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公开(公告)号：US20080021254A1
公开(公告)日：2008-01-24
申请号：US11746689
申请日：2007-05-10
IPC分类号： C07C5/22
CPC分类号： H02S20/00 , H01L31/0521 , H02S40/44 , Y02E10/50 , Y02E10/60
摘要： A process for disproportionating isopentane into isomers of hexane and butane that utilizes a fixed bed reactor employing a catalyst composition comprising aluminum halide. The process additionally includes a product separation zone which can be configured to recover and return at least a portion of the isopentane product stream to the inlet of the disproportionation reactor.
摘要翻译： 使用采用包含卤化铝的催化剂组合物的固定床反应器将异戊烷歧化成己烷和丁烷的异构体的方法。 该方法另外包括产物分离区，其可以被配置为回收并将至少一部分异戊烷产物流返回到歧化反应器的入口。
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公开(公告)号：US07902418B2
公开(公告)日：2011-03-08
申请号：US11746689
申请日：2007-05-10
IPC分类号： C07C6/08
CPC分类号： H02S20/00 , H01L31/0521 , H02S40/44 , Y02E10/50 , Y02E10/60
摘要： A process for disproportionating isopentane into isomers of hexane and butane that utilizes a fixed bed reactor employing a catalyst composition comprising aluminum halide. The process additionally includes a product separation zone which can be configured to recover and return at least a portion of the isopentane product stream to the inlet of the disproportionation reactor.
摘要翻译： 使用采用包含卤化铝的催化剂组合物的固定床反应器将异戊烷歧化成己烷和丁烷的异构体的方法。 该方法另外包括产物分离区，其可以被配置为回收并将至少一部分异戊烷产物流返回到歧化反应器的入口。
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公开(公告)号：US07956227B2
公开(公告)日：2011-06-07
申请号：US11951863
申请日：2007-12-06
申请人： Bruce B. Randolph , Jason J. Gislason , M. Bruce Welch , Richard L. Anderson , Dhananjay B. Ghonasgi , Robert W. Morton , Roland Schmidt
发明人： Bruce B. Randolph , Jason J. Gislason , M. Bruce Welch , Richard L. Anderson , Dhananjay B. Ghonasgi , Robert W. Morton , Roland Schmidt
IPC分类号： C07C2/12
CPC分类号： C10G50/00 , B01J29/185 , B01J29/90 , C07C2/12 , C07C11/02 , C07C2529/18 , C07C2529/22 , C10G35/04 , C10G2300/1081 , C10G2300/1088 , C10G2300/1092 , C10G2400/02 , C10G2400/20 , C10G2400/22 , C10L1/06 , Y02P20/584
摘要： Methods of oligomerizing hydrocarbons are disclosed. These methods include contacting olefins with an oligomerization catalyst in an oligomerization zone under oligomerization reaction conditions.
摘要翻译： 公开了低聚烃的方法。 这些方法包括在低聚反应条件下在低聚区中将烯烃与低聚催化剂接触。
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公开(公告)号：US20090149684A1
公开(公告)日：2009-06-11
申请号：US11951863
申请日：2007-12-06
申请人： Bruce B. Randolph , Jason J. Gislason , M. Bruce Welch , Richard L. Anderson , Dhananjay B. Ghonasgi , Robert W. Morton , Roland Schmidt
发明人： Bruce B. Randolph , Jason J. Gislason , M. Bruce Welch , Richard L. Anderson , Dhananjay B. Ghonasgi , Robert W. Morton , Roland Schmidt
IPC分类号： C07C2/56
CPC分类号： C10G50/00 , B01J29/185 , B01J29/90 , C07C2/12 , C07C11/02 , C07C2529/18 , C07C2529/22 , C10G35/04 , C10G2300/1081 , C10G2300/1088 , C10G2300/1092 , C10G2400/02 , C10G2400/20 , C10G2400/22 , C10L1/06 , Y02P20/584
摘要： Methods of oligomerizing hydrocarbons are disclosed. These methods include contacting olefins with an oligomerization catalyst in an oligomerization zone under oligomerization reaction conditions.
摘要翻译： 公开了低聚烃的方法。 这些方法包括在低聚反应条件下在低聚区中将烯烃与低聚催化剂接触。
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公开(公告)号：US06303843B1
公开(公告)日：2001-10-16
申请号：US08530684
申请日：1995-09-18
IPC分类号： C07C717
CPC分类号： C07C7/10 , C07C2/62 , C07C9/16 , C07C2527/1206
摘要： A process for removing sulfone from a liquid hydrocarbon containing a concentration of sulfone by mixing a liquid acid therewith and thereafter separating the resulting admixture into an acid phase and a hydrocarbon phase. The hydrocarbon phase has a concentration of sulfone less than such concentration in the liquid hydrocarbon.
