the glue or binder mixed with aggregate particles to create asphalt concrete. Its other main uses are for bituminous waterproofing products, including production of roofing felt and for sealing flat roofs. Asphalt concrete pavement mixes are typically composed of 5% asphalt/bitumen cement and 95% aggregates (stone, sand, and gravel).
Specifications
Properties | Unit | Bitumen 40/50 | Bitumen 60/70 | Bitumen 85/100 | Test Method |
---|---|---|---|---|---|
Sp. Gr. @25/25°oC | - | 1.01/1.06 | 1.01/1.06 | 1.00/1.05 | ASTM D 70 |
Penetration @25oC | - | 40/50 | 60/70 | 85/100 | ASTM D 5762 |
Softening Point | oC | 52/60 | 49/56 | 45/52 | ASTM D 36 |
Ductility @25oC | - | 100 min | 100 min | 100 min | ASTM D 113 |
Loss on Heating | %Wt | 0.2 max | 0.2 max | 0.5 max | ASTM D 6 |
Drop in Penetration after Heating | % | 20 max | 20 max | 20 max | ASTM D 6 & ASTM D 5 |
Flash Point | oC | 250 min | 250 min | 225 min | ASTM D 92 |
Solubility in CS2 | %Wt | 99.5 min | 99.5 min | 99.5 min | ASTM D 4007 |
Spot Test | - | Negative | Negative | 0.2 max | AASHO T102 |
Fuel Oil, (also known as marine fuel or heavy oil) is a fraction obtained from petroleum distillation, either as a distillate or a residue. Broadly speaking, fuel oil is any liquid fuel that is burned in a furnace or boiler for the generation of heat or used in an engine for the generation of power, except oils having a flash point of approximately 40 °C (104 °F) and oils burned in cotton or wool-wick burners. In this sense, diesel is a type of fuel oil. Fuel oil is made of long hydrocarbon chains, particularly alkanes, cycloalkanes and aromatics. The term fuel oil is also used in a stricter sense to refer only to the heaviest commercial fuel that can be obtained from crude oil, i.e., heavier than gasoline and naphtha.
Oil has many uses; it heats homes and businesses and fuels trucks, ships and some cars. A small amount of electricity is produced by diesel, but it is more polluting and more expensive than natural gas. It is often used as a backup fuel for peaking power plants in case the supply of natural gas is interrupted or as the main fuel for small electrical generators.
Fuel Oil (M100)
Properties | Unit | Specification | Test Method | |||
---|---|---|---|---|---|---|
Density at 15oC | kg/L | 0.950 MAX | ASTM D1298/12 | |||
Kinematic Viscosity at 50oC | cSt | 150 MAX | ASTM D445/15 | |||
Flash Point | oC | 150 MAX | ASTM D93/15 | |||
Water Content | % (V/M) | 0.5 MAX | ASTM D95/13 | |||
Sulfur Content | %Wt | 2 MAX | ASTM D4294/16 | |||
Vanadium | ppm | 10 MAX | IP 470/05 | |||
Aluminum | ppm | 15 MAX | IP 470/05 | |||
Calcium | ppm | 70 MAX | IP 470/05 | |||
Silicon | ppm | 15 MAX | IP 470/05 | |||
Zinc | ppm | 10 MAX | IP 470/05 | |||
Nickel | ppm | 15 MAX | IP 470/05 | |||
Sodium | ppm | 100 MAX | IP 470/05 |
Cracked Fuel Oil (CFO)
Properties | Unit | Specification | Test Method | |||
---|---|---|---|---|---|---|
Flash Point | oC | 80 Min. | ASTM D 93 | |||
Viscosity@100oC | cSt | 42444 | ASTM D 88 | |||
Specific gravity@15oC | - | 1.01-1.06 | ASTM D 1298 | |||
Ash | ppm (wt) | 150 Max. | ASTM D 482 | |||
Sulfur | %Wt | 0.5 Max. | ASTM D 5453 | |||
Carbon Content | %Wt | 80 Min. | ASTM D 5291 |
Fuel Oil 280 CST
Properties | Unit | Specification | Test Method | |||
---|---|---|---|---|---|---|
