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公开(公告)号：US20160145511A1
公开(公告)日：2016-05-26
申请号：US14932232
申请日：2015-11-04
Applicant: Xiaochun Xu , Bradley R. Fingland , Keith Wilson , Doron Levin , Stuart L. Soled , Sabato Miseo , Joseph E. Baumgartner , Ajit B. Dandekar
Inventor： Xiaochun Xu , Bradley R. Fingland , Keith Wilson , Doron Levin , Stuart L. Soled , Sabato Miseo , Joseph E. Baumgartner , Ajit B. Dandekar
IPC: C10G69/02 , C10M101/02 , C10G67/04
CPC classification number: C10G45/50 , B01J23/882 , B01J23/883 , B01J23/888 , B01J23/8885 , B01J37/20 , C10G35/06 , C10G45/08 , C10G47/06 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G67/04 , C10G69/02 , C10G69/08 , C10G2300/1048 , C10G2300/202 , C10G2300/301 , C10G2400/00 , C10M101/02
Abstract: Methods are provided for hydroprocessing a feed (such as hydrotreating, hydrocracking, or hydrofining a feed) to generate a product with a reduced or minimized aromatics content relative to the severity of the hydroprocessing conditions. In some types of hydroprocessing applications, it can be desirable to select the severity of hydroprocessing conditions to achieve a desired level of removal for sulfur, a desired level for removal of nitrogen, and/or a desired level for increasing the viscosity index of a feed. The severity for heteroatom removal and/or viscosity index uplift can also correspond to an amount of conversion of a feed to lower boiling point products, so the lowest severity conditions suitable for achieving a product quality can be desirable. By improving the aromatics saturation during hydroprocessing, the severity of subsequent aromatics saturation processes can be reduced.
Abstract translation: 提供用于加氢处理饲料（例如加氢处理，加氢裂化或加氢精制饲料）以产生相对于加氢处理条件的严重性降低或最小化芳烃含量的产物。 在一些类型的加氢处理应用中，可以期望选择加氢处理条件的严重性以达到期望的硫去除水平，除去氮的所需水平和/或用于提高进料粘度指数的期望水平 。 杂原子除去和/或粘度指数升高的严重程度也可以对应于进料到低沸点产物的转化量，因此适合于获得产品质量的最低苛刻度条件是可取的。 通过改善加氢处理过程中的芳族化合物饱和度，可以降低随后的芳烃饱和过程的严重性。
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公开(公告)号：US08586809B2
公开(公告)日：2013-11-19
申请号：US13183009
申请日：2011-07-14
Applicant: James H. Beech, Jr. , Julia E. Steinheider , Doron Levin , Selma S. Lawrence
Inventor： James H. Beech, Jr. , Julia E. Steinheider , Doron Levin , Selma S. Lawrence
CPC classification number: C10G25/02 , C10G29/205 , C10G45/54 , C10G45/64 , C10G59/02 , C10G65/04 , C10G2300/1096 , C10G2300/201 , C10G2300/4018 , C10G2400/02 , C10G2400/04 , C10G2400/30
Abstract: A guard bed or absorber is placed upstream of a transalkylation reactor to avoid deposition of halide and/or halogen species on the catalysts in said reactor.
Abstract translation: 保护床或吸收剂放置在烷基转移反应器的上游，以避免卤化物和/或卤素物质沉积在所述反应器中的催化剂上。
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公开(公告)号：US07799956B2
公开(公告)日：2010-09-21
申请号：US11660065
申请日：2005-08-05
Applicant: Jane Chi-ya Cheng , John S. Buchanan , Doron Levin , Michael A. Steckel , Jihad M. Dakka , James P. Stokes , John L. Robbins , Jon E. Stanat , Charles M. Smith , José G. Santiesteban
Inventor： Jane Chi-ya Cheng , John S. Buchanan , Doron Levin , Michael A. Steckel , Jihad M. Dakka , James P. Stokes , John L. Robbins , Jon E. Stanat , Charles M. Smith , José G. Santiesteban
CPC classification number: C07C37/08 , C07C45/53 , C07C409/08 , C07C2529/70 , Y02P20/127 , Y02P20/52 , C07C49/10 , C07C39/04
Abstract: A process for producing phenol and methyl ethyl ketone comprises contacting benzene with a C4 alkylating agent under alkylation conditions with catalyst comprising zeolite beta or 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 to produce an alkylation effluent comprising sec-butylbenzene. The sec-butylbenzene is then oxidized to produce a hydroperoxide and the hydroperoxide is decomposed to produce phenol and methyl ethyl ketone.
