Riyadh, Saudi Arabia
Riyadh, Saudi Arabia

SABIC is a diversified manufacturing company, active in chemicals and intermediates, industrial polymers, fertilizers, and metals. It is the largest public company in Saudi Arabia, as listed in Tadawul, but the Saudi government still owns 70% of its shares. SABIC is also the largest listed company in the Middle East. Private shareholders are from Saudi Arabia and other countries of the six-nation Gulf Cooperation Council .SABIC was the world's fourth largest chemical producer in 2013. It is currently the second largest global ethylene glycol producer and is expected to top the list after the introduction of new projects. SABIC is the third largest polyethylene manufacturer, the fourth largest polyolefins manufacturer, and the fourth largest polypropylene manufacturer. SABIC is also the world’s largest producer of mono-ethylene glycol, MTBE, granular urea, polycarbonate, polyphenylene and polyether imide.In 2014, SABIC was ranked fourth in the world among chemical companies by Fortune Global 500, and the world’s 205th largest corporation. In 2010, SABIC grew to be the second largest diversified chemical company, or first when measured only by asset value. Measured over all its branches, it became the world's 98th largest corporation on the Forbes Global 2000 ranking , with sales revenues of $50.4 billion, profits of $6.7 billion and assets standing at $90.4 billion.The company is based in Riyadh and has interests in 17 affiliated companies, which range from full ownership to significant partial participation. Wikipedia.


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A coated fertilizer comprises a fertilizer granule; and a coating disposed on a surface of the fertilizer granule, wherein the coating comprises a poly(lactic acid); a second polymer comprising a poly(butylene succinate), a cellulose triacetate, or a combination comprising at least one of the foregoing; and a sealant. Methods of making the coated fertilizer are also disclosed.


Patent
Saudi Basic Industries Corporation and Sabic | Date: 2017-01-04

The present invention relates to a process for the preparation of a feedstock for a hydroprocessing unit, wherein said feedstock is based on crude oil containing asphaltenes, said process comprising the steps of: mixing said crude oil with a solvent, wherein said solvent is at least one member chosen from the group of steam cracker cracked distillate (CD), steam cracker carbon black oil (CBO), low asphaltenes containing crude oil residue having a boiling point above 300 deg C and aromatic rich hydrocarbons streams, wherein a mixing ratio solvent: crude oil is such that no aggregation of asphaltenes in said combined mixture of solvent and crude oil takes place under mixing conditions; feeding said combined mixture of solvent and crude oil to one or more hydroprocessing units.


Patent
Sabic | Date: 2017-04-05

Methods and systems for managing a decomposition process are disclosed. An example method can comprise estimating a coking rate for a process based on a coking model. The coking model can comprise a pyrolytic coking term and a catalytic coking term. An example method can comprise, performing at least a portion of the process, receiving a parameter for the process, and adjusting an operation of the process based on the parameter.


Patent
Saudi Basic Industries Corporation and Sabic | Date: 2017-01-04

The present invention relates to an integrated hydrocracking process for production of olefinic and aromatic petrochemicals from a hydrocarbon feedstock comprising crude oil. An object of the present invention is to provide an integrated hydrocracking process for production of olefinic and aromatic petrochemicals from a hydrocarbon feedstock comprising crude oil wherein the portion of the crude oil converted to LPG is increased significantly.


A method for producing C2+ hydrocarbons and H2 comprising (a) introducing to a reactor a reactant mixture comprising methane, (b) heating the reactant mixture to a preheating temperature to yield a heated mixture, (c) generating free radicals in the heated mixture to form a primary effluent mixture comprising free radicals, C2+ hydrocarbons, H2, and unreacted methane, (d) reacting the primary effluent mixture in a secondary reaction zone to form a secondary effluent mixture comprising C2+ hydrocarbons, H2, free radicals, and unreacted methane, at a secondary reaction zone temperature that is greater than the preheating temperature, wherein a free radicals amount in the primary effluent mixture is greater than a free radicals amount in the secondary effluent mixture, (e) cooling the secondary effluent mixture to a quench temperature lower than the secondary reaction zone temperature to yield a product mixture comprising C2+ hydrocarbons and H2, and (f) recovering the product mixture.


Patent
Saudi Basic Industries Corporation and Sabic | Date: 2017-01-04

The present invention relates to a process for converting a high- boiling hydrocarbon feedstock into lighter boiling hydrocarbon products, said lighter boiling hydrocarbon products being suitable as a feedstock for petrochemicals processes, said converting process comprising the following steps of: feeding a heavy hydrocarbon feedstock to a cascade of hydrocracking unit(s), cracking said feedstock in a hydrocracking unit, separating said cracked feedstock into a stream comprising hydrogen, a stream comprising a light boiling hydrocarbon fraction and a bottom stream comprising a heavier hydrocarbon fraction feeding said bottom stream of such a hydrocracking unit as a feedstock for a subsequent hydrocracking unit in said cascade of hydrocracking unit(s), wherein the process conditions in each hydrocracking unit(s) are different from each other, in which the hydrocracking conditions from the first to the subsequent hydrocracking unit(s) increase from least severe to most severe, and sending the light boiling hydrocarbon fractions from each hydrocracking unit(s) to petrochemicals processes.


A method of forming a three dimensional object comprising: depositing a layer of thermoplastic polymeric material in a preset pattern on a platform (14) to form a deposited layer (50); directing an energy source (54), via an energy beam at an energy source target area (56) on the deposited layer (50) to increase the surface energy of the deposited layer at the energy source target area; contacting the energy source target area (56) with a subsequent layer (52) wherein the subsequent layer (52) is deposited along a path of the preset pattern; wherein directing an energy source (54) at the energy source target area (56) comprises applying energy to the layer at an area preceding the depositing of the subsequent layer to that area; and repeating the preceding steps to form the three dimensional object.


Patent
Sabic | Date: 2017-02-22

Polycarbonate blend compositions are disclosed. The compositions include at least one polycarbonate useful for high heat applications. The compositions can include one or more additional polymers. The compositions can include one or more additives. The compositions can be used to prepare articles of manufacture, and in particular, automotive bezels.


In various aspects, the disclosure relates to thermally conductive thermoplastic compositions comprising a polymer matrix, an impact modifier composition having a chemically reactive impact modifier, and, optionally, a chemically non-reative impact modifier, and a thermally conductive filler. The disclosed thermally conductive thermoplastic compositions exhibitgood thermal conductivity and improved impact and ductile properties.


Patent
Saudi Basic Industries Corporation and Sabic | Date: 2017-01-11

The invention relates to a process for the preparation of ethylene -olefin copolymers by copolymerizing ethylene with -olefins in the presence of a catalyst formed by contacting metallocene complex with a cocatalyst, wherein the metallocene complex is chosen from the group consisting of a metallocene complex according to formula I or a metallocene complex according to formula II, wherein M is chosen from the group of Ti, Zr and Hf; Q is halogen (F, CI, Br, I) or an alkyl group comprising 1 to 20 carbon atoms; k is the number of Q groups, is an integer and equals the valence of M minus 2; and wherein R1, R2, R3 and R4 are identical or different and can be chosen from alkyl groups with 1-20 carbon atoms, more preferably R1, R2, R3 and R4 are identical or different and are chosen from methyl or ethyl groups, most preferably R1, R2, R3 and R4 are methyl groups.

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