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    • 1. 发明授权
    • Process for continuous reaction and deparation using reactive
chromatography
    • 使用反应层析连续反应和分离的方法
    • US5744683A
    • 1998-04-28
    • US666713
    • 1996-06-18
    • Hemant W. DandekarGregory A. FunkSimon H. HobbsMasami KojimaRalph D. GillespieHerman A. ZinnenCharles P. McGonegal
    • Hemant W. DandekarGregory A. FunkSimon H. HobbsMasami KojimaRalph D. GillespieHerman A. ZinnenCharles P. McGonegal
    • C07C5/27C07C9/16C07C5/13C07C7/12
    • C07C9/16C07C5/2791C07C2521/04C07C2523/42C07C2527/126C07C2529/44Y02P20/582
    • A process for the continuous isomerization of an alkane to produce an isomerized product through contacting the alkane with a simulated moving bed acting as a catalyst for isomerization and an adsorbent for the alkanes has been developed. The alkane may be n-butane and the isomerized product 2-methylpropane, the alkane may be n-pentane and the isomerized product 2-methylbutane or 2,2-dimethylpropane, the alkane may have from 6 up to about 8 carbon atoms with no more than one methyl branch and the isomerized product having the same number of carbon atoms and at least two methyl branches, or the reactant may be a mixture of the foregoing alkanes with the corresponding isomerized products being formed. In a zone of the simulated moving bed, the alkanes are catalytically isomerized to form the isomerized products. The unreacted alkanes are adsorbed, and the isomerized products are collected. In a first subsequent zone of the simulated moving bed, a large portion of the unreacted alkanes are desorbed using a desorbent. In a second subsequent zone of the simulated moving bed, residual adsorbed alkanes are desorbed using a mixture of desorbent and isomerized products, and the desorbed residual alkanes may be removed from the simulated moving bed or may be reacted to form additional isomerized products. The isomerized products are removed from the simulated moving bed and collected. The process may also be used to effect other chemical reactions with the concurrent separation of product.
    • 已经开发了通过使烷烃与用作异构化的催化剂的模拟移动床和用于烷烃的吸附剂使烷烃连续异构化以产生异构化产物的方法。 烷烃可以是正丁烷,异构化产物2-甲基丙烷,烷烃可以是正戊烷,异构化产物2-甲基丁烷或2,2-二甲基丙烷,烷烃可以具有6个至约8个碳原子,没有 多于一个甲基支链和具有相同数目的碳原子和至少两个甲基支链的异构化产物,或者反应物可以是前述烷烃与形成相应的异构化产物的混合物。 在模拟移动床的区域中,烷烃被催化异构化以形成异构化产物。 未反应的烷烃被吸附,收集异构化产物。 在模拟移动床的第一后续区域中,大部分未反应的烷烃使用解吸剂解吸附。 在模拟移动床的第二个随后的区域中,残余吸附的烷烃使用解吸剂和异构化产物的混合物解吸,并且解吸的残余烷烃可以从模拟的移动床中除去,或者可以反应形成另外的异构化产物。 将异构化产物从模拟移动床上取出并收集。 该方法也可用于通过产品的同时分离来实现其它化学反应。
    • 2. 发明授权
    • Process for alkane isomerization using reactive chromatography
    • 使用反应层析的烷烃异构化方法
    • US5763730A
    • 1998-06-09
    • US666717
    • 1996-06-18
    • Hemant W. DandekarGregory A. FunkRalph D. GillespieHerman A. ZinnenCharles P. McGonegalMasami KojimaSimon H. Hobbs
    • Hemant W. DandekarGregory A. FunkRalph D. GillespieHerman A. ZinnenCharles P. McGonegalMasami KojimaSimon H. Hobbs
    • C07C5/27C07C7/13C07C9/12C07C9/16C07C9/18C07C5/122
    • C07C5/2789C07C5/2791C07C7/13C07C9/12C07C9/16C07C9/18C07C2521/04C07C2521/06C07C2523/42C07C2523/54C07C2527/126C07C2529/22Y02P20/582
    • A process for the continuous isomerization of an alkane to produce an isomerized product through contacting the alkane with a simulated moving bed acting as a catalyst for isomerization and an adsorbent for the alkanes has been developed. The alkane may be n-butane and the isomerized product 2-methylpropane, the alkane may be n-pentane and the isomerized product 2-methylbutane or 2,2-dimethylpropane, the alkane may have from 6 up to about 8 carbon atoms with no more than one methyl branch and the isomerized product having the same number of carbon atoms and at least two methyl branches, or the reactant may be a mixture of the foregoing alkanes with the corresponding isomerized products being formed. In a zone of the simulated moving bed, the alkanes are catalytically isomerized to form the isomerized products. The unreacted alkanes are adsorbed, and the isomerized products are collected. In a subsequent zone of the simulated moving bed, the unreacted alkanes are desorbed using a desorbent and may be catalytically isomerized to form additional isomerized products which are also separated and collected. The catalyst used in the simulated moving bed may be platinum on tungstated zirconia, and the adsorbent used in the simulated moving bed may be EU-1, ZSM-12, SAPO-5, Y-82, faujasite, erionite, zeolite beta exchanged with sodium, lithium, potassium, barium, calcium, strontium or combinations thereof, zeolite X exchanged with calcium and strontium, mordenite exchanged with sodium, lithium, potassium, barium, calcium, strontium, or combinations thereof.
