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1.发明申请METHODS FOR CO-PROCESSING BIORENEWABLE FEEDSTOCK AND PETROLEUM DISTILLATE FEEDSTOCK 有权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：US20120116134A1
公开(公告)日：2012-05-10
申请号：US12941420
申请日：2010-11-08
IPC分类号： C10L1/02
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。
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2.发明授权Methods for co-processing biorenewable feedstock and petroleum distillate feedstock 有权生物可再生原料和石油馏分原料共处理方法公开(公告)号：US08686204B2
公开(公告)日：2014-04-01
申请号：US12941420
申请日：2010-11-08
IPC分类号： C07C1/00
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。
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公开(公告)号：US09394215B2
公开(公告)日：2016-07-19
申请号：US13186205
申请日：2011-07-19
IPC分类号： C07C2/64 , C07C2/04 , C07C2/54 , C07C2/56 , C07C2/72 , C07C6/04 , C07C303/06 , C07C2/06 , C07C5/32 , C10G50/00 , C10G69/12
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 CX to CY olefins are provided. The processes include reacting a feedstock comprising C5 and C6 olefins under dimerization or oligomerization conditions to provide a dimerization or oligomerization product. The product is separated into a stream comprising unreacted C5 and C6 paraffins, a stream comprising C10 to CX-1 olefins, and a stream comprising CX to CY olefins, wherein X is at least 14 and Y is greater than X and less than or equal to 36.
摘要翻译： 提供了制备CX至CY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C5和C6链烷烃的流，包含C10至CX-1烯烃的流和包含CX至CY烯烃的流，其中X为至少14且Y大于X且小于或等于 到36。
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公开(公告)号：US08921632B2
公开(公告)日：2014-12-30
申请号：US13193780
申请日：2011-07-29
申请人： Joseph A. Montalbano , Steven Lee Krupa , John Joseph Senetar , Joseph H. Gregor , Andrea G. Bozzano , Gary S. Sandhu
发明人： Joseph A. Montalbano , Steven Lee Krupa , John Joseph Senetar , Joseph H. Gregor , Andrea G. Bozzano , Gary S. Sandhu
IPC分类号： C07C2/00 , C07C41/06 , C07C1/20 , C07C4/02 , C07C4/04 , C07C5/03 , C07C11/04 , C07C11/06 , C07C11/08
CPC分类号： C07C41/06 , C07C1/20 , C07C4/02 , C07C4/04 , C07C5/03 , C07C11/04 , C07C11/06 , C07C11/08 , Y02P30/42 , C07C43/046 , C07C11/02
摘要： 1-butene is recovered as a purified product from an MTO synthesis and especially from an integrated MTO synthesis and hydrocarbon pyrolysis system in which the MTO system and its complementary olefin cracking reactor are combined with a hydrocarbon pyrolysis reactor in a way that facilitates the flexible production and recovery of olefins and other petrochemical products, particularly butene-1 and MTBE.
摘要翻译： 1-丁烯作为纯化产物从MTO合成中回收，特别是从集成的MTO合成和烃热解系统中回收，其中MTO系统及其互补烯烃裂解反应器以便于柔性生产的方式与烃热解反应器组合 并回收烯烃和其他石化产品，特别是丁烯-1和MTBE。
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5.发明授权Methods for co-production of alkylbenzene and biofuel from natural oils using hydrocracking 有权使用加氢裂化从天然油共生产烷基苯和生物燃料的方法公开(公告)号：US08507741B2
公开(公告)日：2013-08-13
申请号：US13242825
申请日：2011-09-23
申请人： Amarendra Anumakonda , Srikantiah Raghuram , Joao Jorge da Silva Ferreira Alves , Andrea G. Bozzano
发明人： Amarendra Anumakonda , Srikantiah Raghuram , Joao Jorge da Silva Ferreira Alves , Andrea G. Bozzano
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 C9 to C14 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直链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。
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公开(公告)号：US07750198B2
公开(公告)日：2010-07-06
申请号：US12046948
申请日：2008-03-12
CPC分类号： C07C15/107 , C07C2/66
摘要： Aromatic by-products are sorbed from mono-olefin-containing feedstocks of olefins having from about 6 to 22 carbon atoms per molecule that contain aromatic by-products having from 7 to 22 carbon atoms per molecule. A benzene-containing regenerant displaces and desorbs the aromatic by-products from the sorbent and a regeneration effluent is provided. The regeneration effluent is treated in a regeneration effluent distillation system to provide a benzene-rich stream and an aromatic by-products-containing stream. The latter is subjected to benzene-forming conditions and recycled to the regeneration effluent distillation system where benzene is recovered.
