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公开(公告)号：US08383538B2
公开(公告)日：2013-02-26
申请号：US13399285
申请日：2012-02-17
申请人： Manuela Serban , Kurt M. Vanden Bussche , Alakananda Bhattacharyya , Luigi Laricchia , John P. Brady , David N. Myers
发明人： Manuela Serban , Kurt M. Vanden Bussche , Alakananda Bhattacharyya , Luigi Laricchia , John P. Brady , David N. Myers
IPC分类号： C10G21/28
CPC分类号： C10G21/06 , B01D11/0446 , B01D11/0488 , B01D11/0492 , C10G21/28 , C10G2300/1055 , C10G2300/301 , C10G2300/805
摘要： One exemplary embodiment can be an apparatus for treating a hydrocarbon stream having one or more compounds with a boiling point of about 140° to about 450° C. The apparatus can include an extraction zone and a regeneration zone. The extraction zone can include at least one settler. Each settler can have a height and a length. Typically the length is greater than the height. Also, the settler can form a boot, which can be adapted to receive a feed at one end. The regeneration zone may include a regenerator for an ionic liquid. The regenerator can include a column adapted to provide a regenerated ionic liquid to the extraction zone.
摘要翻译： 一个示例性实施方案可以是用于处理具有沸点为约140℃至约450℃的一种或多种化合物的烃流的设备。该设备可以包括提取区和再生区。 提取区可以包括至少一个沉降器。 每个定居者都可以有一个高度和一个长度。 通常长度大于高度。 此外，定居者可以形成一个引导件，它可以适应于在一端接受饲料。 再生区可以包括用于离子液体的再生器。 再生器可以包括适于向再提取区提供再生离子液体的柱。
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公开(公告)号：US08127938B2
公开(公告)日：2012-03-06
申请号：US12416065
申请日：2009-03-31
申请人： David Nathan Myers , Manuela Serban , Kurt M. Vanden Bussche , Alakananda Bhattacharyya , Luigi Laricchia , John Patrick Brady
发明人： David Nathan Myers , Manuela Serban , Kurt M. Vanden Bussche , Alakananda Bhattacharyya , Luigi Laricchia , John Patrick Brady
IPC分类号： C10G21/28
CPC分类号： C10G21/06 , B01D11/0446 , B01D11/0488 , B01D11/0492 , C10G21/28 , C10G2300/1055 , C10G2300/301 , C10G2300/805
摘要： One exemplary embodiment can be an apparatus for treating a hydrocarbon stream having one or more compounds with a boiling point of about 140-about 450° C. The apparatus can include an extraction zone and a regeneration zone. The extraction zone can include at least one settler. Each settler can have a height and a length. Typically the length is greater than the height. Also, the settler can form a boot, which can be adapted to receive a feed at one end. The regeneration zone may include a regenerator for an ionic liquid. The regenerator can include a column adapted to provide a regenerated ionic liquid to the extraction zone.
摘要翻译： 一个示例性实施方案可以是用于处理具有一种或多种沸点为约140-约450℃的化合物的烃流的装置。该装置可包括萃取区和再生区。 提取区可以包括至少一个沉降器。 每个定居者都可以有一个高度和一个长度。 通常长度大于高度。 此外，定居者可以形成一个引导件，它可以适应于在一端接受饲料。 再生区可以包括用于离子液体的再生器。 再生器可以包括适于向再提取区提供再生离子液体的柱。
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公开(公告)号：US08608952B2
公开(公告)日：2013-12-17
申请号：US12945786
申请日：2010-11-12
申请人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
发明人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
CPC分类号： C10G21/24 , C10G21/28 , C10G33/04 , C10G2300/1033 , C10G2300/203 , C10G2300/4081 , C10G2300/805
摘要： A process for de-acidifying a hydrocarbon feed includes contacting the hydrocarbon feed containing an organic acid with a feed-immiscible phosphonium ionic liquid to produce a hydrocarbon and feed-immiscible phosphonium ionic liquid mixture and separating the mixture to produce a hydrocarbon effluent having a reduced organic acid content relative to the hydrocarbon feed. Optionally, a de-emulsifier is added to at least one of the contacting and separating steps.