Abstract translation: 一种生产苯酚和甲基乙基酮的方法包括在烷基化条件下使苯与C4烷基化剂与包含β沸石的催化剂或具有包含d-间距最大值的X射线衍射图的分子筛在12.4±0.25,6.9±0.15， 3.57±0.07和3.42±0.07埃，以产生包含仲丁基苯的烷基化流出物。 然后将仲丁基苯氧化生成氢过氧化物，氢过氧化物分解生成苯酚和甲基乙基酮。
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公开(公告)号：US07468465B2
公开(公告)日：2008-12-23
申请号：US11141482
申请日：2005-05-31
Applicant: James Clarke Vartuli , Doron Levin , Stephen John McCarthy
Inventor： James Clarke Vartuli , Doron Levin , Stephen John McCarthy
CPC classification number: C07C29/00 , B01J23/002 , B01J23/10 , B01J27/053 , B01J2523/00 , C07C1/20 , C07C29/10 , C07C2523/10 , C07C11/02 , B01J2523/3712 , B01J2523/48 , B01J2523/62 , C07C31/10
Abstract: The invention relates to a method of making Group 3 and Group 4 mixed metal oxide catalyst suitable for the decomposition of ethers to alkenes and alkanols. In an embodiment, it relates to a method of making a cerium-zirconium mixed metal oxide catalyst. In an embodiment, the catalyst made by the process of the invention is used for the production of isopropanol (IPA) from isopropyl ether (IPE).
Abstract translation: 本发明涉及一种制备适合于将醚分解成烯烃和链烷醇的第3族和第4族混合金属氧化物催化剂的方法。 在一个实施方案中，它涉及一种制备铈 - 锆混合金属氧化物催化剂的方法。 在一个实施方案中，由本发明方法制备的催化剂用于从异丙醚（IPE）生产异丙醇（IPA）。
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公开(公告)号：US07326815B2
公开(公告)日：2008-02-05
申请号：US11318731
申请日：2005-12-27
Applicant: Jihad Mohammed Dakka , Doron Levin , Jon Edmond Randolph Stanat
Inventor： Jihad Mohammed Dakka , Doron Levin , Jon Edmond Randolph Stanat
CPC classification number: C07C409/08 , C07C37/08 , C07C45/53 , C07C407/00 , C07C409/10 , C07C49/08 , C07C49/10 , C07C39/04
Abstract: The present invention relates to a process for producing phenol and a ketone of general formula R1COCH2R3 (I), in which R1 and R2 each independently represent an alkyl group having from 1 to 4 carbon atoms, said process comprising: (a) providing an alkylbenzene feedstock comprising (i) an alkylbenzene of general formula (II) in which R1 and R2 have the same meaning as in formula (I) and (ii) at least one structural isomer of said alkylbenzene of formula (II) in an amount of at least 0.7% of the weight of alkylbenzene of formula (II), (b) submitting the alkylbenzene feedstock to oxidation conditions in the presence of oxygen and in the presence of a cyclic imide of formula (III): in which X represents a carbonyl (CO) group or a sulfonyl (SO2) group, n is 0, 1, 2, 3 or 4, R3 is one or several groups selected from a hydrogen atom, a halogen atom, an alkyl group, an alkoxy group, an amino group and R4 is a hydrogen atom, an alkaline metal cation or an alkaline earth metal cation, or in the presence of N,N′,N″-trihydroxyisocyanuric acid (THICA), to produce a product comprising a hydroperoxide of general formula (IV) in which R1 and R2 have the same meaning as in formula (I), and (c) converting the hydroperoxide of formula (IV) into phenol and a ketone of formula (I).