摘要翻译： 芳族副产物被从每分子含有约6至22个碳原子的含单烯烃的原料中吸收，每分子含有7至22个碳原子的芳族副产物。 含苯的再生剂从吸附剂中取代并解吸芳族副产物，并提供再生流出物。 再生流出物在再生流出物蒸馏系统中处理以提供富含苯的流和含芳香族副产物的流。 后者经受苯形成条件并再循环至回收苯的再生流出物蒸馏系统。
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公开(公告)号：US20080154078A1
公开(公告)日：2008-06-26
申请号：US11643604
申请日：2006-12-21
申请人： Andrea G. Bozzano , Bryan K. Glover
发明人： Andrea G. Bozzano , Bryan K. Glover
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 dimerization of ethylene to butene and metathesis of butenes and/or hexenes with ethylene. The processing scheme and system may further involve isomerization of at least a portion of 1-butene to 2-butene to produce additional propylene.
摘要翻译： 用于增强轻烯烃生产的加工方案和系统，特别是用于提高丙烯的相对产率，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，包括将乙烯二聚成丁烯和使乙烯和/或己烯与乙烯的复分解。 加工方案和系统可进一步包括将至少一部分1-丁烯异构化成2-丁烯以产生另外的丙烯。
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公开(公告)号：US20080081936A1
公开(公告)日：2008-04-03
申请号：US11540802
申请日：2006-09-29
申请人： Andrea G. Bozzano , Bipin V. Vora
发明人： Andrea G. Bozzano , Bipin V. Vora
IPC分类号： C07C1/00
CPC分类号： C07C11/04 , C07C1/20 , C07C6/04 , C07C11/06 , C10G3/44 , C10G3/57 , C10G11/00 , C10G2400/20 , Y02P30/42 , C07C11/02
摘要： Processing schemes and arrangements for the production of olefins and, more particularly, for the production of light olefins from a methanol feedstock are provided. Such processing schemes and arrangements integrate oxygenate conversion at higher pressures and with subsequent heavy olefins conversion processing to produce additional light olefin products.
摘要翻译： 提供了用于生产烯烃，特别是用于从甲醇原料生产轻质烯烃的加工方案和装置。 这种处理方案和装置将氧化合物转化率与较高压力和随后的重质烯烃转化处理相结合以产生额外的轻质烯烃产物。
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公开(公告)号：US06979394B2
公开(公告)日：2005-12-27
申请号：US10851417
申请日：2004-05-21
申请人： Andrea G. Bozzano , Kurt A. Detrick
发明人： Andrea G. Bozzano , Kurt A. Detrick
IPC分类号： C07C2/66 , C07C15/00 , C07C15/107 , C10G17/00 , C07C2/68
CPC分类号： C07C15/107 , C07C2/66 , C07C15/00 , Y02P20/584
摘要： A process for producing a product aromatic compound is disclosed which uses an on-stream alkylation reactor and an off-stream alkylation reactor, and in which at least a portion of the feed aromatic compound in the effluent stream of off-stream alkylation reactor undergoing regeneration is passed to the on-stream alkylation reactor. An embodiment of this process that uses on-stream and off-stream aromatic byproducts removal zones is also disclosed.
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10.发明申请公开(公告)号：US20130253243A1
公开(公告)日：2013-09-26
申请号：US13427706
申请日：2012-03-22
IPC分类号： C07C1/20
CPC分类号： C10G3/42 , C10G3/50 , C10G2300/1014 , C10G2300/1018 , C10G2400/20 , C10G2400/22 , C10G2400/28 , Y02P30/20
摘要： A method for producing a linear paraffin includes providing a natural oil in a feed stream, deoxygenating the natural oil to form a stream comprising paraffins, purifying the stream comprising paraffins to form a purified stream comprising paraffins, and separating a first fraction of paraffin product from the purified stream comprising paraffins. A method for producing a linear olefin includes providing a natural oil in a feed stream, deoxygenating the natural oil to form a stream comprising paraffins, dehydrogenating the stream comprising paraffins to form a stream comprising olefins, purifying the stream comprising olefins to form a purified stream comprising olefins, and separating a first fraction of olefin product from the purified stream comprising olefins.
摘要翻译： 制备线性链烷烃的方法包括在进料流中提供天然油，对天然油进行脱氧以形成包含链烷烃的物流，纯化包含链烷烃的物流以形成包含链烷烃的纯化物流，并将第一级石蜡产物从 纯化的料流包含石蜡。 制备线性烯烃的方法包括在进料流中提供天然油，使天然油脱氧以形成包含链烷烃的物流，使包含链烷烃的物流脱氢以形成包含烯烃的物流，纯化含有烯烃的物流以形成纯化物流 包括烯烃，并从包含烯烃的纯化流中分离出第一级烯烃产物。
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