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1. 发明申请

WO2013043294A1 METHODS FOR CO-PRODUCTION OF ALKYLBENZENE AND BIOFUEL FROM NATURAL OILS USING HYDROCRACKING 审中-公开
标题翻译：使用水解法从天然油中生产烷基苯酚和生物油的方法
公开(公告)号：WO2013043294A1
公开(公告)日：2013-03-28
申请号：PCT/US2012/051701
申请日：2012-08-21
申请人： UOP LLC , ANUMAKONDA, Amarendra , RAGHURAM, Srikantiah , DA SILVA FERREIRA ALVES, Joao Jorge , BOZZANO, Andrea, G.
发明人： ANUMAKONDA, Amarendra , RAGHURAM, Srikantiah , DA SILVA FERREIRA ALVES, Joao Jorge , BOZZANO, Andrea, G.
IPC分类号： C10G69/12 , C07C15/073 , C07C2/64 , C10L1/04
CPC分类号： C07C2/68 , C07C2/70 , C07C5/333 , C07C7/163 , C07C2527/1206 , C07C2527/126 , C10G3/00 , C10G69/00 , C10G69/123 , C10G69/14 , C10G2300/1014 , C10G2400/30 , Y02P30/20 , C07C15/107 , C07C11/02
摘要： Embodiments of methods for co-production of linear alkylbenzene and biofuel from a natural oil are provided. A method comprises the step of deoxygenating the natural oils to form paraffins. A first portion of the paraffins is hydrocracked to form a first stream of normal and lightly branched paraffins in the C 9 to C 14 range and a second stream of isoparaffins. The first stream is dehydrogenated to provide mono-olefins. Then, benzene is alkylated with the mono-olefins under alkylation conditions to provide an alkylation effluent comprising alkylbenzenes and benzene. Thereafter, the alkylbenzenes are isolated to provide the alkylbenzene product. A second portion of the paraffins and the isoparaffins are processed to form biofuel.
摘要翻译：提供了从天然油共生产线性烷基苯和生物燃料的方法的实施方案。一种方法包括使天然油脱氧以形成链烷烃的步骤。将第一部分石蜡加氢裂化以形成C9至C14范围内的第一流和正链和轻度支化的烷烃，第二股异链烷烃流。将第一流脱氢以提供单烯烃。然后，在烷基化条件下用单烯烃烷基化苯以提供包含烷基苯和苯的烷基化流出物。此后，分离烷基苯以提供烷基苯产物。石蜡和异链烷烃的第二部分被处理以形成生物燃料。

2. 发明申请

WO2007079324A2 METHANOL-WATER MIXTURES IN OLEFIN PRODUCTION VIA OXYGENATE CONVERSION 审中-公开
标题翻译：通过氧化剂转化生产烯烃的甲醇 - 水混合物
公开(公告)号：WO2007079324A2
公开(公告)日：2007-07-12
申请号：PCT/US2006/061877
申请日：2006-12-11
申请人： UOP LLC , MILLER, Lawrence, W. , MILLER, Sterling, T. , BOZZANO, Andrea, G.
发明人： MILLER, Lawrence, W. , MILLER, Sterling, T. , BOZZANO, Andrea, G.
IPC分类号： C07C1/00 , B01J8/00
CPC分类号： C07C11/06 , C07C1/20 , C07C11/04 , C10G2400/20 , Y02P30/42 , C07C11/02
摘要： Processing schemes and arrangements are provided for producing light olefins from an oxygenate-containing feedstock and using methanol-water mixtures to recover oxygenates such as for further processing to form additional light olefins.
摘要翻译：提供加工方案和布置用于从含氧化合物的原料生产轻质烯烃，并使用甲醇 - 水混合物回收含氧化合物，以进一步加工以形成另外的轻质烯烃。

3. 发明申请

WO2008076675A1 OXYGENATE CONVERSION TO OLEFINS WITH METATHESIS 审中-公开
标题翻译：氧化物转化为具有METATHESIS的油脂
公开(公告)号：WO2008076675A1
公开(公告)日：2008-06-26
申请号：PCT/US2007/086860
申请日：2007-12-07
申请人： UOP LLC , BOZZANO, Andrea, G. , GLOVER, Bryan, K.
发明人： BOZZANO, Andrea, G. , GLOVER, Bryan, K.
IPC分类号： C07C6/04 , C07C11/06
CPC分类号： C07C11/06 , C07C1/20 , C07C6/04 , Y02P30/42 , C07C11/02
摘要： Processing schemes and systems (10, 100, 200, 300, 400) for enhanced light olefin production, particularly for increased relative yield of propylene, involve 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 schemes and systems (10, 100, 200, 300, 400) may further involve a reaction with distillation column (162) 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（10,100,200,300,400），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的交叉复分解丁烯，2-丁烯与乙烯的复分解，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（10,100,200,300,400）还可以包括与蒸馏塔（162）的反应，用于使乙烯与乙烯进行复分解以产生丙烯和/或与蒸馏塔反应以使异丁烯转化含有含氧化合物的物质产生叔醚或醇。