摘要翻译： 用于使烃进料脱酸的方法包括将含有机酸的烃进料与进料不混溶的鏻离子液体接触以产生烃和进料不混溶的鏻离子液体混合物，并分离混合物以产生具有还原的 有机酸含量相对于烃进料。 任选地，将去乳化剂加入到至少一个接触和分离步骤中。
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4.发明授权Simultaneous warm gas desulfurization and complete CO-shift for improved syngas cleanup 有权同时进行暖气脱硫和完全合作，改善合成气净化公开(公告)号：US08940660B2
公开(公告)日：2015-01-27
申请号：US12328488
申请日：2008-12-04
IPC分类号： B01J23/00 , C07C1/02 , B01D53/56 , C01B3/12 , C01B3/16 , C01B3/56 , B01J8/02 , B01J8/04 , B01J20/02 , B01J20/08 , B01J35/00 , C10J3/46 , C10K1/00 , C10K3/04 , B01J23/86
CPC分类号： C01B3/56 , B01D2257/304 , B01D2257/308 , B01J8/02 , B01J8/04 , B01J20/0225 , B01J20/08 , B01J23/868 , B01J35/0006 , B01J2208/025 , C01B3/16 , C01B2203/045 , C01B2203/0485 , C10J3/466 , C10J2300/0959 , C10J2300/1618 , C10K1/004 , C10K3/04 , Y02E20/18 , Y02E60/36 , Y02P20/52
摘要： The present invention involves both separated beds (or physical mixture) and a process for treating a fuel gas comprising sending the fuel gas to a separated bed (or physical mixture), in which the separated beds comprise a first bed of a sulfur sorbent and a second bed of a water gas shift catalyst (a physical mixture of a sulfur sorbent and a water gas shift catalyst). The process comprises first sending the fuel gas to the first bed to remove sulfur compounds from said fuel gas and then the fuel gas goes to the second bed to undergo a water gas shift reaction in which carbon monoxide is converted to carbon dioxide and water is converted to hydrogen. (or sending the fuel gas simultaneously to the physical mixture to remove simultaneously the sulfur compounds and to react CO with water to CO2 and hydrogen).
摘要翻译： 本发明涉及分离的床（或物理混合物）和用于处理燃料气体的方法，包括将燃料气体送入分离的床（或物理混合物），其中分离的床包含硫吸附剂的第一床和 第二床的水煤气变换催化剂（硫吸附剂和水煤气变换催化剂的物理混合物）。 该方法包括首先将燃料气体发送到第一床以从所述燃料气体中除去硫化合物，然后燃料气体进入第二床以进行水煤气变换反应，其中将一氧化碳转化为二氧化碳并转化水 到氢。 （或将燃料气体同时发送到物理混合物以同时除去硫化合物并使CO与水反应成CO 2和氢）。
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公开(公告)号：US08608950B2
公开(公告)日：2013-12-17
申请号：US12945765
申请日：2010-11-12
申请人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
发明人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
CPC分类号： C10G21/06 , C10G21/12 , C10G21/20 , C10G21/24 , C10G21/28 , C10G55/02 , C10G57/00 , C10G2300/107 , C10G2300/1077 , C10G2300/205 , C10G2300/206 , C10G2300/4081 , C10G2300/44 , C10G2300/805
摘要： A process for removing a metal from a resid feed includes contacting the resid feed comprising the metal with a resid-immiscible ionic liquid to produce a resid and resid-immiscible ionic liquid mixture, and separating the mixture to produce a resid effluent having a reduced metal content relative to the resid feed.
