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公开(公告)号：US07524995B1
公开(公告)日：2009-04-28
申请号：US12138002
申请日：2008-06-12
申请人： Stephen M. Tieri , John Joseph Hagedom , James Arnold Schultz , Tiberiu M. Leib , Susanne Hawthorne Wolff , Sourav K. Sengupta , Gregory Paul Shankwitz
发明人： Stephen M. Tieri , John Joseph Hagedom , James Arnold Schultz , Tiberiu M. Leib , Susanne Hawthorne Wolff , Sourav K. Sengupta , Gregory Paul Shankwitz
IPC分类号： C07C29/145
CPC分类号： C07C29/145 , C07C31/38
摘要： A continuous process for producing hexafluoroisopropanol is provided which comprises contacting hexafluoroacetone with hexafluoroisopropanol and hydrogen to produce a liquid feed stream; introducing the liquid feed stream to a reactor containing an immobilized hydrogenation catalyst to convert the hexafluoroacetone to hexafluoroisopropanol and provide a product stream; and recovering at least a portion of the hexafluoroisopropanol from the product stream. Preferably a portion of the product stream is recycled. The reactor can be a packed bed or stirred tank reactor.
摘要翻译： 提供生产六氟异丙醇的连续方法，其包括使六氟丙酮与六氟异丙醇和氢接触以产生液体进料流; 将液体进料流引入含有固定化氢化催化剂的反应器中以将六氟丙酮转化为六氟异丙醇并提供产物流; 并从产物流中回收至少一部分六氟异丙醇。 优选地，一部分产物流被再循环。 反应器可以是填充床或搅拌釜反应器。
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2.发明授权Catalytic cracking apparatus using regenerator with multiple catalyst outlets 失效催化裂化装置使用多个催化剂出口的再生器
公开(公告)号：US5427745A
公开(公告)日：1995-06-27
申请号：US564254
申请日：1990-08-08
申请人： Tiberiu M. Leib , Ajit V. Sapre
发明人： Tiberiu M. Leib , Ajit V. Sapre
CPC分类号： B01J8/18 , B01J8/0015 , C10G11/182
摘要： An improved process and apparatus are disclosed for fluidized catalytic cracking of hydrocarbons using a cross-flow or swirl type catalyst regenerator. Instead of a single catalyst withdrawal outlet for regenerated catalyst, multiple catalyst withdrawal points are provided. Use of multiple catalyst outlets, or a continuous radial catalyst outlet, greatly reduces stagnant regions in the bed.
摘要翻译： 公开了一种改进的方法和装置，其用于使用交叉流或涡流型催化剂再生器的烃的流化催化裂化。 代替用于再生催化剂的单个催化剂排出口，提供多个催化剂取出点。 多个催化剂出口或连续的径向催化剂出口的使用大大减少了床中的停滞区域。
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公开(公告)号：US4980048A
公开(公告)日：1990-12-25
申请号：US431953
申请日：1989-11-06
申请人： Tiberiu M. Leib , Ajit V. Sapre
发明人： Tiberiu M. Leib , Ajit V. Sapre
CPC分类号： B01J8/0015 , C10G11/182
摘要： An improved process and apparatus are disclosed for fluidized bed catalyst regeneration in a cross-flow type regenerator. A baffled coked catalyst inlet located within the dense bed of catalyst disperses and distributes coked catalyst flow in a direction generally normal to the direction of flow in the catalyst inlet. The baffle significantly reduces the stagnant regions in the bed.
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公开(公告)号：US4994424A
公开(公告)日：1991-02-19
申请号：US431949
申请日：1989-11-06
申请人： Tiberiu M. Leib , Ajit V. Sapre
发明人： Tiberiu M. Leib , Ajit V. Sapre
CPC分类号： B01J8/0015 , C10G11/182 , Y10S502/515
摘要： An improved process and apparatus are disclosed for fluidized catalytic cracking of hydrocarbons using a swirl type catalyst regenerator. Multiple, symmetrically spaced spent catalyst inlets are provided for addition of coked catalyst to the regenerator. Preferable a single catalyst outlet, for withdrawal of regenerated catalyst, is provided in the center of the regenerator. Use of multiple symmetrical inlets and a central catalyst outlet greatly reduce stagnant regions in the bed.
