会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 14. 发明授权
    • Process for selective oxidation of olefins to epoxides
    • 将烯烃选择性氧化成环氧化物的方法
    • US08080677B2
    • 2011-12-20
    • US12206335
    • 2008-09-08
    • Bala SubramaniamDaryle H. BuschHyun-Jin LeeMadhav GhantaTie-Pan Shi
    • Bala SubramaniamDaryle H. BuschHyun-Jin LeeMadhav GhantaTie-Pan Shi
    • C07D303/00
    • C07D301/12Y02P20/582
    • A process for the selective oxidation of olefins to epoxides comprising the step of contacting the olefin (propylene or ethylene) with an oxidant (hydrogen peroxide) in the presence of a Lewis acid oxidation catalyst (MTO), organic base (pyridine or its N-oxide), in a solvent system comprising an organic water-miscible solvent (methanol). The system is pressurized using either the olefin itself or by adding an inert pressurizing gas (nitrogen) to increase the pressure between 230 and 700 psi at a temperature between 0.7 and 1.3 times the critical temperature of the olefin. The resulting increased solubility of the olefin in the organic solvent system increases the selectivity and yield of the desired epoxide (propylene oxide or ethylene oxide).
    • 一种将烯烃选择性氧化成环氧化物的方法,包括在路易斯酸氧化催化剂(MTO),有机碱(吡啶或其N-氧化物)存在下使烯烃(丙烯或乙烯)与氧化剂(过氧化氢)接触的步骤, 氧化物),在包含有机水混溶性溶剂(甲醇)的溶剂体系中。 使用烯烃本身或通过加入惰性加压气体(氮气)来加压系统,以在烯烃的临界温度的0.7至1.3倍之间的温度下增加230至700psi之间的压力。 所产生的烯烃在有机溶剂体系中的溶解度增加了所需环氧化物(环氧丙烷或环氧乙烷)的选择性和产率。
    • 17. 发明申请
    • Process for Selective Oxidation of Olefins to Epoxides
    • 烯烃选择性氧化成环氧化物的方法
    • US20090131693A1
    • 2009-05-21
    • US12206335
    • 2008-09-08
    • Daryle H. BuschBala SubramaniamHyun-Jin LeeTie-Pan Shi
    • Daryle H. BuschBala SubramaniamHyun-Jin LeeTie-Pan Shi
    • C07D301/03C07D301/12C09K3/00
    • C07D301/12Y02P20/582
    • A process for the selective oxidation of olefins to epoxides comprising the step of contacting the olefin (propylene or ethylene) with an oxidant (hydrogen peroxide) in the presence of a Lewis acid oxidation catalyst (MTO), organic base (pyridine or its N-oxide), in a solvent system comprising an organic water-miscible solvent (methanol). The system is pressurized using either the olefin itself or by adding an inert pressurizing gas (nitrogen) to increase the pressure between 230 and 700 psi at a temperature between 0.7 and 1.3 times the critical temperature of the olefin. The resulting increased solubility of the olefin in the organic solvent system increases the selectivity and yield of the desired epoxide (propylene oxide or ethylene oxide).
    • 一种将烯烃选择性氧化成环氧化物的方法,包括在路易斯酸氧化催化剂(MTO),有机碱(吡啶或其N-氧化物)存在下使烯烃(丙烯或乙烯)与氧化剂(过氧化氢)接触的步骤, 氧化物),在包含有机水混溶性溶剂(甲醇)的溶剂体系中。 使用烯烃本身或通过加入惰性加压气体(氮气)来加压系统,以在烯烃的临界温度的0.7至1.3倍之间的温度下增加230至700psi之间的压力。 所产生的烯烃在有机溶剂体系中的溶解度增加了所需环氧化物(环氧丙烷或环氧乙烷)的选择性和产率。
    • 19. 发明授权
    • Solid acid supercritical alkylation reactions using carbon dioxide
and/or other co-solvents
    • 使用二氧化碳和/或其他共溶剂的固体酸超临界烷基化反应
    • US5907075A
    • 1999-05-25
    • US872865
    • 1997-06-11
    • Bala SubramaniamMichael C. Clark
    • Bala SubramaniamMichael C. Clark
    • B01J3/00C07B61/00C07C2/58C07C9/21C07C2/56
    • C07C2/58B01J3/008C07C2521/06C07C2529/06Y02P20/544
    • Improved isoparaffin-olefin alkylation solid catalyst processes are provided which are characterized by low coke laydown and catalyst deactivation rates and production of valuable branched chain, high octane number alkylates. The processes of the invention involve providing a starting reactant mixture comprising an isoparaffin, an olefin and a co-solvent or diluent (carbon dioxide in molar excess, methane, hydrogen or mixtures thereof), and contacting the reactant mixture with an alkylation catalyst at near-critical or preferably supercritical conditions for the reaction mixture. The carbon dioxide serves as a co-solvent and reduces the critical temperature (T.sub.c) of the reaction mixture, thereby allowing lower reaction temperatures. The isoparaffin and olefin reactants are preferably pretreated to minimize moisture, peroxide and oxygenate impurities therein.
    • 提供改进的异链烷烃烯烃烷基化固体催化剂方法,其特征在于低焦炭沉淀和催化剂失活速率和有价值的支链高辛烷值烷基化物的生产。 本发明的方法包括提供起始反应物混合物,其包含异链烷烃,烯烃和共溶剂或稀释剂(摩尔过量的二氧化碳,甲烷,氢气或其混合物),并将反应混合物与烷基化催化剂接近 重要或优选超临界条件。 二氧化碳用作助溶剂并降低反应混合物的临界温度(Tc),由此允许较低的反应温度。 优选对异链烷烃和烯烃反应物进行预处理,以使其中的水分,过氧化物和含氧化合物的杂质最小化。