4. 发明申请

WO2007102916A2 METHANOL-TO-OLEFINS PROCESS WITH REDUCED COKING 审中-公开
标题翻译：甲醇到烯烃的加工减少了焦化
公开(公告)号：WO2007102916A2
公开(公告)日：2007-09-13
申请号：PCT/US2006/062249
申请日：2006-12-18
申请人： UOP LLC , BOZZANO, Andrea, G. , BRADLEY, Steven, A. , CASTILLO, Ricardo, L. , CHEN, John, Q.
发明人： BOZZANO, Andrea, G. , BRADLEY, Steven, A. , CASTILLO, Ricardo, L. , CHEN, John, Q.
IPC分类号： C07C1/00
CPC分类号： B01J19/02 , B01J8/0055 , B01J8/1863 , B01J2219/0236 , C07C1/20 , C07C2529/85 , C07C11/02
摘要： A process for producing light olefins from oxygenates wherein internal reactor surfaces are protected from metal-catalyzed coking preferably by employing a protective layer.
摘要翻译：一种由含氧化合物生产轻质烯烃的方法，其中内部反应器表面优选通过使用保护层来防止金属催化焦化。

5. 发明申请

WO2008097313A1 STAGED PROCESS FOR PRODUCING LINEAR 2-PHENYL-ALKANES 审中-公开
标题翻译：用于生产线性2-苯乙烯的标记方法
公开(公告)号：WO2008097313A1
公开(公告)日：2008-08-14
申请号：PCT/US2007/061790
申请日：2007-02-07
申请人： UOP LLC , BOZZANO, Andrea, G. , LAWSON, R., Joe , BARGER, Paul, T. , VORA, Bipin, V. , DETRICK, Kurt, A.
发明人： BOZZANO, Andrea, G. , LAWSON, R., Joe , BARGER, Paul, T. , VORA, Bipin, V. , DETRICK, Kurt, A.
IPC分类号： C07C2/64 , C07C2/66
CPC分类号： C07C2/66 , C07C15/107
摘要： The process disclosed herein is a process for producing phenyl-alkanes by alkylation of an aryl compound with an olefinic compound and which uses a mordenite catalyst and a silica-alumina catalyst. The selectivity of the process to 2 phenyl-alkanes can be varied over a wide range.
摘要翻译：本文公开的方法是通过用烯烃化合物烷基化芳基化合物并使用丝光沸石催化剂和二氧化硅 - 氧化铝催化剂来生产苯基烷烃的方法。该方法对2-苯基烷烃的选择性可以在很宽的范围内变化。

6. 发明申请

WO2012087612A3 HIGH PURITY HEAVY NORMAL PARAFFINS UTILIZING INTEGRATED SYSTEMS 审中-公开
公开(公告)号：WO2012087612A3
公开(公告)日：2012-06-28
申请号：PCT/US2011/064142
申请日：2011-12-09
申请人： UOP LLC , SOHN, Stephen, W. , BOZZANO, Andrea, G. , PIEPER, Jeffrey, L.
发明人： SOHN, Stephen, W. , BOZZANO, Andrea, G. , PIEPER, Jeffrey, L.
IPC分类号： C10G67/02 , C10G45/02 , C10G25/00 , C07C7/00
摘要： A process is presented for producing a purified normal paraffin product stream. The process includes passing a hydrocarbon stream having the desired normal paraffins to an adsorption separation system. A process stream generated from the separation system and having the normal paraffins is passed to an adsorption unit for the selective adsorption of aromatic compounds from the process stream, thereby producing a purified product.

7. 发明申请

WO2012064524A2 METHODS FOR CO-PROCESSING BIORENEWABLE FEEDSTOCK AND PETROLEUM DISTILLATE FEEDSTOCK 审中-公开
标题翻译：共同加工可再生原料和石油衍生物原料的方法
公开(公告)号：WO2012064524A2
公开(公告)日：2012-05-18
申请号：PCT/US2011/058254
申请日：2011-10-28
申请人： UOP LLC , BOZZANO, Andrea, G. , EIZENGA, Donald , NORTON, Ralph, Charles
发明人： BOZZANO, Andrea, G. , EIZENGA, Donald , NORTON, Ralph, Charles
IPC分类号： C10G65/04 , C10G45/00 , C10G3/00
CPC分类号： C10L1/02 , C10G3/42 , C10G3/50 , C10G45/02 , C10G69/02 , C10G2300/1011 , C10G2300/1037 , C10G2300/202 , C10G2300/207 , C10G2300/4018 , C10G2300/4081 , Y02E50/13 , Y02P30/20
摘要： Methods for co-processing a biorenewable feedstock and a petroleum distillate feedstock are provided. The petroleum distillate feedstock containing sulfur is reacted with hydrogen gas in the presence of a hydrotreating catalyst thereby forming an effluent mixture comprising hydrogen sulfide. A combined feed comprising the effluent mixture, optionally a recycle liquid, and the biorenewable feedstock is contacted with hydrogen gas in a reaction zone with a deoxygenation catalyst under reaction conditions to provide a reaction product comprising a hydrocarbon fraction. The combined feed comprises greater than 50 weight percent biorenewable feedstock.
摘要翻译：提供了生物可再生原料和石油馏出物原料的共处理方法。含硫的石油馏出物原料在加氢处理催化剂的存在下与氢气反应，从而形成包含硫化氢的流出物混合物。在反应条件下将包含流出物混合物，任选的再循环液体和生物可再生原料的组合进料与反应区中的氢气与脱氧催化剂接触，以提供包含烃馏分的反应产物。组合的进料包含大于50重量％的生物可再生原料。

