欧盟法规
统一分类与标签REACH注册ECHA物质ECHA物质工作场所安全标识要求化妆品禁用物质清单C&L通报食品接触材料-禁用CMR物质REACH预注册欧盟候选物质清单废弃物危险特性清单专利信息
专利号:WO-2004087313-A1
优先权日:2003-03-31
标题:Catalyst for synthesis of hydrocarbons from synthesis gas, process of preparation of catalyst
发明人:PANDULA SAMUEL; MAITY SUDIP; DASANDHI YOGESH CHANDRA; MUKHERJEE SOMNATH; MAITRA SANDIP KUMAR
权利人:COUNCIL SCIENT IND RES
摘要:The present invention relates to a catalyst useful in the synthesis of hydrocarbons from synthesis gas. The present invention also relates to a process for the preparation of a catalyst useful for the production of hydrocarbons from synthesis gas. The present invention particularly relates to preparation of a catalyst for production of wax from synthesis gas. The invention finds its usage in synthesising hydrocarbons, specifically wax, using Fisher-Tropsch Synthesis.
专利号:US-6410814-B2
优先权日:2000-04-04
标题 :Process for synthesis of lower isoparaffins from synthesis gas
发明人:FUJIMOTO KAORU; TSUBAKI NORITATSU
权利人:TOYOTA MOTOR CO LTD; GENESIS RES INST INC
摘要:A process for synthesis of lower isoparaffins from synthesis gas that is a mixture of hydrogen and carbon monoxide, wherein straight chain hydrocarbons are synthesized while isoparaffins and isoolefins are also produced through decomposition of hydrocarbons having a higher carbon number by use of a solid acid catalyst in the first stage, and isoparaffins are synthesized in the second stage. The straight chain hydrocarbons are produced by contacting the synthesis gas with a Fischer-Tropsch synthesis catalyst that is mixed with a solid acid catalyst for mainly hydrocracking long chain hydrocarbons. The isoparaffins are produced by contacting the straight chain hydrocarbons synthesized in the first stage, with a mixture of a hydrogenation catalyst for hydrogenating olefins and a solid acid catalyst for hydrocracking and isomerizing the straight chain hydrocarbons.
专利号:US-7615169-B2
优先权日:2004-09-20
标题 :Method for synthesis of colloidal nanoparticles
发明人:STROUSE GEOFFREY FIELDING; GERBEC JEFFREY A; MAGANA DONNY
权利人:UNIV CALIFORNIA
摘要:A method for synthesis of high quality colloidal nanoparticles using comprises a high heating rate process. Irradiation of single mode, high power, microwave is a particularly well suited technique to realize high quality semiconductor nanoparticles. The use of microwave radiation effectively automates the synthesis, and more importantly, permits the use of a continuous flow microwave reactor for commercial preparation of the high quality colloidal nanoparticles.
专利号:WO-2020248278-A1
优先权日:2019-06-14
标题:Method for continuous synthesis of substituted benzoic-acid organic substance
发明人:HONG HAO; ZHANG ENXUAN; LU JIANGPING; LIU ZHIQING; LI CHAO; TANG YANG
权利人:JINLIN ASYMCHEM LABORATORIES CO LTD
摘要:The present invention provides a method for the continuous synthesis of a substituted benzoic-acid organic substance. The continuous synthesis method comprises: in the presence of catalyst and organic solvent, the organic matter represented by formula (I) and oxygen are continuously inputted to a continuous reaction apparatus for continuous oxidation reaction to obtain a substituted benzoic-acid organic substance, which is discharged continuously, the substituted benzoic-acid organic substance having the structure represented by formula (II). Oxygen is a green reagent and is inexpensive and readily available; a large amount of wastewater, waste gas, and solid waste is not generated after the reaction, and the system is easy to handle. The use of a continuous reaction operation can reduce the risk of flash distillation and explosion of solvent due to a high concentration of oxygen in a batch reaction. Under the same oxidation conditions, the continuous preparation process can reduce the escape of oxygen, greatly increasing the oxygen utilization rate and also simplifying the operation, improving the safety of the reaction and the yield of the substituted benzoic-acid organic substance.
专利号:US-8735317-B2
优先权日:2009-06-16
标 题 :Catalyst for synthesis of hydrocarbons from CO and H2 and preparation method thereof
发明人:MORDKOVICH VLADIMIR ZALMANOVICH; SINEVA LILIA VADIMOVA; SOLOMONIK IGOR GRIGORIEVICH; ERMOLAEV VADIM SERGEEVICH; MITBERG EDUARD BORISOVICH
权利人:MORDKOVICH VLADIMIR ZALMANOVICH; SINEVA LILIA VADIMOVA; SOLOMONIK IGOR GRIGORIEVICH; ERMOLAEV VADIM SERGEEVICH; MITBERG EDUARD BORISOVICH; INFRA XTL TECHNOLOGY LTD
摘要:The present invention relates to petrochemistry, gas chemistry, coal chemistry, particularly the invention relates to a catalyst for synthesis of hydrocarbons from CO and H 2 and a preparation method thereof. The catalyst is pelletized and comprises at least Raney cobalt as active component in an amount of 1-40% by weight based on the total weight of the catalyst, metallic aluminium in an amount of 25-94% by weight based on the total weight of the catalyst and a binder in an amount of 5-30% by weight based on the total weight of the catalyst. The present invention provides the catalyst stability to overheating and high productivity of hydrocarbons C 5 -C 100 for synthesis of hydrocarbons from CO and H 2 .
专利号:US-7414008-B2
优先权日:2002-02-28
标 题:Catalyst for synthesis of unsaturated aldehyde, production process for said catalyst, and production process for unsaturated aldehyde using said catalyst
发明人:YUNOKI HIROMI
权利人:NIPPON SHOLONBAI CO LTD
摘要:The present invention provides: a production process for a catalyst for synthesis of an unsaturated aldehyde and/or an unsaturated carboxylic acid, which production process is suitable for producing the catalyst with good reproducibility, wherein the catalyst is excellent in activity, selectivity, and physical strength; this catalyst; and a production process for the unsaturated aldehyde and/or the unsaturated carboxylic acid by using this catalyst. The production process for the catalyst comprises the steps of: carrying out heat treatment of an aqueous solution or slurry of a starting material to thus prepare a catalyst precursor P1, wherein the starting material includes molybdenum, bismuth, and iron as essential components; thereafter adding and mixing a binder into the P1 to thus prepare a catalyst precursor P2; and molding and then calcining the P2, thereby producing the catalyst for synthesis of the unsaturated aldehyde and/or the unsaturated carboxylic acid; with the production process being characterized by involving an ignition loss ratio of the catalyst precursor P1 in the range of 10 to 40 mass % (excluding 40 mass %).