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Base oilsare used to manufacture products including lubricating greases, motor oil and metal processing fluids. Different products require different compositions and properties in the oil. One of the most important factors is the liquids viscosity at various temperatures.
Group Iconsists of conventional petroleum base oils. API defines group I as base stocks contain less than 90 percent saturates and/or greater than 0.03 percent sulfur and have a viscosity index greater than or equal to 80 and less than 120.
Group II arebase stocks contain greater than or equal to 90 percent saturates and less than or equal to 0.03 percent sulfur and have a viscosity index greater than or equal to 80 and less than 120.
Group III arebase stocks contain greater than or equal to 90 percent saturates and less than or equal to 0.03 percent sulfur and have a viscosity index greater than or equal to 120. This group may be described as Synthetic Technology oils or Hydro-Cracked Synthetic oil. However, some oil companies may call their products under this group as synthetic oil.
Group IV consists of synthetic oils made of Poly-alpha-olefins. PAO oils are much more stable in extreme temperatures, which make much more suitable for use in very cold weather as well as very hot weather.
Group V are any type of base oil other than mentioned in the previously defined groups. They include, among others, naphthenic oils and esters.
Properties | Unit | Min. | Typical | Max. | Test Method |
Kinematic Viscosity @40°C | cSt | – | 38 | – | ASTM D 445 |
Kinematic Viscosity @100°C | cSt | 4.6 | – | 5.6 | ASTM D 445 |
Viscosity Index | 100 | – | – | ASTM D 2270 | |
Flash Point (COC) | °C | 190 | – | – | ASTM D 92 |
Pour Point | °C | – | – | -6 | ASTM D 97 |
CCR | %Wt | – | 0.06 | – | ASTM D 189 |
Total Acidity | mgKOH/g | – | – | 0.05 | ASTM D 664 |
Demulsibility | – | Pass | – | ASTM D 1401 | |
Sulfur Content | %Wt | 0.15 | – | 0.6 | ASTM D 1552 |
Color | – | 0.5 | 1 | ASTM D 1500 | |
Density @15°C | kg/m³ | – | 875 | – | ASTM D 1298 |
Copper Corrosion, 3 hrs @100°C | – | – | 1A | ASTM D 130 | |
Foam | ml | – | Nil | – | ASTM D 892 |
Base Oil SN350
Properties | Unit | Min. | Typical | Max. | Test Method |
Kinematic Viscosity @40°C | cSt | – | 75 | – | ASTM D 445 |
Kinematic Viscosity @100°C | cSt | 8.3 | – | 9.3 | ASTM D 445 |
Viscosity Index | 95 | – | – | ASTM D 2270 | |
Flash Point (COC) | °C | 220 | – | – | ASTM D 92 |
Pour Point | °C | – | – | -6 | ASTM D 97 |
CCR | %Wt | – | 0.06 | – | ASTM D 189 |
Total Acidity | mgKOH/g | – | – | 0.05 | ASTM D 664 |
Demulsibility | – | Pass | – | ASTM D 1401 | |
Sulfur Content | %Wt | 0.15 | – | 0.6 | ASTM D 1552 |
Color | – | 2 | 1 | ASTM D 1500 | |
Density @15°C | kg/m³ | – | 880 | – | ASTM D 1298 |
Copper Corrosion, 3 hrs @100°C | – | – | 1A | ASTM D 130 | |
Foam | ml | – | Nil | – | ASTM D 892 |
Base Oil SN500
Properties | Unit | Min. | Typical | Max. | Test Method |
Kinematic Viscosity @40°C | cSt | – | 96 | – | ASTM D 445 |
Kinematic Viscosity @100°C | cSt | 10 | – | 11.5 | ASTM D 445 |
Viscosity Index | 95 | – | – | ASTM D 2270 | |
Flash Point (COC) | °C | 230 | – | – | ASTM D 92 |
Pour Point | °C | – | – | -6 | ASTM D 97 |
CCR | %Wt | – | 0.08 | 0.15 | ASTM D 189 |
Total Acidity | mgKOH/g | – | – | 0.05 | ASTM D 664 |
Demulsibility | – | Pass | – | ASTM D 1401 | |
Sulfur Content | %Wt | – | 0.7 | – | ASTM D 1552 |
Color | – | 2.5 | – | ASTM D 1500 | |
Density @15°C | kg/m³ | – | 885 | – | ASTM D 1298 |
Copper Corrosion, 3 hrs@100°C | – | Nil | – | ASTM D 130 | |
Foam | ml | – | Nil | – | ASTM D 892 |
Base Oil SN600
Properties | Unit | Specification |
Sp. Gr. @15.5°C | 0.8850-0.8950 | |
Color | 3.0 Max | |
Pour Point | °C | (-3) Max |
Flash Point | °C | 225 min |
Kinematic Viscosity @40°C | cSt | To be reported |
Kinematic Viscosity @100°C | cSt | 12.5 – 13.5 |
Viscosity Index | 90 min |
Condensateis a generic term that many use to describe a variety of light petroleum streams that range from NGLs to light crude oil. Strictly speaking, a condensate is a mixture of hydrocarbons that exists in a gaseous state in an underground gas reservoir but condenses under atmospheric conditions.
