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31. 发明授权

US07781632B2 Integrated processes for making detergent range alkylbenzenes from C5-C6-containing feeds 有权
公开(公告)号：US07781632B2
公开(公告)日：2010-08-24
申请号：US12511617
申请日：2009-07-29
申请人： Bryan K. Glover , Stephen W. Sohn , Mark G. Riley , Dean E. Rende
发明人： Bryan K. Glover , Stephen W. Sohn , Mark G. Riley , Dean E. Rende
IPC分类号： C07C2/58 , C07C5/02 , C07C5/32
CPC分类号： C07C15/107 , C07C2/66 , C07C5/333 , C07C2521/12 , Y02P20/125
摘要： Integrated processes for making detergent range alkylbenzenes from C5-C6-containing feeds involve feed pretreatment and/or selective hydrogenation to enable acceptable quality alkylbenzene production at attractive capital and operating costs.

32. 发明授权

US07663012B2 Conversion of dimethylether to propylene using moving bed technology 有权
标题翻译：使用移动床技术将二甲醚转化为丙烯
公开(公告)号：US07663012B2
公开(公告)日：2010-02-16
申请号：US12115788
申请日：2008-05-06
申请人： Tom N. Kalnes , Daniel H. Wei , Bryan K. Glover
发明人： Tom N. Kalnes , Daniel H. Wei , Bryan K. Glover
IPC分类号： C07C1/00
CPC分类号： C07C1/20 , C07C2529/40 , C07C2529/85 , Y02P20/52 , C07C11/06
摘要： The average cycle propylene selectivity of an oxygenate to propylene (OTP) process using one or more fixed beds of a dual-function oxygenate conversion catalyst is substantially enhanced by the use of moving bed reactor technology in the hydrocarbon synthesis portion of the OTP flow scheme in lieu of fixed bed technology coupled with the selection of a catalyst on-stream cycle time of 200 hours or less. Those provisions hold the build-up of coke deposits on the catalyst to a level which does not substantially degrade dual-function catalyst activity, oxygenate conversion and propylene selectivity, thereby enabling maintenance of propylene average cycle yield at essentially start-of-cycle levels. The propylene average cycle yield improvement enabled by the present invention over that achieved by the fixed bed system of the prior art using the same or a similar catalyst system is of the order of about 1.5 to 5.5 wt-% or more.
摘要翻译：使用一种或多种双功能含氧化合物转化催化剂固定床的含氧化合物对丙烯（OTP）方法的平均循环丙烯选择性通过在OTP流动方案的烃合成部分中使用移动床反应器技术而显着增强固定床技术的替代加上选择催化剂在线循环时间为200小时以下。这些规定将催化剂上的焦炭沉积物积聚到不会显着降低双重功能催化剂活性，含氧化合物转化率和丙烯选择性的水平，从而在基本上循环水平的初始阶段维持丙烯平均循环产率。通过使用相同或相似的催化剂体系的现有技术的固定床系统实现的本发明的丙烯平均循环产率提高约为1.5至5.5重量％或更多。

33. 发明申请

US20090325791A1 Hydrocarbon Dehydrogenation with Zirconia 审中-公开
标题翻译：碳氢脱氢与氧化锆
公开(公告)号：US20090325791A1
公开(公告)日：2009-12-31
申请号：US12488986
申请日：2009-06-22
申请人： Wei Pan , Stephen M. Casey , Bryan K. Glover , Feng Xu
发明人： Wei Pan , Stephen M. Casey , Bryan K. Glover , Feng Xu
IPC分类号： B01J21/06 , B01J23/10 , B01J23/02
CPC分类号： B01J23/10 , B01J21/066 , B01J23/002 , B01J23/02 , B01J23/36 , B01J23/40 , B01J23/48 , B01J35/0006 , B01J37/0009 , B01J37/0215 , B01J37/0221 , C07C5/3332 , C10G2400/20 , C10G2400/22 , Y02P20/584
摘要： A method for obtaining an olefin is disclosed, the method comprising subjecting a paraffin to dehydrogenation in the absence of oxygen and in the presence of a catalyst comprising a crystalline substrate, to obtain an olefin. The catalyst includes an inert stabilizing agent for maintaining the catalyst crystal structure. The catalyst may be regenerated by being subjected, in air, to a temperature between about 550° C. and about 750° C., for a period of time between about 15 minutes and about 4 hours.
摘要翻译：公开了一种获得烯烃的方法，该方法包括在不存在氧的情况下和在含有结晶底物的催化剂的存在下使石蜡脱氢以获得烯烃。催化剂包括用于维持催化剂晶体结构的惰性稳定剂。催化剂可以通过在空气中在约550℃和约750℃之间的温度下在约15分钟至约4小时之间的时间内再生。