Density at 15°C | kg/m³ | 970 max | ASTM D 1298 | |||
Kinematic Viscosity @50°C | cSt | 280 max | ASTM D 445 | |||
Redwood Viscosity @ 37.8°C | Rsecs | 2500 max | Calculated | |||
Pour Point | °C | 24 min | ASTM D 97 | |||
Flash Point | °C | 65 max | ASTM D 93 | |||
Sulfur Content | %Wt | 3.5 max | ASTM D 1552 | |||
CCR | %Wt | 15 max | ASTM D 189 | |||
Ash | %Wt | 0.05 max | ASTM D 482 | |||
Water & Sediment | %Vol | 0.5 max | ASTM D 1796 | |||
Calorific Value (Higher) | Mj/kg | 41.8 min | Calculated |
Fuel Oil 380 CST
Properties | Unit | Specification | Test Method | |||
---|---|---|---|---|---|---|
Density at 15°C | kg/m³ | 990 max | ASTM D 1298 | |||
Kinematic Viscosity @50oC | cSt | 380 max | ASTM D 445 | |||
Pour Point | oC | 32 max | ASTM D 97 | |||
Flash Point | oC | 65 min | ASTM D 93 | |||
Sulfur Content | %Wt | 3.5 max | ASTM D 1552 | |||
CCR | %Wt | 15 max | ASTM D 189 | |||
Ash | %Wt | 0.15 max | ASTM D 482 | |||
Water & Sediment | %Vol | 1 max | ASTM D 1796 | |||
Calorific Value (Higher) | Mj/kg | 41.7 min | Calculated |
LPG has a very wide variety of uses, mainly used for cylinders across many different markets as an efficient fuel container in the agricultural, recreation, hospitality, calefaction, construction, sailing and fishing sectors. It can serve as fuel for cooking, central heating and to water heating and is a particularly cost-effective and efficient way to heat off-grid homes. In the safety font LPG cylinders must be updated to new standards in safety and user experience, giving a huge contribution for domestic usage. It can be used for cooking, rural heating, motor fuel and refrigeration.
Propane
Properties | Unit | Specification | Test Method |
---|---|---|---|
Sp. Gr. 15.6/15.6oC | - | To be Reported | ASTM D 2598 |
Vapor pressure @37.8oC | psig | 200 max | ASTM D 1267 or D 2598 |
Propane Content | %Vol | 96 min | ASTM D 2163 |
Ethane Content | %Vol | 2 max | ASTM D 2163 |
Volatile Residue (Butane+) | %Vol | 2.5 max | ASTM D 2163 |
Residue on evaporation of 100ml | - | 0.05 max | ASTM D 2158 |
Oil stain observation | - | Pass | ASTM D 2158 |
Copper corrosion | - | No. 1 strip | ASTM D 1838 |
Sulfur content (ppm) | ppm | 40 max | ASTM D 1266 or D 5453 |
H2S Content | - | Negative | ASTM D 2420 or IP 103 |
Moisture | - | Pass | ASTM D 2713 or D 1744 |
Butane
Properties | Unit | Specification | Test Method |
---|---|---|---|
Sp. Gr. 15.6/15.6oC | - | To be Reported | ASTM D 2598 |
Vapor pressure @37.8oC | psig | 70 max | ASTM D 1267 or D 2598 |
Butane Content | %Vol | 95 min | ASTM D 2163 |
Volatile Residue (Pentane+) | %Vol | 2 max | ASTM D 2163 |
Copper corrosion | - | No. 1 strip | ASTM D 1838 |
Sulfur content (ppm) | ppm | 80 max | ASTM D 1266 or D 5453 |
H2S Content | - | Negative | ASTM D 2420 |
Moisture | - | None | Visual |
Pyrolysis gasoline or Pygas is a naphtha-range product with a high aromatics content. It is a by-product of high temperature naphtha cracking during ethylene and propylene production. PyGas has high potential for use as a gasoline blending mixture and/or as a source of aromatics. Currently, PyGas is generally used as a gasoline blending mixture due to its high octane number. Pyrolysis gasoline can be blended with other hydrocarbons as a gasoline additive, or distilled (in BTX process) to separate it into its components, including benzene.
