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公开(公告)号:US20080319234A1
公开(公告)日:2008-12-25
申请号:US11821020
申请日:2007-06-21
IPC分类号: C07C409/08 , B01J27/185 , B01J27/24 , B01J31/12
CPC分类号: B01J23/745 , B01J31/0211 , B01J31/0252 , B01J35/0033 , B01J37/0203 , B01J2231/70 , C07C407/00 , C07C409/10 , C07C409/14 , C07C2601/14 , C07C409/08
摘要: A promoter can have utility in selective heterogeneous oxidation of arylalkyl hydrocarbons such as, for example, cyclohexyl benzene and/or sec-butyl benzene to form hydroperoxides. The promoter can include the product of contacting a solid support comprising a metal oxide surface and an iron compound. The solid support can include, for example, titanium dioxide and/or an iron oxide such as magnetite and can have magnetic susceptibility. A method for the oxidation of arylalkyl hydrocarbons to form hydroperoxides can include contacting 16 an arylalkyl hydrocarbon with oxygen in the presence of the promoter under catalytic oxidation conditions to form arylalkyl hydroperoxide, which can then be converted to phenol via cleavage 26. The method can include recovery 22 of the promoter from the arylalkyl hydroperoxide and can further include recycling the recovered promoter to the contacting 16. Where the solid support has magnetic susceptibility, the recovery 22 can include magnetic separation of the promoter.
摘要翻译: 助催化剂可用于芳基烷基烃例如环己基苯和/或仲丁基苯的选择性异相氧化以形成氢过氧化物。 助催化剂可以包括使包含金属氧化物表面和铁化合物的固体载体接触的产物。 固体支持体可以包括例如二氧化钛和/或氧化铁如磁铁矿,并且可以具有磁化率。 用于氧化芳基烷基烃以形成氢过氧化物的方法可以包括在催化氧化条件下在助催化剂存在下使芳烷基烃与氧接触,形成芳基烷基氢过氧化物,然后可通过裂解将其转化为苯酚。该方法可包括 从芳基烷基氢过氧化物中回收22个启动子,并且可以进一步包括将回收的促进剂再循环到接触16.当固体支持物具有磁化率时,回收22可以包括促进剂的磁性分离。
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公开(公告)号:US07692046B2
公开(公告)日:2010-04-06
申请号:US11821020
申请日:2007-06-21
IPC分类号: C07C409/00
CPC分类号: B01J23/745 , B01J31/0211 , B01J31/0252 , B01J35/0033 , B01J37/0203 , B01J2231/70 , C07C407/00 , C07C409/10 , C07C409/14 , C07C2601/14 , C07C409/08
摘要: A promoter can have utility in selective heterogeneous oxidation of arylalkyl hydrocarbons such as, for example, cyclohexyl benzene and/or sec-butyl benzene to form hydroperoxides. The promoter can include the product of contacting a solid support comprising a metal oxide surface and an iron compound. The solid support can include, for example, titanium dioxide and/or an iron oxide such as magnetite and can have magnetic susceptibility. A method for the oxidation of arylalkyl hydrocarbons to form hydroperoxides can include contacting 16 an arylalkyl hydrocarbon with oxygen in the presence of the promoter under catalytic oxidation conditions to form arylalkyl hydroperoxide, which can then be converted to phenol via cleavage 26. The method can include recovery 22 of the promoter from the arylalkyl hydroperoxide and can further include recycling the recovered promoter to the contacting 16. Where the solid support has magnetic susceptibility, the recovery 22 can include magnetic separation of the promoter.
