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公开(公告)号：EP4313348A1
公开(公告)日：2024-02-07
申请号：EP22719394.3
申请日：2022-03-21
发明人： LIU, Yujun , CHEN, Xue , KING, Stephen W. , HASAN, Towhid , RUDDICK, Jerrod , YORK, James , SINGH, Amarnath
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公开(公告)号：EP4157815A2
公开(公告)日：2023-04-05
申请号：EP21734615.4
申请日：2021-05-27
发明人： YU, Wanglin , BRAMMER, Michael A. , DEMAIO-TURNER, Sally , KU, Sung-Yu , HOOK, Bruce D. , SHI, Haifeng , YANG, Jin , LIU, Yujun , JOHNSON, Jeff
IPC分类号： C07C43/11 , C07C31/125 , C07C29/141 , C07C45/45 , C07C45/50 , C07C47/02 , C07C47/21
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公开(公告)号：EP3233248A1
公开(公告)日：2017-10-25
申请号：EP15802241.8
申请日：2015-11-09
CPC分类号： C08J11/02 , B01D53/1425 , B01D53/1487 , B01D53/1493 , B01D2252/205 , B01D2256/24 , B01D2257/2066 , C07C7/11 , Y02P20/154 , C07C11/04
摘要： Disclosed herein is a system for recovering olefins from a vent stream comprising an absorber; and a stripper; where the absorber and the stripper are in a recycle loop; and where the absorber is operative to treat a vent stream with a solvent to remove more than 99 wt% of a halogenated by-product contained in the vent stream and to recover 90 to 95 wt% of olefin molecules present in the vent stream; and where the stripper is operative to remove more than 99 wt% of the halogenated by-products present in the solvent; and where the solvent is recycled to the absorber.
摘要翻译： 本文公开了用于从包含吸收剂的排出流中回收烯烃的系统; 和汽提器; 吸收器和汽提器在循环回路中; 并且其中吸收器可操作以用溶剂处理排出物流以除去排出流中包含的超过99重量％的卤化副产物并回收存在于排出流中的90至95重量％的烯烃分子; 并且其中剥离器可操作以除去存在于溶剂中的超过99重量％的卤化副产物; 并且溶剂被循环到吸收器中。
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公开(公告)号：EP4157816A1
公开(公告)日：2023-04-05
申请号：EP21733653.6
申请日：2021-05-27
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5.发明公开NOVEL CARBON MOLECULAR SIEVE AND PELLET COMPOSITIONS USEFUL FOR C2-C3 ALKANE/ALKENE SEPARATIONS 审中-公开为C2-C3烷烃/烯烃分离新颖的和球团碳分子筛组合物
公开(公告)号：EP2978524A1
公开(公告)日：2016-02-03
申请号：EP14722478.6
申请日：2014-03-24
发明人： LIU, Junqiang , BRAYDEN, Mark K. , CALVERLEY, Edward M. , LAKSO, Steven R. , LIU, Yujun , MARTINEZ, Marcos V.
CPC分类号： B01J20/20 , B01D53/0462 , B01D53/047 , B01D2253/102 , B01D2253/116 , B01D2253/304 , B01D2257/7022 , B01J20/28042 , B01J20/28078 , B01J20/28085 , B01J20/28092 , B01J20/3007 , B01J20/3028 , B01J20/3042 , B01J20/3078 , C01B31/00 , C01B31/02 , C01B31/08 , C01B32/00 , C01B32/05 , C01B32/30 , C01P2004/54 , C01P2004/60 , C01P2006/16 , C01P2006/17 , C07C7/12
摘要： A novel microporous carbon molecular sieve may be used as the basis for carbon adsorbent pellets that have discrete areas of carbonized binder and of carbonized precursor, macropores having an average pore diameter greater than or equal to 1 micrometer and a total macroporosity of at least 30 percent, both as measured by mercury porosimetry, and micropores that are capable of selectively admitting a C2-C3 alkene and excluding a C2-C3 alkane, and a total microporosity ranging from 10 percent to 30 percent. The pellets may be prepared by pyrolyzing a pellet structure comprising a carbon forming, non-melting binder and a non-porous gel type sulfonated polystyrene precursor at a temperature ranging from 500° C. to 1000° C., under an inert atmosphere and other conditions suitable to form the described pellets. The pellets are particularly useful in pressure swing and temperature swing adsorption processes to separate C2-C3 alkane/alkene mixtures.