Petrol is a transparent, petroleum-derived liquid that is used primarily as a fuel in internal combustion engines. The characteristic of a particular gasoline blend to resist igniting too early (which causes knocking and reduces efficiency in reciprocating engines) is measured by its octane rating. Tetraethyllead and other lead compounds are no longer used in most areas to regulate and increase octane-rating, but many other additives are put into gasoline to improve its chemical stability, control corrosiveness and provide fuel system ‘cleaning, ’ and determine performance characteristics under intended use. Sometimes, gasoline also contains ethanol as an alternative fuel, for economic or environmental reasons.
Gasoline A-85
Properties | Unit | Specification | Test Method | ||||||
---|---|---|---|---|---|---|---|---|---|
Density @20 oC | g/cm3 | 0.725 Max | ASTM D 1298 | ||||||
Color | Saybolt | Light/ Red, Yellow | – | ||||||
Total Sulfur | ppm | 500 Max | ASTM D 4294 | ||||||
Lead Content | ppb | 10 Max | A.A | ||||||
IBP | oC | 35 Min | ASTM D 86 | ||||||
FBP | oC | 210 Max | ASTM D 86 | ||||||
Paraffin Naphthenes | %Wt | 40 Min | G.C | ||||||
Aromatics | %Wt | 25 Max | G.C | ||||||
Others | %Wt | 15 Max | G.C | ||||||
RON | - | 85 Min | Infrared |
Gasoline A-92
Properties | Unit | Specification | Test Method | ||||||
---|---|---|---|---|---|---|---|---|---|
Density@ 20 oC | g/ml | 0.755 Max | ASTM D 1298 | ||||||
Color | Saybolt | Light Red/Yellow | – | ||||||
Total Sulfur | ppm | 100 Max | ASTM D 4294 | ||||||
Lead Content | ppb | 10 Max | A.A | ||||||
IBP | oC | 35 Min | ASTM D 86 | ||||||
FBP | oC | 210 Max | ASTM D 86 | ||||||
Paraffin Naphthenes | %Wt | 30 Min | G.C | ||||||
Aromatics | %Wt | 35 Max | G.C | ||||||
Benzene | %Wt | 1 Max | G.C | ||||||
Others | %Wt | 15 Max | G.C | ||||||
RON | - | 92 Min | Infrared | ||||||
MON | - | 84 Min | Infrared |
Gasoline A-95
Properties | Unit | Result | Expected | Test Method | ||||
---|---|---|---|---|---|---|---|---|
Density @15oC | g/cm3 | 0.7391 | 710 min – 780 max | ASTM D 1298 | ||||
RON | - | 95.2 | 95 min | ASTM D 2699 | ||||
MON | - | 85.2 | 85 min | ASTN D 2700 | ||||
RVP @ 37.8oC | kPa | 63.2 | 49 min – 83 max | ASTM D 323 | ||||
Distillation, 10% vol. recovered | °C | 50.3 | 74 max | ASTM D 86 | ||||
Distillation, 50% vol. recovered | °C | 82.2 | 127 max | ASTM D 86 | ||||
Distillation, 90% vol. recovered | °C | 167.1 | 190 max | ASTM D 86 | ||||
FBP | oC | 202.6 | 225 max | ASTM D 86 | ||||
Olefins Content | %Vol | 9.5 | 26 max | ASTM D 1319 | ||||
Aromatics Content | %Vol | 26.7 | 35 max | ASTM D 5580 | ||||