    • 已经开发了通过使烷烃与用作异构化的催化剂的模拟移动床和用于烷烃的吸附剂使烷烃连续异构化以产生异构化产物的方法。 烷烃可以是正丁烷,异构化产物2-甲基丙烷,烷烃可以是正戊烷,异构化产物2-甲基丁烷或2,2-二甲基丙烷,烷烃可以具有6个至约8个碳原子,没有 多于一个甲基支链和具有相同数目的碳原子和至少两个甲基支链的异构化产物,或者反应物可以是前述烷烃与形成相应的异构化产物的混合物。 在模拟移动床的区域中,烷烃被催化异构化以形成异构化产物。 未反应的烷烃被吸附,收集异构化产物。 在模拟移动床的随后区域中,未反应的烷烃使用解吸剂解吸,并且可以被催化异构化以形成也被分离和收集的另外的异构化产物。 在模拟移动床中使用的催化剂可以是钨酸氧化锆上的铂,模拟移动床中使用的吸附剂可以是EU-1,ZSM-12,SAPO-5,Y-82,八面沸石,毛沸石,沸石β与 钠,锂,钾,钡,钙,锶或其组合,与钙和锶交换的沸石X,与钠,锂,钾,钡,钙,锶或它们的组合交换的丝光沸石。
    • 3. 发明授权
    • Process for alkane isomerization using reactive chromatography and
reactive desorbent
    • US5744684A
    • 1998-04-28
    • US666699
    • 1996-06-18
    • Herman A. ZinnenCharles P. McGonegalHemant W. DandekarGregory A. FunkRalph D. Gillespie
    • Herman A. ZinnenCharles P. McGonegalHemant W. DandekarGregory A. FunkRalph D. Gillespie
    • C07C9/16C07C5/22
    • C07C9/16Y02P20/582
    • A process for isomerizing a mixture of alkanes containing pentanes and at least one alkane having from 6 to about 8 carbon atoms and no more than one methyl branch has been developed. The process includes: 1) separating the mixture in a first separation zone to produce two streams, a stream enriched in alkanes having from 6 to about 8 carbon atoms and a stream enriched in pentanes; 2) separating the stream enriched in pentanes in a second separation zone to produce two streams, a stream predominately comprising n-pentane and a stream predominately comprising branched pentanes; 3) passing the stream enriched in alkanes having from 6 to about 8 carbon atoms and the stream enriched in n-pentane to an isomerization zone of a simulated moving bed to produce two streams, a stream containing branched pentanes, n-pentane, and multi-methyl-branched alkanes having from 6 to about 8 carbon atoms, and a stream containing branched pentanes and n-pentane; 4) separating the stream containing branched pentanes, n-pentane, and multi-methyl-branched alkanes having from 6 to about 8 carbon atoms in a third separation zone to produce two streams, a stream enriched in multi-methyl-branched alkanes having from 6 to about 8 carbon atoms and a stream enriched in branched pentanes and n-pentane; and 5) collecting the stream predominately comprising branched pentanes from the second separation zone and the stream enriched in multi-methyl-branched alkanes having from 6 to about 8 carbon atoms from the third separation zone. The catalyst used in the simulated moving bed may be platinum on tungstated zirconia and the adsorbent used in the simulated moving bed may be one or more of the following adsorbents, zeolite beta exchanged with sodium, lithium, potassium, barium, calcium, strontium or combinations thereof, zeolite X exchanged with calcium and strontium, mordenite exchanged with sodium, lithium, potassium, barium, calcium, strontium, or combinations thereof, EU-1, ZSM-12, SAPO-5, Y-82, faujasite and erionite.
    • 5. 发明授权
    • Isomerization process using novel catalyst
    • 使用新型催化剂的异构化方法
    • US07022889B2
    • 2006-04-04
    • US10804358
    • 2004-03-19
    • Ralph D. GillespieMichelle J. CohnLynn H. Rice
    • Ralph D. GillespieMichelle J. CohnLynn H. Rice
    • C07C5/13
    • B01J27/053B01J21/066B01J23/63B01J23/894B01J37/0205C10G2400/02
    • A process for the isomerization of a feedstream comprising C5–C6 hydrocarbons where the process involves charging hydrogen and a feedstream comprising at least normal C5–C6 hydrocarbons into an isomerization zone and contacting said hydrogen and feedstream with an isomerization catalyst at isomerization conditions to increase the branching of the feedstream hydrocarbons and produce an isomerization effluent stream comprising at least normal pentane, normal hexane, methylbutane, dimethylbutane, and methylpentane has been discovered. The catalyst used is a solid acid catalyst comprising a support comprising a sulfated oxide or hydroxide of at least an element of Group IVB (IUPAC 4) of the Periodic Table, a first component selected from the group consisting of at least one lanthanide-series element, mixtures thereof, and yttrium, and a second component selected from the group of platinum-group metals and mixtures thereof.
    • 含有C 5 -C 6烃的进料流的异构化方法,其中该方法包括加入氢气和至少含有正常C 5 -C 15烃的进料流 将-C 6 -C 6烃转化成异构化区,并使异构化催化剂在异构化条件下使所述氢和原料流与异构化催化剂接触以增加原料流烃的分支,并产生异构化流出物流,其至少包含正常戊烷,正常 已经发现己烷,甲基丁烷,二甲基丁烷和甲基戊烷。 所使用的催化剂是一种固体酸催化剂,其包括含有至少元素周期表第IVB族(IUPAC 4)元素的硫酸化氧化物或氢氧化物的载体,选自至少一种镧系元素元素 ,其混合物和钇,以及选自铂族金属及其混合物的第二组分。