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Gasolines

Pyrolysis gasolineorPygasis 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 isa 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.

Properties Unit Specification Test Method
Density @20 °C 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 °C 35 Min ASTM D 86
FBP °C 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 °C 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 °C 35 Min ASTM D 86
FBP °C 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 @15°C 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 @ 37.8°C 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 °C 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 °C 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 °C 38 Report ASTM D 86
FBP °C 185 Report ASTM D 86
5% Vol Recovered °C 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 °C 34 Min. ASTM D 86
FBP °C 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
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Naphtha

Naphtha

Naphthais a general term that has been used for over two thousand years to refer to flammable liquid hydrocarbon mixtures. Mixtures labelled naphtha have been produced from natural gas condensates, petroleum distillates, and the distillation of coal tar and peat. It is used diversely in different industries and regions to refer to gross products like crude oil or refined products such as kerosene. According to boiling points, Lightnaphthais the fraction boiling between 30C and 90C and consists of molecules with 56 carbon atoms.Heavy naphthaboils between 90C and 200C and consists of molecules with 612 carbons. Based on hydrocarbon structure, Light is a mixture consisting mainly of straight-chained and cyclic aliphatic hydrocarbons having from five to nine carbon atoms per molecule.Heavyis a mixture consisting mainly of straight-chained and cyclic aliphatic hydrocarbons having from seven to nine carbons per molecule

Properties Unit Specification Test Method
Density@ 20 °C g/ml 0.73 – 0.76 ASTM D 1298
Lead Content ppb 10 Max A.A
IBP °C 60 Min ASTM D 86
FBP °C 180 Max ASTM D 86
Paraffinic & Naphthenic %Wt 70 Min G.C
Aromatic %Wt 30 Max G.C
Total Sulfur ppm 1700 Max ASTM D 4294
Color   Clear – Light Yellow Visual
RON   75 Min Infrared

Heavy Naphtha

Properties Unit Specification Test Method
IBP °C 165 -179 ASTM D-86
10% °C 177-186 ASTM D-86
30% °C 182-194 ASTM D-87
50% °C 190-205 ASTM D-88
90% °C 250-280 ASTM D-89
FBP °C 297-330 ASTM D-90
Total Sulfur ppm (wt) 1400 Max. ASTM D-3120
Color ASTM 2.0 Max. ASTM D-1500
Flash point °C 58 Min. ASTM D-93
Density @ 15 °C g/ml 0.7800 – 0.8400 ASTM D-4052
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Base Oils

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
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High-density Polyethylene

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.

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Urea Granular

Urea Granular

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
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  • Abdul Mohsin (Gem Polymer Petrochemicals LLC)
  • JAFZA, Dubai - 000, United Arab Emirates
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