Benzene Content | %Vol | 0.64 | 1 max | ASTM D 5580 | ||||
Oxygenates (MTBE) | %Vol | 12.9 | 15 max | ASTM D 4815 | ||||
Total Sulfur Content | ppm | 11 | 150 max | ASTM D 5453 | ||||
Lead content | g/L | <0.0025 | Nil | ASTN D 3237 | ||||
Color | - | Undyed | Report | Visual |
Dry Pyrolysis Gasoline (DPG)
Properties | Unit | Result | Expected | Test Method | ||||
---|---|---|---|---|---|---|---|---|
Density @15.6 oC | g/cm3 | 0.85 | 0.9 Max | ASTM D 4052 | ||||
RVP | psi | 6.5 | Report | ASTM D 323 | ||||
Total Sulfur | ppm | 180 | Report | ASTM D 5453 | ||||
IBP | oC | 38 | Report | ASTM D 86 | ||||
FBP | oC | 185 | Report | ASTM D 86 | ||||
5% Vol Recovered | oC | 51 | Report | ASTM D 86 | ||||
95% Vol Recovered | °C | 177 | Report | ASTM D 86 | ||||
Paraffin | %Wt | 2.1 | Max 3 | G.C | ||||
Olefins | %Wt | 24.5 | Max 30 | G.C | ||||
Naphthenes | %Wt | 0.4 | Max 0.6 | G.C | ||||
Aromatics | %Wt | 66.4 | 60 Min | G.C | ||||
Others | %Wt | 6.6 | 20 Max | G.C | ||||
Benzene Content | %Wt | 42.4 | 40 Min | G.C |
Hydrogenated Pyrolysis Gasoline (HPG)
Properties | Unit | Specification | Test Method | ||||||
---|---|---|---|---|---|---|---|---|---|
Specific gravity @15°C | - | 0.78 – 0.84 | ASTM D 1298 | ||||||
Color | Saybolt | + 5 Min. | ASTM D 156 | ||||||
RVP | psi | 5 – 12 | ASTM D 323 | ||||||
IBP | oC | 34 Min. | ASTM D 86 | ||||||
FBP | oC | 210 Max. | ASTM D 86 | ||||||
Aromatics | %Wt | 50 Min. | By GC | ||||||
Total Sulfur | ppm (wt) | 300 Max. | ASTM D 3120 | ||||||
Copper Corrosion | - | No. 1a | ASTM D 130 | ||||||
Lead Content | ppb | 5 Max. | ATOMIC |
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.
Light Crude Oil
Properties | Unit | Spec 1 | Spec 2 | Test Method | |||||
---|---|---|---|---|---|---|---|---|---|
Sp. Gr. 15.6/15.6 °C | - | 0.8575 | 0.8488 | ASTM D 5002 | |||||
API Gravity | °API | 33.5 | 35.21 | ASTM D 5002 | |||||
Sulfur content | %Wt | 1.45 | 1.69 | ASTM D 4294 | |||||
H2S Content | ppm | 61 | 15 | IP 570 | |||||
Mercaptan Content | ppm | 118 | 243 | UOP 163 | |||||
Nitrogen Content | %Wt | 0.18 | 0.08 | ASTM D 5762 | |||||
Water & Sediment | %Vol | < 0.05 | < 0.05 | ASTM D 4007 | |||||
Water Content | %Vol | < 0.025 | < 0.025 | ASTM D 4006 | |||||
Salt Content | PTB | 9 | 4 | ASTM D 3230 | |||||
Kinematic Viscosity @10°C | mm²/s | 16.51 | 11.02 | ASTM D 445 | |||||
Kinematic Viscosity @20°C | mm²/s | 10.78 | 7.51 | ASTM D 445 | |||||
Kinematic Viscosity @40°C | mm²/s | 5.735 | 4.4 | ASTM D 445 | |||||
Pour Point | oC | -9 | -30 | ASTM D 5853 | |||||
RVP | psi | 8.15 | 8.5 | ASTM D 3230 | |||||
Asphaltene Content | %Wt | 1.3 | 1.1 | IP 143 | |||||
Wax Content | %Wt | 6.2 | 6.7 | BP 237 | |||||