34. 发明申请

US20090292151A1 Oxygenate Conversion to Olefins With Metathesis 有权
标题翻译：氧化烯转化为烯烃与复分解
公开(公告)号：US20090292151A1
公开(公告)日：2009-11-26
申请号：US12536820
申请日：2009-08-06
申请人： Andrea G. Bozzano , Bryan K. Glover
发明人： Andrea G. Bozzano , Bryan K. Glover
IPC分类号： C07C1/02
CPC分类号： C07C11/06 , C07C1/20 , C07C6/04 , Y02P30/42 , C07C11/02
摘要： A processing scheme and system for enhanced light olefin production, particularly for increased relative yield of propylene, involves oxygenate conversion to olefins and subsequent oxygenate conversion effluent stream treatment including cross-metathesis of 1-butene with 2-butene, metathesis of 2-butene with ethylene, conversion or removal of at least a portion of the isobutene, and/or isomerization of at least a portion of 1-butene to 2-butene to produce additional propylene. The processing scheme and system may further involve a reaction with distillation column for the metathesis of butenes with ethylene to produce propylene and/or a reaction with distillation column for the conversion of isobutenes with an oxygenate-containing material to produce a tertiary ether or alcohol.
摘要翻译：用于增强轻烯烃生产的加工方案和系统，特别是用于增加丙烯的相对产率，涉及含氧化合物转化为烯烃和随后的含氧化合物转化流出物流处理，包括1-丁烯与2-丁烯的交错复分解，2-丁烯的复分解乙烯，至少一部分异丁烯的转化或除去，和/或至少一部分1-丁烯异构化成2-丁烯以产生另外的丙烯。处理方案和系统可以进一步包括与用乙烯使乙烯复分解以产生丙烯和/或与蒸馏塔反应以使异丁烯与含氧化合物转化以产生叔醚或醇的反应。

35. 发明申请

US20090292150A1 Integrated Processes for Making Detergent Range Alkylbenzenes from C5-C6-Containing Feeds 有权
标题翻译：用于制备来自含C5-C6的进料的洗涤剂范围烷基苯的综合方法
公开(公告)号：US20090292150A1
公开(公告)日：2009-11-26
申请号：US12511567
申请日：2009-07-29
申请人： Bryan K. Glover , Stephen W. Sohn , Mark G. Riley , Dean E. Rende
发明人： Bryan K. Glover , Stephen W. Sohn , Mark G. Riley , Dean E. Rende
IPC分类号： C07C2/02
CPC分类号： C07C15/107 , C07C2/66 , C07C5/333 , C07C2521/12 , Y02P20/125
摘要： Integrated processes for making detergent range alkylbenzenes from C5-C6-containing feeds involve feed pretreatment and/or selective hydrogenation to enable acceptable quality alkylbenzene production at attractive capital and operating costs.
摘要翻译：用于制备来自含C5-C6的进料的洗涤剂范围烷基苯的综合方法包括进料预处理和/或选择性氢化，以令人满意的资本和操作成本实现可接受的优质烷基苯生产。