Raffinateis a product which has had a component or components removed. The product containing the removed materials is referred to as the extract. For example, in solvent extraction, the raffinate is the liquid stream which remains after solutes from the original liquid are removed through contact with an immiscible liquid. In metallurgy, raffinating refers to a process in which impurities are removed from liquid material.
Properties | Unit | Specification | Test Method |
1,3-Butadiene | %Wt | 47-53 | AN-JG-NO.1 |
1 & I-Butene | %Wt | 43 MAX | AN-JG-NO.1 |
N & I-Butane | %Wt | 2.7 MAX | AN-JG-NO.1 |
Methyl Acetylene | %Wt | 0.14 MAX | AN-JG-NO.1 |
Ethyl Acetylene | %Wt | 0.55 MAX | AN-JG-NO.1 |
Vinyl Acetylene | %Wt | 2.05 MAX | AN-JG-NO.1 |
1,2 – Butadiene | %Wt | 0.5 MAX | AN-JG-NO.1 |
Trans- 2 – Butene | %Wt | 3.5 MAX | AN-JG-NO.1 |
Cis -2- Butene | %Wt | 4.5 MAX | AN-JG-NO.1 |
C-5 | %Wt | 0.3 MAX | AN-JG-NO.1 |
C6-cut
Properties | Unit | Specification | Test Method |
Benzene | %WT | 80 Min. | By GC |
DN Value | gl2/100g | 2 Max. | UOP 326 |
Butene-1
Properties | Unit | Specification |
Purity | %Wt | 99 Min |
Carbon Monoxide | ppm (vol) | 1 Max |
Carbon Dioxide | ppm (vol) | 2 Max |
Ethane | ppm (vol) | 600 Max |
Ethylene | ppm (vol) | 500 Max |
Other Butenes or Butanes | ppm (vol) | 10000 Max |
C6 (Not Cyclic) | ppm (vol) | 50 Max |
Raffinate
Properties | Unit | Specification | Test Method |
RVP | psia | Max 11 | ASTM D 323 |
IBP | °C | Min 30 | ASTM D 86 |
FBP | °C | Max 130 | ASTM D 86 |
Paraffinic | %Wt | Min 70 | GC |
Olefin | %Wt | Max 14 | GC |
Density @15.6°C | kg/m3 | 650-740 | ASTM D 4052 |
Total Sulfur | ppm (wt) | Max 1.5 | ASTM D 5453 |
Color | Saybolt | Min +18 | ASTM D 156 |
Lead | ppb (wt) | Max 5 | GFAAS |
Aromatic Raffinate
Properties | Unit | Specification | Test Method |
Density @20°C | g/ml | 0.84 Min | ASTM D 1298 |
IBP | °C | 60 Min | ASTM D 86 |
FBP | °C | 200 Max | ASTM D 86 |
Total Sulfur | ppm | 500 Max | ASTM D 4294 |
Color | Clear & Light Yellow | Visual | |
Aromatic | %Wt | 60 Min | GC |
Benzene | %Wt | 10 Max | GC |
Toluene & Xylene | %Wt | 45 Min | GC |
Butane-Butene Raffinate (BBR)
Properties | Unit | Specification | Test Method |
I-Butene | %Wt | 65 Min | ASTM D 2426 |
1-Butene | %Wt | 20 Max | ASTM D 2426 |
N & I Butane | %Wt | 4.96 max | ASTM D 2426 |
C3 Cut | %Wt | 0.23 Max | ASTM D 2426 |
Trans-2- Butene | %Wt | 7.48 Max | ASTM D 2426 |
Cis-2-Butene | %Wt | 3.03 Max | ASTM D 2426 |
1, 3 Butadiene | %Wt | 0.3 Max | ASTM D 2426 |
Condensates
Properties | Unit | Specification | Test Method |
Sp. Gr. 15.6/15.6 °C | 0.7228 | ASTM D 4052 | |
API Gravity | °API | 64.3 | ASTM D 1298 |
Sulfur Content | %Wt | 0.03 | ASTM D 4294 |
Mercaptan Content | ppm | 144 | UOP 163 |
H2S Content | ppm | <1 | UOP 163 |
Water Content | ppm | 104 | ASTM D 4928 |
Nitrogen Content | ppm | <10 | ASTM D 5762 |
Saturate Content | %Vol | 91.2 | ASTM D 1319 |
Olefin Content | %Vol | 0.7 | ASTM D 1319 |
Aromatic Content | %Vol | 8.17 | ASTM D 1319 |
Kinematic Viscosity @0°C | %Vol | 0.8897 | ASTM D 445 |
Kinematic Viscosity @10°C | mm²/s | 0.7272 | ASTM D 445 |
Kinematic Viscosity @20°C | mm²/s | 0.6745 | ASTM D 445 |
Pour Point | °C | <-39 | ASTM D 97 |
RVP | psi | 7.55 | ASTM D 323 |
Cold Filter Plugging Point | °C | <-32 | IP 309 |
Wax Content | %Wt | 0.03 | BP 237 |
Drop Melting Point of Wax | °C | <1 | IP 133 |
Copper Corrosion, 3hrs @ 50°C | 1b | ASTM D 130 | |
Total Acidity | mgKOH/g | <1 | ASTM D 664 |
Aniline Point | °C | 57 | ASTM D 611 |
Molecular Weight | 138 | Osmomat | |
Color | Saybolt | 30 | ASTM D 156 |
Lead Content | ppm | <1 | ASTM D 5863 |
Asphalt, also known asbitumenis 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).