Drop Melting Point of Wax | oC | 54 | 52 | IP 133 | |||||
CCR | %Wt | 4.24 | 3.4 | ASTM D 189 | |||||
Total Acid Number | mgKOH/g | 0.1 | <0.05 | UOP 163 | |||||
Nickel Content | ppm | 8 | 5 | ASTM D 5863 | |||||
Vanadium Content | ppm | 41 | 11 | ASTM D 5863 | |||||
Iron Content | ppm | 1 | 1 | ASTM D 5863 | |||||
Lead Content | ppm | < 1 | <1 | ASTM D 5863 | |||||
Sodium Content | ppm | 7 | 3 | ASTM D 5863 | |||||
Zinc Content | ppm | < 1 | <1 | ASTM D 5863 | |||||
Copper Content | ppm | < 1 | <1 | ASTM D 5863 |
Heavy Crude Oil
Properties | Unit | Spec 1 | Spec 2 | Test Method | |||||
---|---|---|---|---|---|---|---|---|---|
Sp. Gr. 15.6/15.6 oC | - | 0.875 | 0.941 | ASTM D 5002 | |||||
API Gravity | oAPI | 30.2 | 18.87 | ASTM D 5002 | |||||
Sulfur content | %Wt | 1.92 | 3.95 | ASTM D 4294 | |||||
H2S Content | ppm | 121 | <1 | IP 570 | |||||
Mercaptan Content | ppm | 185 | 25 | UOP 163 | |||||
Nitrogen Content | %Wt | 0.23 | 0.19 | ASTM D 5762 | |||||
Water & Sediment | %Vol | < 0.05 | 0.05 | ASTM D 4007 | |||||
Water Content | %Vol | < 0.025 | 0.05 | ASTM D 4006 | |||||
Salt Content | PTB | 10 | 25 | ASTM D 3230 | |||||
Kinematic Viscosity @10oC | mm²/s | 29.07 | 1610 | ASTM D 445 | |||||
Kinematic Viscosity @20oC | mm²/s | 18.4 | 607.7 | ASTM D 445 | |||||
Kinematic Viscosity @40oC | mm²/s | 9.218 | 179.7 | ASTM D 445 | |||||
Pour Point | oC | -12 | -27 | ASTM D 5853 | |||||
RVP | psi | 6.25 | 3.5 | ASTM D 3230 | |||||
Asphaltene Content | %Wt | 3.4 | 8.9 | IP 143 | |||||
Wax Content | %Wt | 5.7 | 4.1 | BP 237 | |||||
Drop Melting Point of Wax | oC | 55 | 64 | IP 133 | |||||
CCR | %Wt | 6.2 | 12.4 | ASTM D 189 | |||||
Total Acid Number | mgKOH/g | 0.15 | 0.7 | UOP 163 | |||||
Nickel Content | ppm | 14 | 30 | ASTM D 5863 | |||||
Vanadium Content | ppm | 73 | 116 | ASTM D 5863 | |||||
Iron Content | ppm | <1 | 2 | ASTM D 5863 | |||||
Lead Content | ppm | <1 | <1 | ASTM D 5863 | |||||
Sodium Content | ppm | 5 | 13 | ASTM D 5863 | |||||
Zinc Content | ppm | <1 | <1 | ASTM D 5863 | |||||
Copper Content | ppm | <1 | <1 | ASTM D 5863 |
Iraq Light Crude Oil
Properties | Unit | Specification | Test Method | |||||||
---|---|---|---|---|---|---|---|---|---|---|
Density at 15oC | kg/L | 0.9011 | ASTM D 1298 | |||||||
API Gravity at 60f | °API | 25.44 | ASTM D 287 | |||||||
Water by Distillation | %Vol | 0.05 | ASTM D 4006 | |||||||
Sediment by Extraction | %Wt | 0.015 | ASTM D 473 | |||||||
Sulfur | %Wt | 3.705 | IP336 | |||||||
Pour Point | °C | ASTM D5853 | ||||||||
Salt Content | lb/1000bbl | 4.6 | ASTM D3230 | |||||||
Water KF | %Wt | 1053 | ASTM D4928 | |||||||
