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1. 发明申请

WO2013012486A2 PROCESSES FOR MAKING CX-CY OLEFINS FROM C5 AND C6 PARAFFINS 审中-公开
标题翻译：从C5和C6石蜡制备CX-CY烯烃的方法
公开(公告)号：WO2013012486A2
公开(公告)日：2013-01-24
申请号：PCT/US2012/041193
申请日：2012-06-07
申请人： UOP LLC , MAJUMDER, Debarshi , SOHN, Stephen W. , GLOVER, Bryan K. , BOZZANO, Andrea G.
发明人： MAJUMDER, Debarshi , SOHN, Stephen W. , GLOVER, Bryan K. , BOZZANO, Andrea G.
IPC分类号： C07C2/04 , C07C5/10 , C07C9/00 , C07C2/64 , C07C15/073
CPC分类号： C07C6/04 , C07C2/06 , C07C2/64 , C07C5/32 , C07C303/06 , C10G50/00 , C10G69/126 , C07C11/02 , C07C11/10 , C07C11/107 , C07C15/107 , C07C309/31
摘要： Processes for making C X to C Y olefins are provided. The processes include reacting a feedstock comprising C 5 and C 6 olefins under dimerization or oligomerization conditions to provide a dimerization or oligomerization product. The product is separated into a stream comprising unreacted C 5 and C 6 paraffins, a stream comprising C 10 to C X-1 olefins, and a stream comprising C X to C Y olefins, wherein X is at least 14 and Y is greater than X and less than or equal to 36.
摘要翻译：提供了用于将C≡X取代为C≡Y烯烃的方法。该方法包括在二聚或低聚条件下使包含C5和C6烯烃的原料反应以提供二聚或低聚产物。将产物分离成包含未反应的C 5和C 6链烷烃的物流，包含C 10到C X-1的物流烯烃和包含C≡X至C≡Y烯烃的物流，其中X至少为14并且Y大于X且小于或等于36

2. 发明申请

WO2012173847A2 PROCESSES AND APPARATUSES FOR REGENERATING CATALYST PARTICLES 审中-公开
标题翻译：用于再生催化剂颗粒的方法和装置
公开(公告)号：WO2012173847A2
公开(公告)日：2012-12-20
申请号：PCT/US2012/041189
申请日：2012-06-07
申请人： UOP LLC , MOORE, Michael, A. , SECHRIST, Paul, A. , GLOVER, Bryan, K.
发明人： MOORE, Michael, A. , SECHRIST, Paul, A. , GLOVER, Bryan, K.
IPC分类号： B01J37/08 , B01J4/00 , C01G55/00
CPC分类号： B01J8/125 , B01J23/96 , B01J38/14 , B01J38/18 , B01J38/20 , B01J38/24 , B01J38/44 , B01J2208/00504
摘要： Processes and apparatuses for regenerating catalyst particles are provided. The processes include introducing spent catalyst particles to a burn zone in a continuous catalyst regenerator. When introduced, the catalyst particles, which contain a platinum group metal, carry coke deposits. In the process, a combustion gas at a temperature of at least 490°C with an oxygen content of at least 0.5 mol% is fed to the burn zone. There, the coke deposits on the catalyst particles are combusted with the combustion gas. The catalyst particles are passed from the burn zone to a halogenation zone in the continuous catalyst regenerator and the catalyst particles are oxyhalogenated to redisperse the platinum group metal to form regenerated catalyst particles.
摘要翻译：提供了再生催化剂颗粒的方法和装置。这些方法包括将废催化剂颗粒引入连续催化剂再生器中的燃烧区。当引入时，含有铂族金属的催化剂颗粒携带焦炭沉积物。在此过程中，氧气含量至少为0.5摩尔％的温度至少为490℃的燃烧气体被供给至燃烧区。在那里，催化剂颗粒上的焦炭沉积物与燃烧气体一起燃烧。催化剂颗粒从燃烧区通过连续催化剂再生器中的卤化区，催化剂颗粒被卤代卤化以再分散铂族金属以形成再生的催化剂颗粒。