Properties | Unit | Bitumen 40/50 | Bitumen 60/70 | Bitumen 85/100 | Test Method |
Sp. Gr. @25/25°C | 1.01/1.06 | 1.01/1.06 | 1.00/1.05 | ASTM D 70 | |
Penetration @25°C | 40/50 | 60/70 | 85/100 | ASTM D 5762 | |
Softening Point | °C | 52/60 | 49/56 | 45/52 | ASTM D 36 |
Ductility @25°C | 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 | °C | 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 |
Paraffin waxis a white or colorless soft solid derivable from petroleum, coal or oil shale, that consists of a mixture of hydrocarbon molecules containing between twenty and forty carbon atoms. It is solid at room temperature and begins to melt above approximately 37C;its boiling point is 370C. Common applications for paraffin wax include lubrication, electrical insulation, and candles. In industrial applications, it is often useful to modify the crystal properties of the paraffin wax, typically by adding branching to the existing carbon backbone chain. The modification is usually done with additives, such as EVA copolymers, microcrystalline wax, or forms of polyethylene.
Slack waxeshave an oil content of from 5 to 30%, depending on the product. They are a welcome by-product of the production of lubricating oils. They can be productively employed in many industrial processes as they are; or they can be mixed, blended, or further refined. The melting points of slack wax varies from 41F to 66F. Some examples of applications for slack waxes: in wax emulsions, as binders and water-proofing in artificial woods; in matches; in jar candles; in rust-protection products; in industrial lubricants; in arena-footing; in soil or turf protection; and in fireplace products.
Properties | Unit | Light Grade | Light Heavy Grade | Heavy Grade |
Oil Content | %Wt. | 2 max | 3 max | 5 max |
Congealing Point | °C | 56-58 | 59-64 | 63-71 |
Viscosity @ 100°C | cSt | 3.87-4.36 | 4.6-6.5 | 6.5-8.1 |
Refractive Index | RI | 1.43 5 0 | 1.43 8 0 | 1.443 0 |
Slack Wax
Properties | Unit | Specification | Test Method |
Kinematic Viscosity @100°C | cSt | 7-9 | ASTM D 445 |
Congealing Point | °C | 65-68 | ASTM D 938 |
Density @15°C | kg/m³ | 830-850 | ASTM D 1298 |
Oil Content | RI | 30 max | ASTM D 721 |
Refractive Index @70°C | 1.4520 | ASTM D 2159 | |
Color | Brownish |
High-density polyethylene(HDPE) is a polyethylene thermoplastic made from petroleum. It is sometimes called alkathene or polythene when used for pipes. With a high strength-to-density ratio, HDPE is used in the production of plastic bottles, corrosion-resistant piping, geomembranes, and plastic lumber. HDPE is commonly recycled, and has the number 2 as its resin identification code.
Linear low-density polyethylene(LLDPE) is a substantially linear polymer, with significant numbers of short branches, commonly made by copolymerization of ethylene with longer-chain olefins. Linear low-density polyethylene differs structurally from conventional low-density polyethylene (LDPE) because of the absence of long chain branching. The linearity of LLDPE results from the different manufacturing processes of LLDPE and LDPE. In general, LLDPE is produced at lower temperatures and pressures by copolymerization of ethylene and such higher alpha-olefins as butene, hexene, or octene. The copolymerization process produces an LLDPE polymer that has a narrower molecular weight distribution than conventional LDPE and in combination with the linear structure, significantly different rheological properties.