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5.发明授权Hydrofluorocarbon production using heat carriers in high temperature hydrogenolysis 失效在高温氢解中使用热载体的氢氟碳化合物生产
公开(公告)号：US5841008A
公开(公告)日：1998-11-24
申请号：US836954
申请日：1997-05-22
CPC分类号： C07C17/23
摘要： This invention relates to a process for the hydrogenolysis of halogenated hydrocarbons containing fluorine together with chlorine and/or bromine.
摘要翻译： PCT No.PCT / US95 / 15105 Sec。 371日期：1997年5月22日 102（e）日期1997年5月22日PCT 1997年11月15日PCT公布。 公开号WO96 / 16009 日期：1996年5月30日本发明涉及含氟和/或溴的卤代烃氢解的方法。
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公开(公告)号：US5205993A
公开(公告)日：1993-04-27
申请号：US808953
申请日：1991-12-13
申请人： Tiberiu M. Leib , Ajit V. Sapre
发明人： Tiberiu M. Leib , Ajit V. Sapre
CPC分类号： B01J8/0015 , C10G11/182
摘要： An process and apparatus are disclosed for fluidized bed catalyst regeneration in a cross-flow type regenerator. A baffled coked catalyst inlet located within the dense bed of catalyst disperses and distributes coked catalyst flow in a direction generally normal to the direction of flow in the catalyst inlet. The baffle significantly reduces the stagnant regions in the bed.
摘要翻译： 公开了一种在交叉流型再生器中用于流化床催化剂再生的方法和装置。 位于催化剂致密床内的带挡板的焦化催化剂入口分散并在大致垂直于催化剂入口流动方向的方向上分配焦化催化剂流。 挡板显着减少了床上停滞的区域。
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公开(公告)号：US5062944A
公开(公告)日：1991-11-05
申请号：US431952
申请日：1989-11-06
申请人： Tiberiu M. Leib , Ajit V. Sapre
发明人： Tiberiu M. Leib , Ajit V. Sapre
CPC分类号： B01J8/18 , B01J8/0015 , C10G11/182
摘要： An improved process and apparatus are disclosed for fluidized catalytic cracking of hydrocarbons using a cross-flow or swirl type catalyst regenerator. Instead of a single catalyst withdrawal outlet for regenerated catalyst, multiple catalyst withdrawal points are provided. Use of multiple catalyst outlets, or a continuous radial catalyst outlet, greatly reduces stagnant regions in the bed.
摘要翻译： 公开了一种改进的方法和装置，其用于使用交叉流或涡流型催化剂再生器的烃的流化催化裂化。 代替用于再生催化剂的单个催化剂排出口，提供多个催化剂取出点。 多个催化剂出口或连续的径向催化剂出口的使用大大减少了床中的停滞区域。
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公开(公告)号：US4684756A
公开(公告)日：1987-08-04
申请号：US858620
申请日：1986-05-01
申请人： W. Rodman Derr, Jr. , William E. Garwood , James C. Kuo , Tiberiu M. Leib , Donald M. Nace , Samuel A. Tabak
发明人： W. Rodman Derr, Jr. , William E. Garwood , James C. Kuo , Tiberiu M. Leib , Donald M. Nace , Samuel A. Tabak
CPC分类号： C10L1/06 , C07C1/0485 , C10G2/32 , C10L1/04 , C10G2300/1022
摘要： The waxy liquid phase of an oil suspension of Fischer-Tropsch catalyst containing dissolved wax is separated out and the wax is converted by hydrocracking, dewaxing or by catalytic cracking with a low activity catalyst to provide a highly olefinic product which may be further converted to premium quality gasoline and/or distillate fuel.
摘要翻译： 分离含有溶解蜡的费 - 托催化剂的油悬浮液的蜡状液相，通过加氢裂化，脱蜡或用低活性催化剂进行催化裂化来转化蜡，以提供可进一步转化为优质的高烯烃产物 优质汽油和/或馏出燃料。
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