摘要翻译: 助催化剂可用于芳基烷基烃例如环己基苯和/或仲丁基苯的选择性异相氧化以形成氢过氧化物。 助催化剂可以包括使包含金属氧化物表面和铁化合物的固体载体接触的产物。 固体支持体可以包括例如二氧化钛和/或氧化铁如磁铁矿,并且可以具有磁化率。 用于氧化芳基烷基烃以形成氢过氧化物的方法可以包括在催化氧化条件下在助催化剂存在下使芳烷基烃与氧接触,形成芳基烷基氢过氧化物,然后可通过裂解将其转化为苯酚。该方法可包括 从芳基烷基氢过氧化物中回收22个启动子,并且可以进一步包括将回收的促进剂再循环到接触16.当固体支持物具有磁化率时,回收22可以包括促进剂的磁性分离。
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公开(公告)号:US20140187821A1
公开(公告)日:2014-07-03
申请号:US13989903
申请日:2011-10-25
申请人: Kun Wang , Jihad M. Dakka , Stephen Zushma , James R. Lattner , Christopher L. Becker , Tan-Jen Chen
发明人: Kun Wang , Jihad M. Dakka , Stephen Zushma , James R. Lattner , Christopher L. Becker , Tan-Jen Chen
CPC分类号: C07C2/74 , C07C37/08 , C07C45/53 , C07C2529/08 , C07C2529/18 , C07C2529/70 , C07C2601/14 , C07C39/04 , C07C49/403 , C07C13/28
摘要: In a process for producing a cycloalkylaromatic compound, an aromatic compound and a cyclic olefin are contacted with a first catalyst under conditions effective to produce a reaction product comprising the cycloalkylaromatic compound and at least one non-fused bicyclic by-product. The at least one non-fused bicyclic by-product is then contacted with a second catalyst under conditions effective to convert at least a portion of the at least one non-fused bicyclic by-product to a converted by-product.
摘要翻译: 在制备环烷基芳族化合物的方法中,芳族化合物和环状烯烃在有效产生包含环烷基芳族化合物和至少一种非稠合双环副产物的反应产物的条件下与第一催化剂接触。 然后至少一种非稠合双环副产物在有效将至少一部分非稠合双环副产物转化为转化副产物的条件下与第二催化剂接触。
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公开(公告)号:US20110105805A1
公开(公告)日:2011-05-05
申请号:US12996219
申请日:2009-07-14
IPC分类号: C07C37/08
CPC分类号: C07C37/06 , C07C2/74 , C07C37/08 , C07C45/53 , C07C407/00 , C07C2601/14 , C07C13/28 , C07C39/04 , C07C49/403 , C07C409/14
摘要: In a process for producing phenol, cyclohexylbenzene is oxidized to produce cyclohexylbenzene hydroperoxide and then the resultant cyclohexylbenzene hydroperoxide is cleaved to produce an effluent stream comprising phenol and cyclohexanone. At least a portion of the effluent stream is then fed to at least one dehydrogenation reaction zone, where the effluent stream portion is contacted with a dehydrogenation catalyst under conditions effective to convert at least part of the cyclohexanone in the effluent portion into phenol and hydrogen.
摘要翻译: 在生产苯酚的方法中,将环己基苯氧化生产环己基苯氢过氧化物,然后将所得的环己基苯氢过氧化物切割以产生包含苯酚和环己酮的流出物流。 然后将至少一部分流出物流送入至少一个脱氢反应区,其中流出物流部分与脱氢催化剂在有效地将流出物部分中的至少一部分环己酮转化为酚和氢的条件下接触。
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公开(公告)号:US08487140B2
公开(公告)日:2013-07-16
申请号:US12996219
申请日:2009-07-14
CPC分类号: C07C37/06 , C07C2/74 , C07C37/08 , C07C45/53 , C07C407/00 , C07C2601/14 , C07C13/28 , C07C39/04 , C07C49/403 , C07C409/14
摘要: In a process for producing phenol, cyclohexylbenzene is oxidized to produce cyclohexylbenzene hydroperoxide and then the resultant cyclohexylbenzene hydroperoxide is cleaved to produce an effluent stream comprising phenol and cyclohexanone. At least a portion of the effluent stream is then fed to at least one dehydrogenation reaction zone, where the effluent stream portion is contacted with a dehydrogenation catalyst under conditions effective to convert at least part of the cyclohexanone in the effluent portion into phenol and hydrogen.
摘要翻译: 在生产苯酚的方法中,将环己基苯氧化生产环己基苯氢过氧化物,然后将所得的环己基苯氢过氧化物切割以产生包含苯酚和环己酮的流出物流。 然后将至少一部分流出物流送入至少一个脱氢反应区,其中流出物流部分与脱氢催化剂在有效地将流出物部分中的至少一部分环己酮转化为酚和氢的条件下接触。
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公开(公告)号:US09061270B2
公开(公告)日:2015-06-23
申请号:US13520467
申请日:2010-12-17
申请人: Teng Xu , Terry E. Helton , Jihad M. Dakka , Tan-Jen Chen , Sabato Miseo , Lorenzo C. Decaul , Edward A. Lemon, Jr.
