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    • 75. 发明授权
    • Method for separating compounds in process streams
    • 在工艺流中分离化合物的方法
    • US5440058A
    • 1995-08-08
    • US255338
    • 1994-06-07
    • William C. HoffmanJohn P. Dever
    • William C. HoffmanJohn P. Dever
    • A62D3/00A62D3/37A62D3/38A62D101/28A62D101/40B01J19/00C07D301/32C07C29/88C07C31/20C07D303/04
    • A62D3/38A62D3/37B01J19/002C07D301/32A62D2101/28A62D2101/40
    • A method, especially applicable on a continuous basis to commercial process streams, for treating unwanted by-products and/or impurities contained in those streams. The method comprises the reaction in situ of such by-products or impurities with a reagent, preferably selected for its reactivity under ambient conditions of the process stream, to produce one or more materials which may then be separated from the process by economical means. The treated stream may be recycled to the process for further processing. While the method is not limited as to the process to which it is applied nor to the reagent or reagents used, in one convenient embodiment, formaldehyde in aqueous solution is reacted with an alkali metal sulfite or bisulfite to produce the corresponding salt, which may then be separated essentially completely by, e.g., distillation or membrane separation, etc., or its concentration in the process may be controlled by, e.g., continuous removal of a purge stream, etc.
    • 特别适用于商业工艺流的连续的方法,用于处理这些流中包含的不需要的副产物和/或杂质。 该方法包括将这种副产物或杂质与试剂原位反应,优选在工艺流的环境条件下选择其反应性,以产生一种或多种材料,然后可以通过经济方式与该方法分离。 经处理的流可以再循环到该方法进行进一步处理。 虽然该方法不限于其应用的方法,也不限于所用的试剂或试剂,但是在一个方便的实施方案中,水溶液中的甲醛与碱金属亚硫酸盐或亚硫酸氢盐反应以产生相应的盐, 通过例如蒸馏或膜分离等基本上完全分离,或者其过程中的浓度可以通过例如连续除去吹扫流等来控制。
    • 77. 发明授权
    • Epoxidation using hydrogen peroxide and tungsten catalysts
    • 使用过氧化氢和钨催化剂进行环氧化
    • US5430161A
    • 1995-07-04
    • US170213
    • 1993-12-28
    • Scott W. BrownAnthony HackettAlexander JohnstoneRobert A. W. Johnstone
    • Scott W. BrownAnthony HackettAlexander JohnstoneRobert A. W. Johnstone
    • B01J27/228B01J23/30B01J27/188B01J31/06B01J31/08C07B61/00C07D301/12C07D303/04
    • C07D303/04B01J23/30B01J27/188B01J31/08C07D301/12B01J2231/72
    • Alkenes can be expoxidized with hydrogen peroxide using a homogeneous heavy metal catalyst, but discharge of spent reaction mixtures releases the heavy metal in the environment. The problem can be ameliorated by selecting a heterogeneous catalyst system comprising a tungsten-containing heteropolyacid supported on selected Group IIa, IIb, IVa or IVb inorganic supports or on a strong basic resin, which catalyst has either been calcined after impregnation of in the impregnation stage an alcoholic solution of the heteropolyacid is employed and by employing a nitrilo or oxygenated polar solvent reaction medium. A number of preferred heteropolyacids satisfy the empirical formula M.sub.3/n PW.sub.w MO.sub.12-w O.sub.40 in which w represents an integer of at least 1, M represents a counterion and n its basicity. Preferred supports include activated alumina, calcined at 400.degree. to 600.degree. C. and cross-linked quaternary ammonium-substituted polystyrene resins. The most preferred catalysts are made by impregnating an inorganic support with a methanol solution of the heteropolyacid to a desired loading of active material on the support and subsequently calcining the loaded support at 400.degree. to 600.degree. C. Preferred reaction media include acetonitrile and tertiary butanol.
    • PCT No.PCT / GB92 / 01154 Sec。 371日期:1993年12月28日 102(e)日期1993年12月28日PCT提交1992年6月25日PCT公布。 公开号WO93 / 00338 日期1993年1月7日。可以使用均匀的重金属催化剂用过氧化氢对烯烃进行过氧化,但废弃的反应混合物的排放在环境中释放重金属。 可以通过选择包含负载在选定的IIa,IIb,IVa或IVb族无机载体上的含钨杂多酸的非均相催化剂体系或强碱性树脂来改善该问题,该催化剂在浸渍阶段浸渍后煅烧 采用杂多酸的醇溶液,并采用氮化或含氧极性溶剂反应介质。 许多优选的杂多酸满足经验式M3 / nPWwMO12-wO40,其中w表示至少为1的整数,M表示抗衡离子,n表示碱性。 优选的载体包括活性氧化铝,在400〜600℃下煅烧,交联季铵取代聚苯乙烯树脂。 最优选的催化剂是通过将无机载体用杂多酸的甲醇溶液浸渍到载体上所需的活性物质负载并随后在400℃至600℃下煅烧负载的载体而制备的。优选的反应介质包括乙腈和叔丁醇 。
    • 78. 发明授权
    • Asymmetric epoxidation reaction
    • 不对称环氧化反应
    • US5420314A
    • 1995-05-30
    • US209723
    • 1994-03-14
    • Tsutomu KatsukiRyo IrieHidehiko Sasaki
    • Tsutomu KatsukiRyo IrieHidehiko Sasaki
    • C07D301/02C07D303/04C07D493/04C07D498/14C07F13/00C07D323/00C07D487/00C07F9/547
    • C07D493/04C07D301/02C07D303/04C07F13/005
    • An optically active manganese complex of the formula I or I': ##STR1## wherein R.sup.1, R.sup.2, R.sup.3, and R.sup.4 independently represent hydrogen atom, C.sub.1 -C.sub.4 alkyl group, phenyl group which may be substituted by a halogen atom, C.sub.1 -C.sub.4 alkyl group, C.sub.1 -C.sub.4 alkoxyl group, cyano group or nitro group; and any two of R.sup.1, R.sup.2, R.sup.3 and R.sup.4 together form the C.sub.4 -C.sub.8 ring, X.sup.- represents a counter anion which may form a salt, Y represents hydrogen atom, halogen atom, C.sub.1 -C.sub.4 alkyl group, C.sub.1 -C.sub.4 alkoxyl group, nitro group or cyano group, R represents hydrogen atom, C.sub.1 -C.sub.4 alkyl group, phenyl group which may be substituted by halogen atom, C.sub.1 -C.sub.4 alkyl group or C.sub.1 -C.sub.4 alkoxyl group, or substituted silyl group and a process for producing epoxy compounds using the complex as a catalyst.
    • 式I或I'的光学活性锰络合物:其中R 1,R 2,R 3和R 4独立地表示氢原子,C 1 -C 4烷基,可以是C 1 -C 4烷基的苯基 被卤素原子,C1-C4烷基,C1-C4烷氧基,氰基或硝基取代; 并且R 1,R 2,R 3和R 4中的任何一个一起形成C 4 -C 8环,X-表示可形成盐的抗衡阴离子,Y表示氢原子,卤素原子,C1-C4烷基,C1-C4烷氧基 硝基或氰基,R表示氢原子,C1-C4烷基,可被卤素原子取代的苯基,C1-C4烷基或C1-C4烷氧基或取代甲硅烷基,以及环氧化物的制备方法 使用该络合物作为催化剂的化合物。