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公开(公告)号:US5275726A
公开(公告)日:1994-01-04
申请号:US921872
申请日:1992-07-29
CPC分类号: B01D63/10
摘要: An improved spiral wound element for separations is disclosed wherein the improvement comprises using as the feed/retentate space one or more layers of a material having an open cross-sectional area in the range 30 to 70% and as the permeate spacer material at least three layers of material two of which are fine and have an open cross-sectional area of about 10 to 50% surrounding a coarse layer having an open cross-sectional area of about 50 to 90%.
摘要翻译: 公开了一种用于分离的改进的螺旋缠绕元件,其中改进包括使用一层或多层具有在30-70%范围内的开口横截面积的材料作为进料/滞留物空间,并且作为渗透物间隔物材料至少三个 其中两层材料是细的并且具有围绕具有约50至90%的敞开横截面积的粗糙层的约10至50%的敞开横截面积。
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公开(公告)号:US5095170A
公开(公告)日:1992-03-10
申请号:US622443
申请日:1990-12-05
申请人: Tan-Jen Chen , James R. Sweet
发明人: Tan-Jen Chen , James R. Sweet
IPC分类号: C10G53/04
CPC分类号: C10G53/04
摘要: The yield, raffinate product quality, and throughput of the selective solvent extraction of hydrocarbon feeds is improved by subjecting the hydrocarbon feeds from which aromatic hydrocarbons are to be selectively solvent extracted to a membrane separation process which selectively permeates aromatics through the membranes to produce a permeate rich in aromatics and a retentate rich in saturates and 1-ring aromatics and subjecting this retentate to the selective solvent extraction process.
摘要翻译: 通过使选择性地将芳烃选择性地溶剂萃取的烃进料经由选择性地通过膜渗透芳族化合物以产生渗透物的膜分离方法来改进烃进料的选择性溶剂萃取的产率,萃余液产品质量和通量 富含芳烃和富含饱和物和1-环芳烃的保留物,并使该滞留物进行选择性溶剂萃取过程。
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公开(公告)号:US5039394A
公开(公告)日:1991-08-13
申请号:US591336
申请日:1990-12-10
申请人: Tan-Jen Chen , Lloyd A. Pine
发明人: Tan-Jen Chen , Lloyd A. Pine
CPC分类号: C10G9/005 , C10J3/482 , C10J3/54 , C10J3/721 , C10J3/84 , C10K1/024 , C10K1/08 , C10J2300/0986 , C10J2300/1807 , Y02E20/18
摘要: A fluid coking-gasification process for converting heavy hydrocarbonaceous chargestocks to lower boiling products in which a zeolitic material is use to mitigate slagging in the gasifier, especially when the zeolite material is spent catalytic cracking catalyst. The zeolite material is added either directly into the gasifier on it is mixed with the coke passing from the heating zone to the gasification zone.
摘要翻译: 一种流化焦化气化方法,用于将重质烃类物料转化为较低沸点产物,其中沸石材料用于减轻气化器中的结渣,特别是当沸石材料为废催化裂化催化剂时。 将沸石材料直接加入到气化器中,将其与通过加热区的焦炭混合到气化区。
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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:US08329956B2
公开(公告)日:2012-12-11
申请号:US13409331
申请日:2012-03-01
申请人: Jane C. Cheng , Tan-Jen Chen , Prasenjeet Ghosh
发明人: Jane C. Cheng , Tan-Jen Chen , Prasenjeet Ghosh
IPC分类号: C07C45/27 , C07C27/08 , C07C2/68 , C07C15/067
CPC分类号: B01J29/7088 , B01J21/04 , B01J23/44 , B01J29/7476 , B01J29/7676 , B01J35/0006 , B01J37/0009 , B01J2229/42 , C07C2/74 , C07C6/126 , C07C37/07 , C07C37/08 , C07C45/53 , C07C407/00 , C07C409/14 , C07C2521/04 , C07C2521/06 , C07C2523/44 , C07C2529/74 , C07C2529/76 , C07C2601/14 , Y02P20/52 , C07C13/28 , C07C49/403 , C07C39/04
摘要: In a process for producing cyclohexylbenzene, benzene and hydrogen are contacted under hydroalkylation conditions with a catalyst system comprising a MCM-22 family molecular sieve and at least one hydrogenation metal. The conditions comprise a temperature of about 140° C. to about 175° C., a pressure of about 135 psig to about 175 psig (931 kPag to 1207 kPag), a hydrogen to benzene molar ratio of about 0.30 to about 0.65 and a weight hourly space velocity of benzene of about 0.26 to about 1.05 hr−1.
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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:US07910778B2
公开(公告)日:2011-03-22
申请号:US12665154
申请日:2008-07-11
IPC分类号: C07C45/27 , C07C27/08 , C07C2/68 , C07C15/067
CPC分类号: C07C6/126 , C07C2/74 , C07C37/07 , C07C37/08 , C07C45/53 , C07C407/00 , C07C409/14 , C07C2521/04 , C07C2521/06 , C07C2523/06 , C07C2523/14 , C07C2523/44 , C07C2523/46 , C07C2523/75 , C07C2523/755 , C07C2601/14 , Y02P20/52 , C07C13/28 , C07C49/403 , C07C39/04
摘要: In a process for producing cyclohexylbenzene, benzene and hydrogen are contacted with a catalyst under hydroalkylation conditions to produce an effluent containing cyclohexylbenzene. The catalyst comprises a composite of a molecular sieve, an inorganic oxide different from said molecular sieve and at least one hydrogenation metal, wherein at least 50 wt % of said hydrogenation metal is supported on the inorganic oxide.
摘要翻译: 在生产环己基苯的方法中,苯和氢在加氢烷基化条件下与催化剂接触以产生含有环己基苯的流出物。 催化剂包括分子筛,不同于所述分子筛的无机氧化物和至少一种氢化金属的复合物,其中至少50wt%的所述氢化金属负载在无机氧化物上。
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公开(公告)号:US07906685B2
公开(公告)日:2011-03-15
申请号:US12601572
申请日:2008-08-12
IPC分类号: C07C45/27 , C07C27/08 , C07C2/68 , C07C15/067
摘要: In a process for producing cyclohexylbenzene, benzene and hydrogen are fed to at least one reaction zone. The benzene and hydrogen are then contacted in the at least one reaction zone under hydroalkylation conditions with a catalyst system comprising a molecular sieve having an X-ray diffraction pattern including d-spacing maxima at 12.4±0.25, 6.9±0.15, 3.57±0.07 and 3.42±0.07 Angstrom, and at least one hydrogenation metal to produce an effluent containing cyclohexylbenzene. The ratio of the total number of moles of hydrogen fed to said at least one reaction zone to the number of moles of benzene fed to said at least one reaction zone is between 0.4 and 0.9:1.
摘要翻译: 在生产环己基苯的方法中,将苯和氢气进料至至少一个反应区。 然后使苯和氢在加氢烷基化条件下在至少一个反应区中与包含分子筛的催化剂体系接触,所述催化剂体系包含具有12.4±0.25,6.9±0.15,3.57±0.07的d间距最大值的X射线衍射图, 3.42±0.07埃,和至少一种氢化金属,以生产含有环己基苯的流出物。 供给到所述至少一个反应区的氢的总摩尔数与进料到所述至少一个反应区的苯的摩尔数之比为0.4-0.9:1。
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