摘要翻译： 用于从渣油中除去金属的方法包括将包含金属的残渣进料与残渣不混溶的离子液体接触以产生渣油和残渣不混溶的离子液体混合物，并分离混合物以产生具有还原金属的残渣流出物 相对于残留饲料的内容。
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公开(公告)号：US07759282B2
公开(公告)日：2010-07-20
申请号：US12328503
申请日：2008-12-04
IPC分类号： B01J23/00
CPC分类号： C01G53/00 , B01D53/8603 , B01D2255/20753 , B01D2257/306 , B01J23/002 , B01J23/007 , B01J23/755 , B01J35/1019 , B01J35/1038 , B01J35/1061 , C01B3/48 , C01B2203/0283 , C01B2203/0415 , C01B2203/0475 , C01B2203/0485 , C01B2203/1058 , C01P2002/54 , C01P2006/12 , C01P2006/14 , C01P2006/16 , C10J2300/1618 , C10K1/00 , C10K3/04 , Y02P20/52
摘要： The present invention involves a process and materials for simultaneous desulfurization and water gas shift of a gaseous stream comprising contacting the gas stream with a nickel aluminate catalyst. The nickel aluminate catalyst is preferably selected from the group consisting of Ni2xAl2O2x+3, Ni(2−y)Ni0yAl2O(5−y), Ni(4−y)Ni0yAl2O(7−y), Ni(6−y)Ni0yAl2O(9−y), and intermediates thereof, wherein x≧0.5 and 0.01≦y≦2. Preferably, x is between 1 and 3. More preferably, the nickel containing compound further comprises Ni2xAl2O2x+3−zSz wherein 0≦z≦2x.
摘要翻译： 本发明涉及用于气态物流的同时脱硫和水煤气变换的方法和材料，包括使气流与铝酸镍催化剂接触。 镍酸镍催化剂优选选自Ni2xAl2O2x + 3，Ni（2-y）Ni0yAl2O（5-y），Ni（4-y）NiOyAl2O（7-y），Ni（6-y）Ni0Al2O2O 9-y）及其中间体，其中x≥0.5和0.01＆amp; nlE; y＆nlE; 2。 优选地，x在1和3之间。更优选地，含镍化合物还包含Ni 2 x Al 2 O x + 3-z S z，其中0和n 1; z和n 1; 2x。
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公开(公告)号：US20100150805A1
公开(公告)日：2010-06-17
申请号：US12555365
申请日：2009-09-08
IPC分类号： B01D53/48 , C07C5/333 , C07C5/05 , C07D301/03 , C07D301/10 , C07C57/03 , C07C51/36
CPC分类号： C07D301/03 , B01D53/8603 , B01D2255/206 , C07C5/05 , C07C5/09 , C07C5/3337 , C07C29/147 , C07C51/16 , C07C2521/04 , C07C2521/06 , C07C2521/12 , C07C2523/10 , C07C2523/20 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07D301/10 , C10G45/34 , Y02P20/52 , C07C11/06 , C07C11/04 , C07C31/207 , C07C57/04
摘要： This invention involves highly porous, stable metal oxide felt materials that are used as catalytic supports for a number of different applications including dehydrogenation of light paraffins to olefins, selective hydrogenation of dienes to olefins, hydrogenation of carboxylic acids, oxidation or ammoxidation reactions, epoxidation of light olefins and removal of sulfur compounds from gas streams.
摘要翻译： 本发明涉及高度多孔，稳定的金属氧化物毡材料，其用作多种不同应用的催化载体，包括将轻链烷烃脱氢成烯烃，将烯烃选择性氢化成烯烃，羧酸氢化，氧化或氨氧化反应，环氧化 轻质烯烃和从气流中除去硫化合物。
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8.发明申请Simultaneous Warm Gas Desulfurization and CO-Shift for Improved Syngas Cleanup 有权同时进行暖气脱硫和CO转化，改善合成气净化公开(公告)号：US20100143229A1
公开(公告)日：2010-06-10
申请号：US12328501
申请日：2008-12-04
IPC分类号： B01D53/48
CPC分类号： B01D53/8603 , B01D2255/20753 , B01D2257/306 , B01J20/0225 , B01J20/08 , B01J23/002 , B01J23/007 , B01J23/755 , B01J35/1019 , B01J35/1038 , B01J35/1061 , B01J37/031 , C01B3/16 , C01B3/48 , C01B2203/0283 , C01B2203/0415 , C01B2203/045 , C01B2203/0475 , C01B2203/0485 , C01G53/00 , C01G53/006 , C01P2002/22 , C01P2006/12 , C01P2006/14 , C01P2006/16 , Y02P20/52
摘要： The present invention involves a process and materials for simultaneous desulfurization and water gas shift of a gaseous stream comprising contacting the gas stream with a nickel aluminate catalyst. The nickel aluminate catalyst is preferably selected from the group consisting of Ni2xAl2O2x+3, Ni(2−y)Ni0yAl2O(5−y), Ni(4−y)Ni0yAl2O(7−y), Ni(6−y)Ni0yAl2O(9−y), and intermediates thereof, wherein x≧0.5 and 0.01≦y≦2. Preferably, x is between 1 and 3. More preferably, the nickel containing compound further comprises Ni2xAl2O2x+3−zSz wherein 0≧z≧2x.