发明人: Teng Xu , Terry E. Helton , Jihad M. Dakka , Tan-Jen Chen , Sabato Miseo , Lorenzo C. Decaul , Edward A. Lemon, Jr.
IPC分类号: C07C37/08 , C07C37/00 , B01J29/04 , B01J21/00 , B01J23/58 , B01J21/08 , B01J37/02 , B01J37/12 , C07C2/74 , C07C37/06 , C07C45/53 , C07C407/00 , C07C37/07
CPC分类号: B01J23/58 , B01J21/08 , B01J37/0205 , B01J37/12 , C07C2/74 , C07C37/06 , C07C37/07 , C07C37/08 , C07C45/53 , C07C407/00 , C07C2529/70 , C07C2601/14 , Y02P20/52 , C07C13/28 , C07C39/04 , C07C49/403 , C07C409/14
摘要: A catalyst composition comprising: (i) a support; (ii) a first component comprising at least one metal component selected from Group 1 and Group 2 of the Periodic Table of Elements; and (iii) a second component comprising at least one metal component selected from Groups 6 to 10 of the Periodic Table of Elements, wherein the catalyst composition exhibits an oxygen chemisorption of greater than 50%.
摘要翻译: 一种催化剂组合物,其包含:(i)载体; (ii)包含选自元素周期表第1族和第2族的至少一种金属成分的第一成分; 和(iii)包含选自元素周期表第6至10族的至少一种金属组分的第二组分,其中催化剂组合物显示出大于50%的氧化学吸附。
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公开(公告)号:US09024078B2
公开(公告)日:2015-05-05
申请号:US13515104
申请日:2010-12-17
申请人: Jihad M. Dakka , Lorenzo C. Decaul , Sabato Miseo , James R. Lattner , Tan-Jen Chen , Terry E. Helton , Teng Xu
发明人: Jihad M. Dakka , Lorenzo C. Decaul , Sabato Miseo , James R. Lattner , Tan-Jen Chen , Terry E. Helton , Teng Xu
IPC分类号: C07C37/08 , C07C5/32 , C07C37/07 , C07C45/53 , C07C407/00
CPC分类号: C07C37/08 , B01J23/58 , B01J35/1019 , B01J35/1061 , B01J37/0009 , B01J37/0203 , C07C5/367 , C07C37/07 , C07C45/53 , C07C407/00 , C07C2521/08 , C07C2523/42 , C07C2523/58 , C07C2601/14 , Y02P20/52 , C07C39/04 , C07C49/403 , C07C409/14 , C07C15/04
摘要: A dehydrogenation process for the dehydrogenation of at least one dehydrogenatable hydrocarbon, the process comprising contacting a feed comprising the at least one dehydrogenatable hydrocarbon under dehydrogenation conditions with a catalyst composition comprising a support and at least one dehydrogenation component wherein said conditions include a temperature of from 400° C. to 750° C. and a pressure of at least 50 psig (345 kPag).
摘要翻译: 用于脱氢至少一种可脱氢烃的脱氢方法,该方法包括在脱氢条件下使包含至少一种可脱氢烃的进料与包含载体和至少一种脱氢组分的催化剂组合物接触,其中所述条件包括 400℃至750℃,压力至少为50psig(345kPag)。
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公开(公告)号:US08884065B2
公开(公告)日:2014-11-11
申请号:US13989903
申请日:2011-10-25
申请人: Kun Wang , Jihad M. Dakka , Stephen Zushma , James R. Lattner , Christopher L. Becker , Tan-Jen Chen
发明人: Kun Wang , Jihad M. Dakka , Stephen Zushma , James R. Lattner , Christopher L. Becker , Tan-Jen Chen
IPC分类号: C07C45/53 , C07C15/067 , C07C37/08 , C07C2/74
CPC分类号: C07C2/74 , C07C37/08 , C07C45/53 , C07C2529/08 , C07C2529/18 , C07C2529/70 , C07C2601/14 , C07C39/04 , C07C49/403 , C07C13/28
摘要: In a process for producing a cycloalkylaromatic compound, an aromatic compound and a cyclic olefin are contacted with a first catalyst under conditions effective to produce a reaction product comprising the cycloalkylaromatic compound and at least one non-fused bicyclic by-product. The at least one non-fused bicyclic by-product is then contacted with a second catalyst under conditions effective to convert at least a portion of the at least one non-fused bicyclic by-product to a converted by-product.