3. 发明申请

WO2009015118A3 INTEGRATION OF OLEFIN CRACKING WITH METATHESIS TO INCREASE LIGHT OLEFINS PRODUCTION 审中-公开
标题翻译：结合元素分析的烯烃裂解增加轻质烯烃生产
公开(公告)号：WO2009015118A3
公开(公告)日：2009-04-16
申请号：PCT/US2008070713
申请日：2008-07-22
申请人： UOP LLC , SENETAR JOHN J , GLOVER BRYAN K
发明人： SENETAR JOHN J , GLOVER BRYAN K
IPC分类号： C07C4/02 , C07C6/04
CPC分类号： C07C4/06 , C07C6/04 , C07C11/04 , C07C11/06 , C10G2400/20
摘要： A process for increasing the propylene yields for hydrocarbon cracking processes. The process includes adding using alkylation of the C4s coming from the hydrocarbon cracker, and passing larger olefins to an olefin cracking unit.
摘要翻译：一种提高烃裂解过程丙烯收率的方法。该方法包括使用来自烃裂化器的C4的烷基化加入，并将较大的烯烃通入烯烃裂化单元。

4. 发明申请

WO2008082866A1 FLUIDIZED BED REACTOR WITH BACK-MIXING FOR DEHYDROGENATION OF LIGHT PARAFFINS 审中-公开
标题翻译：具有反混合的流化床反应器，用于脱色轻木素
公开(公告)号：WO2008082866A1
公开(公告)日：2008-07-10
申请号：PCT/US2007/087065
申请日：2007-12-11
申请人： UOP LLC , GLOVER, Bryan K. , ZARRAGA, Julie A. , SCHULTZ, Michael A.
发明人： GLOVER, Bryan K. , ZARRAGA, Julie A. , SCHULTZ, Michael A.
IPC分类号： B01J8/18
CPC分类号： C07C5/324 , C07C5/325 , C07C2521/04 , C07C2521/08 , C07C2521/16 , C07C2523/26 , C07C2523/28 , C07C2523/30 , C07C2523/36 , C07C2523/42 , C07C2523/44 , C07C2523/745 , C07C2523/75 , C07C2523/755 , Y02P20/584 , C07C11/02
摘要： An improved process and system for the endothermic dehydrogenation of an alkane stream (1) is described. The process and system of the present invention comprise a back-mixed fluidized bed reactor (4). The alkane stream is dehydrogenated in a single reactor stage by contacting the alkane stream with a back-mixed fluidized bed (44) of catalyst. Deactivated catalyst (38) is withdrawn from the back-mixed fluidized reactor and heated to produce hot regenerated catalyst (36). The hot regenerated catalyst is returned to the back-mixed fluidized bed reactor at a rate sufficient to maintain the back-mixed fluidized bed reactor at substantially isothermal conditions.
摘要翻译：描述了用于烷烃流（1）的吸热脱氢的改进方法和系统。本发明的方法和系统包括反混流化床反应器（4）。烷烃流在单个反应器阶段通过使烷烃流与催化剂的反混流化床（44）接触而脱氢。将脱活催化剂（38）从反混合流化反应器中取出并加热以产生热再生催化剂（36）。热再生催化剂以足以将反混流化床反应器保持在基本等温条件的速率返回到反混流化床反应器。