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公开(公告)号：EP4340994A1
公开(公告)日：2024-03-27
申请号：EP21940145.2
申请日：2021-05-19
发明人： JIANG, Qi , OHBA, Kaoru , LIU, Yujun
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公开(公告)号：EP4157977A1
公开(公告)日：2023-04-05
申请号：EP21735469.5
申请日：2021-05-26
发明人： YU, Wanglin , BRAMMER, Michael A. , DEMAIO-TURNER, Sally , KU, Sung-Yu , YANG, Jin , SHI, Haifeng , HOOK, Bruce D. , LIU, Yujun , JOHNSON, Jeff
IPC分类号： C11D1/14 , C11D1/29 , C11D1/72 , C07C31/125
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公开(公告)号：EP4341240A1
公开(公告)日：2024-03-27
申请号：EP21940146.0
申请日：2021-05-19
发明人： JIANG, Qi , OHBA, Kaoru , LIU, Yujun , KIM, Jongcheol , CHEN, Xue , MU, Li
IPC分类号： C07C209/84
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公开(公告)号：EP4132903A1
公开(公告)日：2023-02-15
申请号：EP20930126.6
申请日：2020-04-08
发明人： JIANG, Qi , LIU, Yujun , OHBA, Kaoru , KIM, Jongcheol , CHEN, Xue , MU, Li , MU, Jianhai , KING, Stephen, W.
IPC分类号： C07C211/63 , C07C213/10
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10.发明公开
公开(公告)号：EP2994220A1
公开(公告)日：2016-03-16
申请号：EP14727124.1
申请日：2014-04-22
发明人： NAIR, Sankar , KIM, Seok Jhin , LIU, Yujun , PENDERGAST, John G. , DIXIT, Ravindra S. , MOORE, Jason S.
IPC分类号： B01D67/00 , B01J29/08 , B01J29/40 , B01J29/70 , B01D69/02 , B01D71/02 , B01J35/06 , C01B39/08
CPC分类号： B01J35/065 , B01D67/0051 , B01D67/0093 , B01D69/02 , B01D71/028 , B01D2323/08 , B01D2323/10 , B01D2325/42 , B01J20/186 , B01J20/28035 , B01J20/3085 , B01J29/085 , B01J29/405 , B01J29/7053 , B01J2229/186 , C01B39/08 , C01B39/082 , C01B39/40
摘要： Effect ion-exchange of an alpha-alumina supported zeolite (e.g. a MFI zeolite, an LTA zeolite or a FAU zeolite) membrane, which process comprises: a) placing the membrane, which has a first surface and a spaced apart second surface, the first and second surfaces defining therebetween the membrane, in an ion exchange apparatus such that the first surface is in contact with an ion exchange solution and the second surface is in contact with a vapor space that is connected to a source of reduced pressure; b) actuating the source of reduced pressure to create a pressure differential between the first and second membrane surfaces of at least 0.4 atmosphere (0.405×105 pascals); and c) maintaining the pressure differential under ion exchange conditions for a period of time sufficient to effect exchange of an ion contained in the ion exchange solution with an ion in the zeolite membrane in an amount that is greater than an amount of ion exchange attained using an apparatus that places the second surface in contact with a liquid solvent that is at a pressure of at least one atmosphere (1.013×105 pascals) and the first surface in contact with the ion exchange solution at a pressure of at least two atmospheres (2.026×105 pascals) so as to establish a pressure differential between the two surfaces of at least one atmosphere (1.013×105 pascals), maintaining the pressure differential for the same period of time, and using the same ion exchange membrane, ion exchange solution and ion exchange temperature, the greater amount of ion exchange yielding an improved ion exchange membrane that a ratio of the ion that entered the membrane from the solution to the ion that left the membrane that is greater than that of the ion exchanged membrane prepared with the second surface in contact with the liquid solvent.
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