36. 发明授权

US07622089B1 Conically shaped screenless internals for radial flow reactors 有权
标题翻译：用于径向流动反应器的圆锥形无筛网
公开(公告)号：US07622089B1
公开(公告)日：2009-11-24
申请号：US11458401
申请日：2006-07-19
申请人： Bryan K. Glover
发明人： Bryan K. Glover
IPC分类号： B01J8/00 , B01J8/12
CPC分类号： B01J8/12 , B01J8/085 , B01J2219/0077 , B01J2219/00774
摘要： An apparatus for contacting a bed of particulate material with a cross flowing fluid, which maintains the bed of particulate material within a retention volume. The apparatus includes partitions for retaining particles, with apertures disposed within the partitions. The apertures are covered by shrouds that extend above the edges of the apertures to prevent solid particles from spilling through inlet apertures.
摘要翻译：用于使颗粒材料床与交叉流动流体接触的装置，其将颗粒材料床保持在保持体积内。该装置包括用于保持颗粒的分隔物，孔中设置在隔板内。这些孔被在孔的边缘上方延伸的护罩覆盖，以防止固体颗粒通过入口孔溢出。

37. 发明申请

US20080242910A1 Conversion of Dimethylether to Propylene using Moving Bed Technology 有权
标题翻译：使用移动床技术将二甲醚转化成丙烯
公开(公告)号：US20080242910A1
公开(公告)日：2008-10-02
申请号：US12115788
申请日：2008-05-06
申请人： Tom N. Kalnes , Daniel H. Wei , Bryan K. Glover
发明人： Tom N. Kalnes , Daniel H. Wei , Bryan K. Glover
IPC分类号： C07C1/20
CPC分类号： C07C1/20 , C07C2529/40 , C07C2529/85 , Y02P20/52 , C07C11/06
摘要： The average cycle propylene selectivity of an oxygenate to propylene (OTP) process using one or more fixed beds of a dual-function oxygenate conversion catalyst is substantially enhanced by the use of moving bed reactor technology in the hydrocarbon synthesis portion of the OTP flow scheme in lieu of fixed bed technology coupled with the selection of a catalyst on-stream cycle time of 200 hours or less. Those provisions hold the build-up of coke deposits on the catalyst to a level which does not substantially degrade dual-function catalyst activity, oxygenate conversion and propylene selectivity, thereby enabling maintenance of propylene average cycle yield at essentially start-of-cycle levels. The propylene average cycle yield improvement enabled by the present invention over that achieved by the fixed bed system of the prior art using the same or a similar catalyst system is of the order of about 1.5 to 5.5 wt-% or more.
摘要翻译：使用一种或多种双功能含氧化合物转化催化剂固定床的含氧化合物对丙烯（OTP）方法的平均循环丙烯选择性通过在OTP流动方案的烃合成部分中使用移动床反应器技术而显着增强固定床技术的替代加上选择催化剂在线循环时间为200小时以下。这些规定将催化剂上的焦炭沉积物积聚到不会显着降低双重功能催化剂活性，含氧化合物转化率和丙烯选择性的水平，从而在基本上循环水平的初始阶段维持丙烯平均循环产率。通过使用相同或相似的催化剂体系的现有技术的固定床系统实现的本发明的丙烯平均循环产率提高约为1.5至5.5重量％或更多。

38. 发明申请

US20080207973A1 Purge Gas Streams to Stagnant Zones within Oxygenate-to-Olefin Reactor 有权
标题翻译：将气流吹入含氧烯烃反应器内的停滞区域
公开(公告)号：US20080207973A1
公开(公告)日：2008-08-28
申请号：US12116253
申请日：2008-05-07
申请人： Paolo Palmas , Daniel N. Myers , Bryan K. Glover
发明人： Paolo Palmas , Daniel N. Myers , Bryan K. Glover
IPC分类号： C07C1/00 , B01J8/04
CPC分类号： B01J8/0055 , B01J8/1818 , B01J8/26 , B01J2208/00274 , B01J2208/00292 , B01J2219/00006 , C07C1/20 , C07C11/02
摘要： The present invention comprises a process for conversion of oxygenates to olefins comprising contacting within a reactor the oxygenates with a catalyst to produce light olefins and wherein the reactor comprises at least two zones, a first zone wherein gas circulates at a faster rate than a second zone wherein a gas circulates at a slower rate; and inserting a quantity of inert gas into the second zone to increase circulation of any materials located in said second zone. The invention prevents accumulation of undesirable by-products within stagnant zones within the reactor and reduces the amount of coke deposited on catalyst or on surfaces within these zones.
摘要翻译：本发明包括将含氧化合物转化为烯烃的方法，包括在反应器内使含氧化合物与催化剂接触以产生轻质烯烃，并且其中反应器包括至少两个区域，第一区域，其中气体以比第二区域更快的速率循环其中气体以较慢的速率循环; 以及将一定数量的惰性气体插入所述第二区域以增加位于所述第二区域中的任何材料的循环。本发明防止不期望的副产物在反应器内的停滞区内积聚，并减少沉积在催化剂上或在这些区域内的表面上的焦炭的量。

