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51 results about "Propylbenzene" patented technology

Propylbenzene may refer to: Cumene n-Propylbenzene

Anti-corrosion coating capable of emitting aromatic odor for glass door and preparation method of anti-corrosion coating

The invention discloses an anti-corrosion coating capable of emitting aromatic odor for a glass door. The anti-corrosion coating is characterized by being prepared from the following raw materials in parts by weight: 46-52 parts of a transparent polyurethane emulsion, 1-2 parts of a polyethylene wax emulsion, 20-24 parts of a modified styrene-acrylic emulsion, 1-3 parts of methoxy-1-methylethylacetate, 0.2-0.5 part of propanediol butyl ether bi(2-octyloxy pyrophosphate-yl) ethylene titanate, 0.2-0.4 part of a polyacrylate flatting agent, 1-2 parts of ethyl acetate, 0.2-0.3 part of ethyecellulose, 0.2-0.5 part of polyether-modified polyethylene organic siloxane, 0.3-0.6 part of propyl triethoxy siloxane, 0.3-0.7 part of menthyl acetate, 0.2-0.5 part of polyoxyethylene oleate, 0.3-0.5 part of phenoxyaethanol, 1-3 parts of a pigment, 1-2 parts of nano ceramic powder and 10-15 parts of deionized water. The water-based coating disclosed by the invention has excellent water resistance, rot resistance and adhesive force, also has fresh aromatic odor, and is refreshing; the coating has the effects of sterilizing, preventing dust, resisting static electricity and the like due to the added modified styrene-acrylic emulsion; and the quality of the coating is further improved.
Owner:凤阳徽亨商贸有限公司

Anticorrosive anti-yellowing coating for glass door and preparation method of coating

The invention discloses an anticorrosive anti-yellowing coating for a glass door. The coating is characterized by being prepared from the following raw materials in parts by weight: 8 to 12 parts of water-based vinyl polyurethane, 30 to 35 parts of amino resin emulsion, 0.1 to 0.3 part of water-based silane coupling agent KH460, 26 to 32 parts of modified styrene-acrylic emulsion, 1 to 3 parts of dipropylene glycol dimethyl ether, 0.3 to 0.5 part of alcohol amine alkoxy titanate ester, 0.2 to 0.4 part of fluoro-alkyl polyether modified polysiloxane, 0.1 to 0.3 part of lauroyl diethanolamide, 0.2 to 0.3 part of white oil, 0.2 to 0.4 part of polyoxyethylene sorbitan monooleate, 0.1 to 0.2 part of ammonium polyphosphate, 0.3 to 0.7 part of ethylparaben, 0.2 to 0.5 part of glycerin, 0.3 to 0.6 part of quartz powder, 1 to 3 parts of pigment and 10 to 15 parts of deionized water. The sterilization, the dust prevention, the anti-static performance and the like of the coating are improved due to the added modified styrene-acrylic emulsion; the coating has the functions of sterilization and anticorrosion due to the added ethylparaben; and on the basis of water resistance, acid resistance and an excellent adhesive force of the water-based coating, the water-based coating is also good in weatherability, aging resistance and anticorrosion.
Owner:凤阳徽亨商贸有限公司

Separation process for producing ethylbenzene and/or propylbenzene product from gas containing ethylene and/or propylene by gas phase process

The invention belongs to the field of petrochemical industry and discloses a separation process for producing an ethylbenzene and/or propylbenzene product from gas containing ethylene and/or propylene by a gas phase process. The separation process comprises the following steps: 1) feeding alkylation reaction products getting out of an alkylation reactor and anti-alkylation reaction products getting out of an anti-alkylation reactor into a benzene tower respectively or after mixing; 2) feeding gas-phase materials at the top of the benzene tower after separation into an absorption tower after the gas-phase materials are drawn out of the tower top of the benzene tower; 3) drawing out liquid-phase materials at the upper part of the benzene tower after separation from the tower top or the side of the benzene tower and then returning the liquid-phase materials into the reaction part; and 4) performing corresponding separation on the materials at the tower bottom of the benzene tower by a subsequent separation tower to obtain several or all of methylbenzene, ethylbenzene, propylbenzene, diethylbenzene and high-boiling residues. By adopting the separation process disclosed by the invention, by directly bringing heat of the reaction products, including reaction heat, into the benzene tower, the heat supply at the tower bottom of the benzene tower is reduced and the energy consumption is reduced; and the utilization of the heat is reasonable. By adopting the separation process disclosed by the invention, the number of the towers required for separation is not increased, and indirect heat exchange equipment is reduced.
Owner:LUOYANG PETROCHEMICAL ENG CORP SINOPEC +1

A gas-phase process for the separation of ethylbenzene and/or propylbenzene from gas containing ethylene and/or propylene

The invention belongs to the field of petrochemical industry. The invention discloses a process for separating ethylbenzene and / or propylbenzene products from gas containing ethylene and / or propylene by gas phase method, which comprises the following steps: 1) alkylation reaction from an alkylation reactor The product and the anti-alkylation reaction product from the anti-alkylation reactor enter the benzene tower separately or after being mixed; 2) the separated benzene tower top gas phase material enters the absorption tower after being extracted from the benzene tower top; 3) the separated The liquid phase material in the upper part of the benzene tower is withdrawn from the top or side of the benzene tower and then returned to the reaction part; 4) The bottom material of the benzene tower is separated from toluene, ethylbenzene, propylbenzene, diethylbenzene, and high-boiling substances through the subsequent separation tower. some or all of them. By adopting the present invention, by directly bringing the heat of the reaction product including the reaction heat into the benzene tower, the heat supply at the bottom of the benzene tower is reduced, and the energy consumption is reduced; the heat utilization is reasonable. Adopting the present invention does not increase the number of towers required for separation, and reduces the equipment for indirect heat exchange.
Owner:SINOPEC LUOYANG PETROCHEM ENG CORP +1

Preparation method and application of catalyst for producing mixed propylbenzene through alkylation of benzene and C4 olefin

The preparation method of the catalyst comprises the following steps: mixing at least one zeolite with a binder, adding water and a peptizing agent, kneading, extruding and molding, and then sequentially drying and roasting, finally, the roasted catalyst is subjected to metal or nonmetal oxide modification through an impregnation method, and the required catalyst is obtained. According to the present invention, benzene and C4 olefin are adopted as reaction raw materials, the catalyst obtained by using the preparation method is adopted to catalyze the reaction of benzene and butene so as to generate the target product mixed propylbenzene, the reaction can be performed under the mild reaction condition, the reaction speed is high, and the olefin conversion rate is high. Through measurement, under the conditions that the reaction temperature is 360 DEG C, the reaction pressure is 0.8 MPa, the total weight hourly space velocity is 5.0 h <-1 > and the molar ratio of benzene to alkene is 5.5: 1, the conversion rate of C4 olefin reaches 99.8%, the selectivity of the product mixed propylbenzene reaches 72.6%, the proportion of isopropyl benzene in the mixed propylbenzene is 52.69%, and the proportion of n-propylbenzene in the mixed propylbenzene is 47.31%.
Owner:洛阳市科创石化科技开发有限公司
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