5. 发明申请

WO2006033759A3 CONVERSION OF OXYGENATE TO PROPYLENE WITH SELECTIVE HYDROGEN TREATMENT OF HEAVY OLEFIN RECYCLE STREAM 审中-公开
标题翻译：通过选择性氢处理重型油脂循环流程将氧化剂转化为丙烯
公开(公告)号：WO2006033759A3
公开(公告)日：2006-09-14
申请号：PCT/US2005030075
申请日：2005-08-25
申请人： UOP LLC , KALNES TOM N , WEI DANIEL H , GLOVER BRYAN K
发明人： KALNES TOM N , WEI DANIEL H , GLOVER BRYAN K
IPC分类号： C07C1/00
CPC分类号： C07C11/06 , C07C1/20 , C07C2529/40 , C07C2529/80 , C07C2529/85 , Y02P20/52 , Y02P20/582 , Y02P20/584
摘要： The average cycle propylene selectivity of an oxygenate to propylene (OTP) process using one or more fixed or moving beds of a dual-function oxygenate conversion catalyst with recycle of one or more C4+ olefin-rich fractions is substantially enhanced by the use of selective hydrotreating technology on these C4+ olefin-rich recycle streams to substantially eliminate detrimental coke precursors such as dienes and acetylenic hydrocarbons. This hydrotreating step helps hold the build-up of detrimental coke deposits on the catalyst to a level which does not substantially degrade dual-function catalyst activity, oxygenate conversion and propylene selectivity, thereby enabling a substantial improvement in propylene average cycle yield. The propylene average cycle yield improvement enabled by the present invention over the prior art system but without the use of the hydrotreating step on the C4+ olefin-rich recycle stream is of the order of 1.5 to 5.5 wt-% or more.
摘要翻译：使用一种或多种具有一种或多种富含C4 +烯烃的级分的再循环的双功能含氧化合物转化催化剂的固定床或移动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使用选择性加氢处理这些富含C4 +烯烃的循环物流的技术基本上消除了有害的焦炭前体，如二烯和炔烃。该加氢处理步骤有助于将催化剂上的有害焦炭沉积物的积聚保持在基本上不降低双功能催化剂活性，含氧化合物转化率和丙烯选择性的水平，从而可以显着提高丙烯平均循环产率。本发明相对于现有技术的系统而言，丙烯平均循环产率的改进，但不使用在富含C4 +烯烃的再循环料流上的加氢处理步骤为1.5〜5.5重量％以上。

6. 发明申请

WO2005047430A1 RING OPENING FOR INCREASED OLEFIN PRODUCTION 审中-公开
标题翻译：戒指开放以增加油脂生产
公开(公告)号：WO2005047430A1
公开(公告)日：2005-05-26
申请号：PCT/US2004/037300
申请日：2004-11-05
申请人： UOP LLC , GALPERIN, Irina, Z. , FOLEY, Timothy, D. , MCCALL, Michael, J. , KOCAL, Joseph, A. , GLOVER, Bryan, K. , PUJADO, Peter, R.
发明人： FOLEY, Timothy, D. , MCCALL, Michael, J. , KOCAL, Joseph, A. , GLOVER, Bryan, K. , PUJADO, Peter, R.
IPC分类号： C10G45/62
CPC分类号： C10G45/62 , C10G67/06 , C10G69/06
摘要： A process for cracking a naphtha feedstream to light olefins is presented. The process comprises converting aromatics and naphthenes to paraffins, and separating iso- and normal paraffins using a ring opening reactor (50) and an adsorption separation unit (20).
摘要翻译：提出了一种将石脑油原料流裂解成轻质烯烃的方法。该方法包括将芳烃和环烷烃转化为链烷烃，并使用开环反应器（50）和吸附分离单元（20）分离异链烷烃和正链烷烃。

7. 发明申请

WO2012173847A3 PROCESSES AND APPARATUSES FOR REGENERATING CATALYST PARTICLES 审中-公开
标题翻译：用于再生催化剂颗粒的方法和装置
公开(公告)号：WO2012173847A3
公开(公告)日：2013-04-25
申请号：PCT/US2012041189
申请日：2012-06-07
申请人： UOP LLC , MOORE MICHAEL A , SECHRIST PAUL A , GLOVER BRYAN K
发明人： MOORE MICHAEL A , SECHRIST PAUL A , GLOVER BRYAN K
IPC分类号： B01J37/08 , B01J4/00 , C01G55/00
CPC分类号： B01J8/125 , B01J23/96 , B01J38/14 , B01J38/18 , B01J38/20 , B01J38/24 , B01J38/44 , B01J2208/00504
摘要： Processes and apparatuses for regenerating catalyst particles are provided. The processes include introducing spent catalyst particles to a burn zone in a continuous catalyst regenerator. When introduced, the catalyst particles, which contain a platinum group metal, carry coke deposits. In the process, a combustion gas at a temperature of at least 490°C with an oxygen content of at least 0.5 mol% is fed to the burn zone. There, the coke deposits on the catalyst particles are combusted with the combustion gas. The catalyst particles are passed from the burn zone to a halogenation zone in the continuous catalyst regenerator and the catalyst particles are oxyhalogenated to redisperse the platinum group metal to form regenerated catalyst particles.
摘要翻译：提供了再生催化剂颗粒的方法和装置。这些方法包括将废催化剂颗粒引入连续催化剂再生器中的燃烧区。当引入时，含有铂族金属的催化剂颗粒携带焦炭沉积物。在此过程中，氧气含量至少为0.5摩尔％的温度至少为490℃的燃烧气体被供给至燃烧区。在那里，催化剂颗粒上的焦炭沉积物与燃烧气体一起燃烧。催化剂颗粒从燃烧区通过连续催化剂再生器中的卤化区，催化剂颗粒被卤代卤化以再分散铂族金属以形成再生的催化剂颗粒。