8. 发明申请

WO2010002573A2 OTO QUENCH TOWER CATALYST RECOVERY SYSTEM UTILIZING A LOW TEMPERATURE FLUIDIZED DRYING CHAMBER 审中-公开
标题翻译：采用低温流化干燥室的OTO QUENCH TOWER催化剂回收系统
公开(公告)号：WO2010002573A2
公开(公告)日：2010-01-07
申请号：PCT/US2009/047332
申请日：2009-06-15
申请人： UOP LLC , MYERS, Daniel, N. , JOHNSON, Richard, A. , BOZZANO, Andrea, G.
发明人： MYERS, Daniel, N. , JOHNSON, Richard, A. , BOZZANO, Andrea, G.
IPC分类号： B01J38/72 , B01J38/02 , C10G11/02
CPC分类号： B01J8/26 , B01J29/90 , B01J38/02 , B01J38/12 , B01J38/30 , B01J38/32 , B01J2219/00006 , C07C1/20 , Y02P20/584 , Y02P30/20 , C07C11/02
摘要： Systems and methods for recovering catalyst in an oxygenate to olefin process are provided that include removing a quench tower bottoms stream containing catalyst from a quench tower and passing the catalyst containing stream to a drying chamber, where the catalyst containing stream is dried to produce substantially dried catalyst.
摘要翻译：提供了用于在含氧化合物至烯烃方法中回收催化剂的系统和方法，其包括从骤冷塔中除去含有催化剂的骤冷塔塔底物流并将含催化剂物流通入干燥室，其中催化剂将含氧气流干燥以产生基本干燥的催化剂。

9. 发明申请

WO2016094176A2 USE OF CATALYST TO ADJUST PRODUCT DISTRIBUTIONS IN MTO PROCESS 审中-公开
标题翻译：使用催化剂调整MTO工艺中的产品分布
公开(公告)号：WO2016094176A2
公开(公告)日：2016-06-16
申请号：PCT/US2015/063654
申请日：2015-12-03
申请人： UOP LLC
发明人： FUNK, Gregory, A. , BOZZANO, Andrea, G. , SCHOENFELDT, Nicholas, J. , CHELLPPANNAIR, Thulasidas , SPIEKER, Wolfgang, A. , VORA, Bipin, V.
IPC分类号： C07C1/20
CPC分类号： C07C1/20 , C07C4/02 , C07C6/04 , C07C2529/85 , Y02P30/42 , C07C11/04 , C07C11/06
摘要： A process is presented for generating light olefins with the methanol to olefins process from a combination of catalysts. The process controls the product distribution for ethylene, propylene and butylenes, to enable shifting of the product distribution. The process includes passing a second catalyst to a reactor while the process is on-going.
摘要翻译：提出了一种从催化剂组合中用甲醇 - 烯烃方法生产轻质烯烃的方法。该方法控制乙烯，丙烯和丁烯的产物分布，以实现产品分布的转移。该过程包括在过程持续时将第二催化剂通入反应器。

10. 发明申请

WO2014160825A1 INTEGRATED PROCESS FOR INCREASING BUTADIENE PRODUCTION 审中-公开
标题翻译：综合方法增加二倍体生产
公开(公告)号：WO2014160825A1
公开(公告)日：2014-10-02
申请号：PCT/US2014/031948
申请日：2014-03-27
申请人： UOP LLC
发明人： BOZZANO, Andrea, G. , VORA, Bipin, V. , WEI, Daniel, H. , KRUPA, Steven, L.
IPC分类号： C07C7/00 , C07C5/00 , C07C11/167
CPC分类号： C07C5/48 , C07C7/10 , Y02P20/125 , C07C11/167
摘要： A process is present for increasing the yields of 1,3 butadiene. The process includes recovering 1,3 butadiene from a cracking unit that generates a crude C4 stream. The 1,3 butadiene is separated and the remaining C4 process stream components are further reacted and dehydrogenated to generate 1,3 butadiene in a subsequent process stream. The subsequent process stream is recycled to recover the additional 1,3 butadiene.
摘要翻译：存在一种提高1,3-丁二烯产率的方法。该方法包括从产生粗C4流的裂解装置回收1,3-丁二烯。分离1,3-丁二烯，剩余的C4工艺流组分进一步反应和脱氢，以便在随后的工艺流中产生1,3-丁二烯。随后的工艺流被再循环以回收额外的1,3-丁二烯。

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