Abstract translation: 本发明涉及一种制备通式为R 1，R 2，R 3，R 3（I）的苯酚和酮的方法，其中R 各个独立地表示具有1至4个碳原子的烷基，所述方法包括：（a）提供烷基苯原料，其包含（i）烷基苯， 其中R 1和R 2 2的通式（II）具有与式（I）中相同的含义和（ii）所述烷基苯的至少一种结构异构体 （II）的量为至少0.7％的式（II）的烷基苯的重量，（b）将烷基苯原料在氧气存在下并在式（III）的环状酰亚胺存在下， ：其中X表示羰基（CO）基团或磺酰基（SO 2 H 2）基团，n为0,1,2,3或4，R 3为一个 或选自氢原子，卤素原子，烷基，烷氧基，氨基的数个基团 并且R 4是氢原子，碱金属阳离子或碱土金属阳离子，或在N，N'，N“ - 三羟基异氰尿酸（THICA）的存在下，产生 包含通式（IV）的氢过氧化物的产物，其中R 1和R 2具有与式（I）中相同的含义，和（c）将氢过氧化物 式（IV）转化成苯酚和式（I）的酮。
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Patent Agency Ranking
公开(公告)号：US20070265476A1
公开(公告)日：2007-11-15
申请号：US11318731
申请日：2005-12-27
Applicant: Jihad Dakka , Doron Levin , Jon Stanat
Inventor： Jihad Dakka , Doron Levin , Jon Stanat
IPC: C07C45/53
CPC classification number: C07C409/08 , C07C37/08 , C07C45/53 , C07C407/00 , C07C409/10 , C07C49/08 , C07C49/10 , C07C39/04
Abstract: The present invention relates to a process for producing phenol and a ketone of general formula R1COCH2R2 (I), in which R1 and R2 each independently represent an alkyl group having from 1 to 4 carbon atoms, said process comprising: (a) providing an alkylbenzene feedstock comprising (i) an alkylbenzene of general formula (II) in which R1 and R2 have the same meaning as in formula (I) and (ii) at least one structural isomer of said alkylbenzene of formula (II) in an amount of at least 0.7% of the weight of alkylbenzene of formula (II), (b) submitting the alkylbenzene feedstock to oxidation conditions in the presence of oxygen and in the presence of a cyclic imide of formula (III): in which X represents a carbonyl (CO) group or a sulfonyl (SO2) group, n is 0, 1, 2, 3 or 4, R3 is one or several groups selected from a hydrogen atom, a halogen atom, an alkyl group, an alkoxy group, an amino group and R4 is a hydrogen atom, an alkaline metal cation or an alkaline earth metal cation, or in the presence of N,N′,N″-trihydroxyisocyanuric acid (THICA), to produce a product comprising a hydroperoxide of general formula (IV) in which R1 and R2 have the same meaning as in formula (I), and (c) converting the hydroperoxide of formula (IV) into phenol and a ketone of formula (I).
Abstract translation: 本发明涉及一种制备通式为R 1，R 2，R 2，R 2（I）的苯酚和酮的方法，其中R 各个独立地表示具有1至4个碳原子的烷基，所述方法包括：（a）提供烷基苯原料，其包含（i）烷基苯， 其中R 1和R 2 2的通式（II）具有与式（I）中相同的含义和（ii）所述烷基苯的至少一种结构异构体 （II）的量为至少0.7％的式（II）的烷基苯的重量，（b）将烷基苯原料在氧气存在下并在式（III）的环状酰亚胺存在下， ：其中X表示羰基（CO）基团或磺酰基（SO 2 H 2）基团，n为0,1,2,3或4，R 3为一个 或选自氢原子，卤素原子，烷基，烷氧基，氨基的数个基团 并且R 4是氢原子，碱金属阳离子或碱土金属阳离子，或在N，N'，N“ - 三羟基异氰尿酸（THICA）的存在下，产生 包含通式（IV）的氢过氧化物的产物，其中R 1和R 2具有与式（I）中相同的含义，和（c）将氢过氧化物 式（IV）转化成苯酚和式（I）的酮。
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公开(公告)号：US07199278B2
公开(公告)日：2007-04-03
申请号：US10903717
申请日：2004-07-30
Applicant: Shun Chong Fung , Doron Levin , Jose Santiesteban , Nicolas P. Coute
Inventor： Shun Chong Fung , Doron Levin , Jose Santiesteban , Nicolas P. Coute
IPC: C07C1/00
CPC classification number: C10G3/62 , C10G3/42 , C10G3/48 , C10G3/49 , C10G3/55 , C10G2300/708 , C10G2400/20 , Y02P30/20 , Y02P30/40 , Y02P30/42
Abstract: A process is described for converting an oxygenate-containing feedstock into one or more olefins in a moving bed reactor system operating in countercurrent flow using a catalyst composition comprising a molecular sieve and at least one metal oxide having an uptake of carbon dioxide at 100° C. of at least 0.03 mg/m2 of the metal oxide.