摘要翻译： 本发明涉及用于气态物流的同时脱硫和水煤气变换的方法和材料，包括使气流与铝酸镍催化剂接触。 镍酸镍催化剂优选选自Ni2xAl2O2x + 3，Ni（2-y）Ni0yAl2O（5-y），Ni（4-y）NiOyAl2O（7-y），Ni（6-y）Ni0Al2O2O 9-y）及其中间体，其中x≥0.5和0.01＆amp; nlE; y＆nlE; 2。 优选地，x在1和3之间。更优选地，含镍化合物还包含Ni2xAl2O2x + 3-zSz，其中0≥z≥2x。
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公开(公告)号：US08608943B2
公开(公告)日：2013-12-17
申请号：US12945253
申请日：2010-11-12
申请人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Joseph A. Kocal , Warren K. Bennion
发明人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Joseph A. Kocal , Warren K. Bennion
CPC分类号： C10G21/28 , C10G21/24 , C10G55/06 , C10G67/02 , C10G2300/1074 , C10G2300/202 , C10G2300/4081 , C10G2300/805 , C10G2400/06
摘要： A process for removing a nitrogen compound from a vacuum gas oil feed includes contacting the vacuum gas oil feed comprising the nitrogen compound with a VGO-immiscible phosphonium ionic liquid to produce a vacuum gas oil and VGO-immiscible phosphonium ionic liquid mixture, and separating the mixture to produce a vacuum gas oil effluent having a reduced nitrogen content relative to the vacuum gas oil feed.
摘要翻译： 从真空瓦斯油进料中除去氮化合物的方法包括将包含氮化合物的减压瓦斯油进料与VGO不混溶的鏻离子液体接触以产生真空瓦斯油和VGO不混溶的鏻离子液体混合物， 混合物以产生相对于减压瓦斯油进料具有降低的氮含量的减压瓦斯油流出物。
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公开(公告)号：US08580107B2
公开(公告)日：2013-11-12
申请号：US12945303
申请日：2010-11-12
申请人： Alakananda Bhattacharyya , Manuela Serban , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Joseph A. Kocal , Warren K. Bennion
发明人： Alakananda Bhattacharyya , Manuela Serban , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Joseph A. Kocal , Warren K. Bennion
CPC分类号： C10G21/28 , C10G21/20 , C10G21/24 , C10G21/27 , C10G53/06 , C10G2300/1074 , C10G2300/202
摘要： A process for removing a sulfur compound from a vacuum gas oil feed includes contacting the vacuum gas oil feed comprising the sulfur compound with a VGO-immiscible ionic liquid to produce a vacuum gas oil and VGO-immiscible ionic liquid mixture, and separating the mixture to produce a vacuum gas oil effluent having a reduced sulfur content relative to the vacuum gas oil feed.
摘要翻译： 从减压瓦斯油进料中除去硫化合物的方法包括将包含硫化合物的减压瓦斯油进料与VGO不混溶的离子液体接触以产生真空瓦斯油和VGO不混溶的离子液体混合物，并将该混合物分离成 产生相对于减压瓦斯油进料具有降低的硫含量的减压瓦斯油流出物。
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