摘要翻译： 通过将液体酸与其混合，然后将所得混合物分离成酸相和烃相，从含有砜浓度的液体烃中除去砜的方法。 烃相在液态烃中的砜浓度低于这样的浓度。
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6.发明授权
公开(公告)号：US5648588A
公开(公告)日：1997-07-15
申请号：US569625
申请日：1995-12-08
CPC分类号： C07C9/00 , C07C7/10 , C07C2527/1206
摘要： Disclosed is a process for separating sulfone and hydrogen fluoride from hydrocarbon streams containing a concentration of such compounds. An extraction solvent laden with sulfone and HF is contacted with a reversible base in order to remove the HF therefrom. The thus-treated extract stream is separated into a water stream that can be reused as the water extractant and a sulfone stream that is suitably free of HF.
摘要翻译： 公开了从含有这种化合物浓度的烃流中分离砜和氟化氢的方法。 将含有砜和HF的提取溶剂与可逆碱接触以从其中除去HF。 将如此处理的萃取物流分离成可以作为水提取剂重复使用的水流和适合不含HF的砜流。
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公开(公告)号：US5792896A
公开(公告)日：1998-08-11
申请号：US808778
申请日：1997-03-04
CPC分类号： B01J19/2465 , C07C2/62 , C07C2527/1206
摘要： An alkylation process for reacting alkylatable hydrocarbons in the presence of a sulfolane and hydrofluoric acid catalyst within a natural circulation reaction and circulation system.
摘要翻译： 在环丁砜和氢氟酸催化剂存在下，使烷基化烃在自然循环反应和循环系统内反应的烷基化方法。
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8.发明授权
公开(公告)号：US5753575A
公开(公告)日：1998-05-19
申请号：US601921
申请日：1996-02-15
CPC分类号： B01J31/4092 , B01J31/0222 , B01J38/48 , C07C2/62 , B01J2231/4205 , B01J27/12 , C07C2527/1206 , Y02P20/584
摘要： Disclosed is an alkylation process which utilizes a mixture of sulfone and hydrogen fluoride as an alkylation catalyst. The process provides for the regeneration of an alkylation catalyst having ASO therein by separating HF from the ASO and sulfone components. The ASO and sulfone are thereafter separated to provide sulfone which is substantially free of ASO.
摘要翻译： 公开了一种利用砜和氟化氢的混合物作烷基化催化剂的烷基化方法。 该方法通过从ASO和砜组分分离HF来提供其中具有ASO的烷基化催化剂的再生。 然后将ASO和砜分离，得到基本上不含ASO的砜。
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9.发明授权
公开(公告)号：US5382744A
公开(公告)日：1995-01-17
申请号：US88942
申请日：1993-07-12
CPC分类号： C07C2/62 , C07C2527/1206
摘要： A method of minimizing or controlling the production of synthetic isopentane during the catalyzed alkylation reaction of amylenes and isoparaffins by providing a concentration of isopentane in the alkylation reactor feed material.
摘要翻译： 通过在烷基化反应器进料中提供异戊烷的浓度，在二烯烃和异链烷烃的催化烷基化反应期间最小化或控制合成异戊烷的生产的方法。
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公开(公告)号：US08258363B2
公开(公告)日：2012-09-04
申请号：US13238974
申请日：2011-09-21
申请人： Sumod Kalakkunnath , Richard L. Anderson , James A. Anderson, legal representative , Richard D. Sadok , Prakash A. Karpe
IPC分类号： C07C7/144
CPC分类号： C10G7/00 , B01D61/022 , B01D61/027 , B01D61/362 , B01D61/58 , B01D2311/04 , B01D2311/06 , B01D2311/08 , B01D2317/022 , B01D2317/025 , C10G2300/1096 , C10G2400/30 , B01D2311/2669
摘要： Methods and apparatus relate to separating and removing aromatic compounds from a hydrocarbon stream. Splitting of the hydrocarbon stream into constituents as desired relies on a membrane and distillation columns that supply feed into the membrane and receive retentate and permeate streams output from the membrane. Configurations employing the membrane and the distillation columns enable benzene recovery and facilitate efficient separation.
摘要翻译： 方法和装置涉及从烃流中分离和除去芳族化合物。 根据需要将烃流分解成组分依赖于将进料加入到膜中并接收从膜输出的渗余物和渗透物流的膜和蒸馏塔。 使用膜和蒸馏塔的配置使得苯回收和促进有效的分离。
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