Abstract translation: 描述了一种用于使用包含分子筛和至少一种在100℃摄入二氧化碳的金属氧化物的催化剂组合物将逆境流反应器中的含氧化合物原料转化为一种或多种烯烃的方法 至少为0.03mg / m 2的金属氧化物。
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公开(公告)号：US07186875B2
公开(公告)日：2007-03-06
申请号：US10909012
申请日：2004-07-30
Applicant: Shun Chong Fung , Doron Levin , Jose Santiesteban , Nicolas P. Coute
Inventor： Shun Chong Fung , Doron Levin , Jose Santiesteban , Nicolas P. Coute
IPC: C07C1/00
CPC classification number: C07C1/20 , C07C2521/04 , C07C2521/06 , C07C2521/10 , C07C2521/16 , C07C2523/02 , C07C2523/10 , C07C2529/70 , C07C2529/85 , Y02P20/584 , C07C11/02
Abstract: A process is described for converting an oxygenate-containing feedstock into one or more olefins in a reactor system including a plurality of fixed bed reactors each containing a catalyst composition comprising a molecular sieve and at least one metal oxide having an uptake of carbon dioxide at 100° C. of at least 0.03 mg/m2 of the metal oxide. Each reactor is sequentially rotated between at least one operating mode, wherein the catalyst composition in the reactor is contacted with the oxygenate-containing feedstock, and a regeneration mode, wherein the catalyst composition in the reactor is contacted with a regeneration medium.
Abstract translation: 描述了一种在含有含氧化合物的原料转化为一种或多种烯烃的方法，该反应器系统包括多个固定床反应器，每个反应器均含有包含分子筛和至少一种二氧化碳吸收量的至少一种金属氧化物， 至少为0.03mg / m 2的金属氧化物。 每个反应器在至少一个操作模式之间依次旋转，其中反应器中的催化剂组合物与含氧化合物的原料接触，再生模式，其中反应器中的催化剂组合物与再生介质接触。
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9.发明申请公开(公告)号：US20060004240A1
公开(公告)日：2006-01-05
申请号：US10883438
申请日：2004-07-01
Applicant: Teng Xu , Nicolas Coute , Kenneth Clem , Doron Levin , James Vartuli
Inventor： Teng Xu , Nicolas Coute , Kenneth Clem , Doron Levin , James Vartuli
IPC: C07C1/00
CPC classification number: C07C1/20 , C07C2529/85 , C10G3/48 , C10G3/49 , C10G3/62 , C10G2300/1088 , C10G2300/703 , C10G2400/20 , Y02P30/42 , C07C11/02
Abstract: This invention relates to processes for converting oxygenates to olefins that include a step of pretreating catalyst, which comprises molecular sieve and one or more active metal oxides of one or more metals, with a hydrocarbon composition to provide an integrated hydrocarbon co-catalyst within the molecular sieve. The combination of molecular sieve and hydrocarbon co-catalyst converts oxygenate to an olefin product with high selectivity to light olefins (i.e., ethylene or propylene, or mixture thereof).
Abstract translation: 本发明涉及将含氧化合物转化为烯烃的方法，包括将包含分子筛和一种或多种金属的一种或多种活性金属氧化物的催化剂预处理成烃类组合物以在分子内提供整合的烃助催化剂的步骤 筛。 分子筛和烃助催化剂的组合将含氧化合物转化为对轻质烯烃（即乙烯或丙烯或其混合物）具有高选择性的烯烃产物。
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公开(公告)号：US10040735B2
公开(公告)日：2018-08-07
申请号：US14696688
申请日：2015-04-27
Applicant: Doron Levin
Inventor： Doron Levin
Abstract: Methods are provided for producing an alcohol-containing pyrolysis product. Initially, a hydrocarbon feedstock is pyrolyzed in the presence of a catalyst system, the catalyst system comprising a basic metal oxide catalyst and a hydrogenation metal catalyst. A pyrolysis product is produced that contains at least one alcohol. The basic metal oxide catalyst is comprised of at least one metal from Group 2, Group 3 including Lanthanides and Actinides, or Group 4 of the Periodic Table of Elements, and the supported hydrogenation metal catalyst is comprised of at least one metal from Group 6 or Groups 8-10 of the Periodic Table of Elements.
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