Polypropylene(PP), also known aspolypropene, is a thermoplastic polymer used in a wide variety of applications including packaging and labeling, textiles (e.g., ropes, thermal underwear and carpets), stationery, plastic parts and reusable containers of various types, laboratory equipment, loudspeakers, automotive components, and polymer banknotes. An addition polymer made from the monomer propylene, it is rugged and unusually resistant to many chemical solvents, bases and acids.
Grade Name | MFR(gr/10min) (5kg,190OC) | Density | Application |
AM 5010 T2 N (EX3) | 0.45 | 0.945 | PE-80 Pressure pipe, e.g. drinking water and gas pipes, waste pipes and sewer pipes, their fittings and also sheets (natural grade). |
AM 5010 T2 B (EX3B) | 0.45 | 0.954 | PE-80 Pressure pipes, e.g. drinking water and gas pipes, waste pipes and sewer pipes, their fittings and also sheets (black grade) |
AM 5010 T3 N | 0.43 | 0.944 | High quality PE-80 pressure pipe for gas and water transportation (natural grade). |
AM 5010 T3 B | 0.43 | 0.954 | High quality PE-80 pressure pipe for gas and water transportation (black grade). |
AM CRP 100 N (PE – 100 W) | 0.22 | 0.948 | Top quality PE-100 pressure pipes for gas and water transportation at higher pressures or with thinner walls as PE-80(natural grade). |
AM CRP 100 B PE – 100 B | 0.22 | 0.957 | Leading PE-100 for pressure pipes for all purposes for gas, water and sewage transportation (black grade). |
AM CRP 100 Blue (PE – 100 Blue) |
0.22 | 0.948 | Leading PE-100, specially for drinking water (blue marker) |
Extrusion – Stretched Film and tape (Basell license)
Grade Name | MFR(gr/10min) (5kg,190OC) | Density | Application |
AF 7740 F (EX 1) | 1.6 | 0.944 | Stretched films and tapes for production of high quality knitted and woven. |
AF 7740 F2 (EX1 S) | 1.8 | 0.944 | Tapes to be used for agricultural packaging and as protective cover. |
Extrusion – Tubular film (Basell license)
Grade Name | MFR(gr/10min) (5kg,190OC) | Density | Application |
AM 9450 F (EX5) | 0.28 | 0.949 | For blown films with paper like quality, suitable for counter bags, carrier bags and wrapping films, excellent processing. |
AM 9450 F1 (EX5 HS) | 0.24 | 0.95 | For blown films with paper like quality, suitable for counter bags, carrier bags and wrapping films, excellent processing and sealability. |
AM 9455 F (EX4) | 0.28 | 0.956 | For blown films with paper like quality, suitable for counter bags, carrier bags and wrapping films, excellent processing stiffer than HM 9450 F. |
AM 9455 F1 (EX4 HS) | 0.24 | 0.957 | For blown films with paper like quality, suitable for counter bags, carrier bags and wrapping films, excellent processing, stiffer than HM9450 F1. |
AM 9445 HT (EX6 HT) | 0.18 | 0.944 | For blown films with paper like quality, suitable for counter bags, carrier bags and wrapping film, excellent processing with high tenacity. |
Extrusion – Filment (Basell license)
Grade Name | MFR(gr/10min) (5kg,190OC) | Density | Application |
AF 7750 M2 (EX2 S) | 3.3 | 0.956 | Monofilament for fishing notes, geo textiles and civil engineering. |
LPGhas 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.
Properties | Unit | Specification | Test Method |
Sp. Gr. 15.6/15.6°C | To be Reported | ASTM D 2598 | |
Vapor pressure @37.8°C | 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. 15.6/15.6°C | To be Reported | ASTM D 2598 | |
Vapor pressure @37.8°C | 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 |
Ureais the worlds most commonly used nitrogen fertilizer and indeed more urea is manufactured by mass than any other organic chemical. Containing 46% N, it is the most concentrated nitrogen fertilizer, and is readily available as free-flowing prills (granules). While over 90% of urea produced is used as a fertilizer, it has other uses, which include the manufacture of the melamine, used in melamine-methanal resins. Urea itself also forms important resins. An increasingly important use of urea is in reducing air pollution from diesel engines in cars, buses and lorries.
Properties | Unit | Specification | Test Method |
Nitrogen | %Wt | 2 max | AOAC (1995) Method 955.04 (2.4.03) |
Biuret | %Wt | Report | AOAC (1995) Method 960.04 (2.4.03) |
Moisture | %Wt | Report | AOAC (1995) Method 972.01 (2.2.03) |
Formaldehyde | %Wt | 50 | UKF SBB 0071-02-E,ED,2 (1982) |
Particle Size | 2.0-4.0 min by %Wt | 55 | IV-A TFI-1982 |