39. 发明申请

US20080154077A1 Oxygenate conversion to olefins with metathesis 审中-公开
标题翻译：复合转化烯烃转化为烯烃
公开(公告)号：US20080154077A1
公开(公告)日：2008-06-26
申请号：US11643301
申请日：2006-12-21
申请人： Andrea G. Bozzano , Bryan K. Glover
发明人： Andrea G. Bozzano , Bryan K. Glover
IPC分类号： B01J14/00 , C07C6/02
CPC分类号： C07C11/06 , C07C1/20 , C07C6/04 , Y02P30/42 , C07C11/02
摘要： A processing scheme and system for enhanced light olefin production, particularly for increased relative yield of propylene, involves oxygenate conversion to olefins and subsequent oxygenate conversion effluent stream treatment including cross-metathesis of 1-butene with 2-butene, metathesis of 2-butene with ethylene, conversion or removal of at least a portion of the isobutene, and/or isomerization of at least a portion of 1-butene to 2-butene to produce additional propylene. The processing scheme and system may further involve a reaction with distillation column for the metathesis of butenes with ethylene to produce propylene and/or a reaction with distillation column for the conversion of isobutenes with an oxygenate-containing material to produce a tertiary ether or alcohol.
摘要翻译：用于增强轻烯烃生产的加工方案和系统，特别是用于增加丙烯的相对产率，涉及含氧化合物转化为烯烃和随后的含氧化合物转化流出物流处理，包括1-丁烯与2-丁烯的交错复分解，2-丁烯的复分解乙烯，至少一部分异丁烯的转化或除去，和/或至少一部分1-丁烯异构化成2-丁烯以产生另外的丙烯。处理方案和系统可以进一步包括与用乙烯使乙烯复分解以产生丙烯和/或与蒸馏塔反应以使异丁烯与含氧化合物转化以产生叔醚或醇的反应。

40. 发明授权

US07368618B2 Process for removal of oxygenates from a paraffin stream 有权
标题翻译：从石蜡流中除去含氧化合物的方法
公开(公告)号：US07368618B2
公开(公告)日：2008-05-06
申请号：US11457889
申请日：2006-07-17
申请人： Santi Kulprathipanja , James W. Priegnitz , Stephen W. Sohn , Bryan K. Glover , Bipin V. Vora
发明人： Santi Kulprathipanja , James W. Priegnitz , Stephen W. Sohn , Bryan K. Glover , Bipin V. Vora
IPC分类号： C07C5/327
CPC分类号： C07C5/333 , C07C2/66 , C07C7/12 , C07C7/13 , C07C15/107 , C07C9/14 , C07C11/02
摘要： The present invention comprises a process for removal of oxygenates from a paraffin-rich or olefin-rich paraffin stream which comprises passing a feed stream, comprising one or more C10 to C15 feed paraffins or C10 to C15 olefin-rich paraffin stream and one or more oxygenates through an adsorbent bed comprising one or more adsorbents selected from silica gel, activated alumina and sodium x zeolites to remove essentially all of said oxygenates; and recovering said paraffins. A second adsorbent bed may be employed to more thoroughly remove these oxygenates.
摘要翻译：本发明包括从富含链烷烃或富烯烃的石蜡流中除去含氧化合物的方法，该方法包括将含有一个或多个C 10的进料流送入C 15 通过吸附床将含有一种或多种选自硅胶，活性氧化铝和吸附剂的吸附剂的烷烃或C 10向富含C 15的富烯烃链烷烃流和一种或多种含氧化合物进料，钠x沸石以除去基本上所有的含氧化合物; 并回收所述石蜡。可以使用第二吸附剂床来更彻底地除去这些含氧化合物。

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