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1. 发明申请

WO2009051767A1 IMPROVED ENDOTHERMIC HYDROCARBON CONVERSION PROCESS 审中-公开
标题翻译：改进的内热转化过程
公开(公告)号：WO2009051767A1
公开(公告)日：2009-04-23
申请号：PCT/US2008/011835
申请日：2008-10-16
申请人： SUD-CHEMIE INC. , URBANCIC, Michael A. , FRIDMAN, Vladimir
发明人： URBANCIC, Michael A. , FRIDMAN, Vladimir
IPC分类号： C10G11/18 , B01J21/00 , B01J23/00
CPC分类号： B01J23/26 , B01J23/32 , B01J23/72 , B01J35/0006 , C07C5/3332 , C07C2521/02 , C07C2521/04 , C07C2521/08 , C07C2521/10 , C07C2521/12 , C07C2523/02 , C07C2523/04 , C07C2523/06 , C07C2523/26 , C07C2523/34 , C07C2523/72 , C07C2523/889 , C07C2529/04 , Y02P20/52 , C07C11/06 , C07C11/09
摘要： The present invention is an improved cyclic, endothermic hydrogen conversion process and a catalyst bed system for accomplishing the same. Specifically, the improved process comprises reacting a hydrocarbon with a multi-component catalyst bed in such a manner that the temperature within the catalyst bed remains within controlled temperature ranges throughout all stages of the process. The multi-component catalyst bed comprises a reaction-specific catalyst physically mixed with a heat-generating material.
摘要翻译：本发明是一种改进的循环吸热氢转化方法和用于实现其的催化剂床系统。具体地，改进的方法包括使烃与多组分催化剂床反应，使得催化剂床内的温度在整个过程的所有阶段都保持在受控温度范围内。多组分催化剂床包括与发热材料物理混合的反应特异性催化剂。

2. 发明申请

WO2010022318A8 PROCESS TO PURIFY ETHYLENE-CONTAINING OFF-GAS FEED STREAMS 审中-公开
标题翻译：净化含有乙烯含氟气体进料流的方法
公开(公告)号：WO2010022318A8
公开(公告)日：2012-11-15
申请号：PCT/US2009054592
申请日：2009-08-21
申请人： SUED CHEMIE INC , SUN MINGYONG , BRYAN MARTY , BLANKENSHIP STEVE , URBANCIC MICHAEL A
发明人： SUN MINGYONG , BRYAN MARTY , BLANKENSHIP STEVE , URBANCIC MICHAEL A
IPC分类号： C10G11/18 , B01J21/02 , B01J21/06 , B01J23/46 , C10G51/04
CPC分类号： C07C7/167 , B01J23/462 , B01J23/48 , B01J23/60 , B01J23/62 , B01J23/6447 , B01J23/8926 , B01J35/008 , B01J35/1009 , B01J35/1014 , B01J35/1019 , B01J37/20 , Y02P20/52 , C07C11/04
摘要： A method for purification of ethylene-containing feed streams from steam crackers or fluid catalytic crackers (FCC), wherein the feed streams further comprises hydrogen, carbon monoxide, acetylenes, oxygen, nitrogen oxides, is disclosed. The method comprises contacting an ethylene-comprising gas stream with a Ru-based catalyst at reaction temperatures of at least 120°C. The process results in an ethylene- containing feed stream wherein the ethylene is essentially free of acetylenes, nitrogen oxides and oxygen. The purifying of the feed stream occurs with minimal loss of ethylene.
摘要翻译：公开了一种用于从蒸汽裂化器或流化催化裂化器（FCC）净化含乙烯进料流的方法，其中进料流还包含氢气，一氧化碳，乙炔，氧气，氮氧化物。该方法包括在至少120℃的反应温度下使含乙烯的气流与Ru-基催化剂接触。该方法产生含乙烯的进料流，其中乙烯基本上不含乙炔，氮氧化物和氧。进料流的纯化以最小的乙烯损失发生。

3. 发明申请

WO2010022318A3 PROCESS TO PURIFY ETHYLENE-CONTAINING OFF-GAS FEED STREAMS 审中-公开
标题翻译：净化含有乙烯含氟气体进料流的方法
公开(公告)号：WO2010022318A3
公开(公告)日：2010-06-10
申请号：PCT/US2009054592
申请日：2009-08-21
申请人： SUED CHEMIE INC , SUN MINGYONG , BRYAN MARTY , BLANKENSHIP STEVE , URBANCIC MICHAEL A
发明人： SUN MINGYONG , BRYAN MARTY , BLANKENSHIP STEVE , URBANCIC MICHAEL A
IPC分类号： C10G11/18 , B01J21/02 , B01J21/06 , B01J23/46 , C10G51/04
CPC分类号： C07C7/167 , B01J23/462 , B01J23/48 , B01J23/60 , B01J23/62 , B01J23/6447 , B01J23/8926 , B01J35/008 , B01J35/1009 , B01J35/1014 , B01J35/1019 , B01J37/20 , Y02P20/52 , C07C11/04
摘要： A method for purification of ethylene-containing feed streams from steam crackers or fluid catalytic crackers (FCC), wherein the feed streams further comprises hydrogen, carbon monoxide, acetylenes, oxygen, nitrogen oxides, is disclosed. The method comprises contacting an ethylene-comprising gas stream with a Ru-based catalyst at reaction temperatures of at least 120°C. The process results in an ethylene- containing feed stream wherein the ethylene is essentially free of acetylenes, nitrogen oxides and oxygen. The purifying of the feed stream occurs with minimal loss of ethylene.
摘要翻译：公开了一种用于从蒸汽裂化器或流化催化裂化器（FCC）净化含乙烯进料流的方法，其中进料流还包含氢气，一氧化碳，乙炔，氧气，氮氧化物。该方法包括在至少120℃的反应温度下使含乙烯的气流与Ru-基催化剂接触。该方法产生含乙烯的进料流，其中乙烯基本上不含乙炔，氮氧化物和氧。进料流的纯化以最小的乙烯损失发生。