H2S Content | ppm | 0.63 | UOP 163 | |||||||
Acidity | mgKOH/g | 0.075 | ASTM D664 | |||||||
Mercaptan Sulfur | ppm | 88.9 | ASTM D3227 | |||||||
Kinematic Viscosity at 50°C | cSt | 11.5581 | ASTM D445 | |||||||
Asphalthenes | %Wt | 5.5 | IP143 | |||||||
IBP | oC | 48 | ASTM D86 | |||||||
Distillation at 5% | oC | 82 | ASTM D86 | |||||||
Distillation at 10% | oC | 108 | ASTM D86 | |||||||
Distillation at 20% | oC | 169 | ASTM D86 | |||||||
Distillation at 30% | oC | 231 | ASTM D86 | |||||||
Distillation at 40% | oC | 282 | ASTM D86 | |||||||
Distillation at 50% | oC | 317 | ASTM D86 | |||||||
Distillation at 60% | oC | 332 | ASTM D86 | |||||||
Distillation at 70% | oC | 339 | ASTM D86 | |||||||
Distillation at 80% | oC | 350 | ASTM D86 | |||||||
Distillation at 89% | oC | 353 | ASTM D86 | |||||||
FBP | oC | 355 | ASTM D86 |
Iraq Heavy Crude Oil Assays
Properties | Unit | T-1A | T-2 | T-4 | Test Method | ||||
---|---|---|---|---|---|---|---|---|---|
Density @15oC | kg/L | 0.9097 | 0.9153 | 0.9135 | ASTM D 5002 | ||||
Sp. Gr. @ 15.6/15.6oC | 0.9102 | 0.9158 | 0.914 | Conversion | |||||
API Gr. @15.6oC | °API | 23.96 | 23.01 | 23.31 | Calculated | ||||
Sulfur Content | %Wt | 3.34 | 3.34 | 3.25 | ASTM D 4294 | ||||
Carbon Residue, Micro | %Wt | 7.65 | 8.31 | 8.74 | ASTM D 4530 | ||||
Bottom Sediment & Water | %Vol | 0.1 | 1.35 | 0.6 | ASTM D 4007 | ||||
Salt as NaCl | mg/L | 5.04 | 15 | 6.3 | ASTM D 3230 | ||||
Ash Content @550oC | %Wt | 0.013 | 0.049 | 0.012 | ASTM D 482 | ||||
Total Nitrogen | ppm | 0.14 | 0.13 | ASTM D 5762-01 | |||||
Copper | ppm | <1 | <1 | <1 | IP 501 (Mod.) | ||||
Iron | ppm | 1 | 1 | <1 | IP 501 (Mod.) | ||||
Nickel | ppm | 12 | 13 | 12 | IP 501 (Mod.) | ||||
Vanadium | ppm | 36 | 37 | 36 | IP 501 (Mod.) | ||||
Lead | ppm | <1 | <1 | <1 | IP 501 (Mod.) | ||||
Chromium | ppm | <1 | <1 | <1 | IP 501 (Mod.) | ||||
Zinc | ppm | <1 | 1 | <1 | IP 501 (Mod.) | ||||
Calcium | ppm | 5 | 63 | 1 | IP 501 (Mod.) | ||||
Magnesium | ppm | 1 | <1 | <1 | IP 501 (Mod.) | ||||
Sodium | ppm | 1 | 5 | <1 | IP 501 (Mod.) | ||||
Total Acid Number | mgKOH/g | 0.302 | 0.026 | 0.748 | ASTM D 664 | ||||
Vapor Pressure (DVPE) | kPa | 11.2 | 20.7 | 6.6 | ASTM D 5191 | ||||
Pour Point (max/Upper) | oC | -39 | -24 | < -42 | ASTM D 5853 | ||||
Pour Point (min/Upper) | oC | < -42 | < -42 | ASTM D 5853 | |||||
Flash Point | oC | < -5 | < -5 | < -5 | ASTM D 93 (Mod.) | ||||
Asphaltenes | %Wt | 5.2 | 4.82 | 5.5 | ASTM D 3279 | ||||
Wax Content | %Wt | 0.5 | 0.7 max | UOP 46 | |||||
Kinematic Viscosity @26.7oC | cSt | 31.03 | 40.11 | 31.97 | ASTM D 445 | ||||
Kinematic Viscosity @37.8oC | cSt | 19.32 | 25.09 | 19.55 | ASTM D 446 |