摘要翻译: 在制备环烷基芳族化合物的方法中,芳族化合物和环状烯烃在有效产生包含环烷基芳族化合物和至少一种非稠合双环副产物的反应产物的条件下与第一催化剂接触。 然后至少一种非稠合双环副产物在有效将至少一部分非稠合双环副产物转化为转化副产物的条件下与第二催化剂接触。
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公开(公告)号:US20120302798A1
公开(公告)日:2012-11-29
申请号:US13515104
申请日:2010-12-17
申请人: Jihad M. Dakka , Lorenzo C. Decaul , Sabato Miseo , James R. Lattner , Tan-Jen Chen , Terry E. Helton , Teng Xu
发明人: Jihad M. Dakka , Lorenzo C. Decaul , Sabato Miseo , James R. Lattner , Tan-Jen Chen , Terry E. Helton , Teng Xu
CPC分类号: C07C37/08 , B01J23/58 , B01J35/1019 , B01J35/1061 , B01J37/0009 , B01J37/0203 , C07C5/367 , C07C37/07 , C07C45/53 , C07C407/00 , C07C2521/08 , C07C2523/42 , C07C2523/58 , C07C2601/14 , Y02P20/52 , C07C39/04 , C07C49/403 , C07C409/14 , C07C15/04
摘要: A dehydrogenation process for the dehydrogenation of at least one dehydrogenatable hydrocarbon, the process comprising contacting a feed comprising the at least one dehydrogenatable hydrocarbon under dehydrogenation conditions with a catalyst composition comprising a support and at least one dehydrogenation component wherein said conditions include a temperature of from 400° C. to 750° C. and a pressure of at least 50 psig (345 kPag).
摘要翻译: 用于脱氢至少一种可脱氢烃的脱氢方法,该方法包括在脱氢条件下使包含至少一种可脱氢烃的进料与包含载体和至少一种脱氢组分的催化剂组合物接触,其中所述条件包括 400℃至750℃,压力至少为50psig(345kPag)。
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公开(公告)号:US09365467B2
公开(公告)日:2016-06-14
申请号:US13883742
申请日:2011-12-02
CPC分类号: C07C2/74 , C07C5/367 , C07C6/126 , C07C2521/08 , C07C2523/14 , C07C2523/42 , C07C2601/08 , C07C2601/14 , C07C13/28
摘要: In a process for producing cyclohexylbenzene, benzene is contacted with hydrogen under hydroalkylation conditions effective to form a first effluent stream comprising cyclohexylbenzene, cyclohexane, methylcyclopentane, and unreacted benzene. At least a portion of the first effluent stream is contacted with a dehydrogenation catalyst under dehydrogenation conditions to convert at least a portion of the cyclohexane to benzene thereby forming a second effluent stream. The amount of methylcyclopentane in the second effluent stream is different by no more than 65% of the total amount of the portion of the first effluent stream, said amounts being on a weight basis. A methylcyclopentane-containing stream is removed from either the first or the second effluent stream and at least a portion of the second effluent stream containing benzene is recycled to the hydroalkylation step.
摘要翻译: 在生产环己基苯的方法中,苯在有效形成包含环己基苯,环己烷,甲基环戊烷和未反应苯的第一流出物流的加氢烷基化条件下与氢气接触。 在脱氢条件下,将至少一部分第一流出物流与脱氢催化剂接触以将至少一部分环己烷转化为苯,从而形成第二流出物流。 第二流出物流中的甲基环戊烷的量不同于第一流出物流的部分总量的不超过65%,所述量基于重量。 从第一或第二流出物流中除去含甲基环戊烷的物流,并将含有苯的第二流出物流的至少一部分再循环至加氢烷基化步骤。
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