8. 发明申请

WO2012039999A3 INTEGRATION OF CYCLIC DEHYDROGENATION PROCESS WITH FCC FOR DEHYDROGENATION OF REFINERY PARAFFINS 审中-公开
标题翻译：循环脱氢工艺与FCC在炼油石蜡脱氢中的集成
公开(公告)号：WO2012039999A3
公开(公告)日：2012-08-16
申请号：PCT/US2011051363
申请日：2011-09-13
申请人： UOP LLC , GLOVER BRYAN K
发明人： GLOVER BRYAN K
IPC分类号： C10G11/18 , C07C2/00 , C07C4/06 , C07C11/04 , C10G57/02
CPC分类号： C07C4/06 , C07C2/56 , C07C5/3335 , C07C5/3337 , C07C6/04 , C07C2521/06 , C07C2523/26 , C07C2523/42 , C10G11/18 , C10G57/00 , C10G57/005 , C10G70/00 , C10G2400/20 , Y02P20/52 , C07C11/06 , C07C11/04
摘要： A process for increasing light olefin yields from the fluidized catalytic cracking process. The process combines small units to treat the paraffinic components in the product streams from the fluidized cracking process. The paraffins are dehydrogenated and light olefins are separated. Heavier olefins are passed to an olefin cracking unit for increasing the yields of ethylene and propylene.
摘要翻译：一种从流化催化裂化过程中提高轻质烯烃收率的方法。该工艺将小型装置结合起来处理来自流化裂化工艺的产物流中的链烷烃组分。石蜡脱氢并分离出轻质烯烃。重质烯烃被送到烯烃裂化单元以增加乙烯和丙烯的收率。

9. 发明申请

WO2008011292A1 SCREENLESS INTERNALS FOR RADIAL FLOW REACTORS 审中-公开
标题翻译：径流式反应器的无缝内部
公开(公告)号：WO2008011292A1
公开(公告)日：2008-01-24
申请号：PCT/US2007/073054
申请日：2007-07-09
申请人： UOP LLC , GLOVER, Bryan, K. , WOODLE, Guy, B. , ZIMMERMANN, Joseph, E. , SENETAR, John, J.
发明人： GLOVER, Bryan, K. , WOODLE, Guy, B. , ZIMMERMANN, Joseph, E. , SENETAR, John, J.
IPC分类号： B01J8/06
CPC分类号： B01J8/12 , B01J8/008 , B01J8/085
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 (10, 100) for retaining particles, with apertures (20, 120) disposed within the partitions (10, 100). The apertures (20, 120) are covered by louvers (30, 130) that extend above the edges (110) of the apertures (20, 120) to prevent solid particles from spilling through inlet apertures (20).
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隔板（10,100），其中设置在隔板（10,100）内的孔（20,120）。所述孔（20,120）由在所述孔（20,120）的边缘（110）上方延伸的百叶窗（30,130）覆盖以防止固体颗粒溢出入口孔（20）。

10. 发明申请

WO2012044594A3 PARAMETERS FOR A LOUVERED CENTERPIPE IN A RADIAL FLOW REACTOR 审中-公开
标题翻译：在径向流动反应器中扩大中心的参数
公开(公告)号：WO2012044594A3
公开(公告)日：2012-08-16
申请号：PCT/US2011053371
申请日：2011-09-27
申请人： UOP LLC , SUN BING , SECHRIST PAUL A , GLOVER BRYAN K , VETTER MICHAEL J
发明人： SUN BING , SECHRIST PAUL A , GLOVER BRYAN K , VETTER MICHAEL J
IPC分类号： B01J8/18 , B01J8/44
CPC分类号： B01J8/12 , B01D53/0423 , B01J8/085 , B01J2208/00849 , B01J2208/00929 , B01J2219/00024
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 louvers 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，其中孔设置在隔板内。孔由在孔的边缘上方延伸的百叶窗覆盖以防止固体颗粒通过入口孔溢出。

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