4. 发明申请

WO2010022318A2 PROCESS TO PURIFY ETHYLENE-CONTAINING OFF-GAS FEED STREAMS 审中-公开
标题翻译：纯化含乙烯的废气进料流的方法
公开(公告)号：WO2010022318A2
公开(公告)日：2010-02-25
申请号：PCT/US2009/054592
申请日：2009-08-21
申请人： SUD-CHEMIE INC. , SUN, Mingyong , BRYAN, Marty , BLANKENSHIP, Steve , URBANCIC, Michael, A.
发明人： SUN, Mingyong , BRYAN, Marty , BLANKENSHIP, Steve , URBANCIC, Michael, A.
IPC分类号： C10G11/18 , C10G51/04 , B01J23/46 , B01J21/02 , B01J21/06
CPC分类号： C07C7/167 , B01J23/462 , B01J23/48 , B01J23/60 , B01J23/62 , B01J23/6447 , B01J23/8926 , B01J35/008 , B01J35/1009 , B01J35/1014 , B01J35/1019 , B01J37/20 , Y02P20/52 , C07C11/04
摘要： A method for purification of ethylene-containing feed streams from steam crackers or fluid catalytic crackers (FCC), wherein the feed streams further comprises hydrogen, carbon monoxide, acetylenes, oxygen, nitrogen oxides, is disclosed. The method comprises contacting an ethylene-comprising gas stream with a Ru-based catalyst at reaction temperatures of at least 120°C. The process results in an ethylene- containing feed stream wherein the ethylene is essentially free of acetylenes, nitrogen oxides and oxygen. The purifying of the feed stream occurs with minimal loss of ethylene.
摘要翻译：公开了一种用于从蒸汽裂化器或流体催化裂化器（FCC）纯化含乙烯的进料流的方法，其中进料流还包含氢气，一氧化碳，乙炔，氧气，氮氧化物。该方法包括在至少120℃的反应温度下使含乙烯气流与Ru基催化剂接触。该方法得到含乙烯的进料流，其中乙烯基本上不含乙炔，氮氧化物和氧。进料流的净化发生时乙烯损失最小。

5. 发明申请

WO2007030298A1 CATALYTICALLY INACTIVE HEAT GENERATOR AND IMPROVED DEHYDROGENATION PROCESS 审中-公开
标题翻译：催化惰性热发生器和改进的脱氢方法
公开(公告)号：WO2007030298A1
公开(公告)日：2007-03-15
申请号：PCT/US2006/032441
申请日：2006-08-21
申请人： SUD-CHEMIE INC. , FRIDMAN, Vladimir , MERRIAM, Jay, S. , URBANCIC, Michael, A.
发明人： FRIDMAN, Vladimir , MERRIAM, Jay, S. , URBANCIC, Michael, A.
IPC分类号： B01J23/26 , B01J23/72 , B01J23/32
CPC分类号： B01J23/32 , B01J23/26 , B01J23/72 , B01J35/0006 , C07C5/322 , C07C2521/02 , C07C2521/04 , C07C2521/08 , C07C2521/10 , C07C2521/12 , C07C2523/02 , C07C2523/04 , C07C2523/06 , C07C2523/26 , C07C2523/34 , C07C2523/72 , C07C2523/889 , C07C2529/04 , Y02P20/52 , Y02P20/584 , C07C11/06
摘要： An improved dehydrogenation catalyst bed system for olein production utilizing classical processing techniques is disclosed. The catalyst bed system comprises a dehydrogenation catalyst comprising an active component selected from an oxide of a metal of Group 4 or Group 5 or Group 6 and combinations thereof and a support selected from aluminum oxide, aluminas, alumina monohydrate, alumina trihydrate, alumina-silica, transition aluminas, alpha- alumina, silica, silicate, aluminates, calcined hydrotalcites, zeolites and combinations thereof mixed with a first inert material selected from any material that is catalytically inactive when subjected to reaction conditions that can effect dehydrogenation of olefins and that has a high density and high heat capacity and that is not capable of producing heat during any stage of the dehydrogenation process, and the dehydrogenation catalyst plus the first inert material then being physically mixed with a secondary component comprising a heat-generating inert material and a carrier capable of supporting the heat-generating inert material, wherein the secondary component is catalytically inert with respect to dehydrogenation reactions or to cracking or to coking and generates heat after being exposed to reducing and/or to oxidizing reaction conditions.
摘要翻译：公开了一种利用经典处理技术改进的用于油精生产的脱氢催化剂床系统。催化剂床系统包括脱氢催化剂，其包含选自第4组或第5组或第6组金属的氧化物的活性组分及其组合，以及选自氧化铝，氧化铝，一水合氧化铝，三水合氧化铝，氧化铝 - 二氧化硅，过渡氧化铝，α-氧化铝，二氧化硅，硅酸盐，铝酸盐，煅烧水滑石，沸石及其混合物，其与第一惰性材料混合，所述第一惰性材料选自当受到可能影响烯烃脱氢的反应条件时具有催化活性的任何材料，并且具有高密度和高热容量，并且在脱氢过程的任何阶段都不能产生热量，然后脱氢催化剂加第一惰性材料与包含发热惰性材料和载体的次级组分物理混合支撑发热惰性材料，其中次要组分相对于脱氢反应是催化惰性的，或者在暴露于还原和/或氧化反应条件之后开裂或焦化并产生热量。

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