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公开(公告)号：US20180208861A1
公开(公告)日：2018-07-26
申请号：US15871614
申请日：2018-01-15
Applicant: Phillips 66 Company
Inventor： Jianhua YAO , Hong XIE , Bruce B. RANDOLPH , Steven E. LUSK , Dhananjay B. GHONASGI , Jonathan R. MARDA
CPC classification number: C10G50/00 , B01D3/143 , B01J29/40 , C07C2/12 , C10G2300/1088 , C10G2400/02 , C10G2400/04
Abstract: The present disclosure relates generally processes and systems for converting a mixture of light hydrocarbons to liquid transportation fuels by first cracking the light hydrocarbons to an intermediate comprising olefins, which is converted by contacting with a catalyst comprising at least one zeolite in two separate conversion stages with an intervening recovery of liquid product. The first stage conversion favors oligomerization of larger olefins to form diesel range products that are collected prior to directing unconverted smaller olefins to be oligomerized in a second stage conversion conducted at a higher temperature and lower pressure.
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公开(公告)号：US20170240817A1
公开(公告)日：2017-08-24
申请号：US15433569
申请日：2017-02-15
Applicant: PHILLIPS 66 COMPANY
Inventor： Uchenna P. PAUL , Jianhua YAO
CPC classification number: C10G3/49 , C10G2300/202 , C10G2300/305 , C10G2400/02 , C10L1/06 , C10L2200/0469 , C10L2270/023 , Y02P30/20
Abstract: The present invention relates to processes for converting a feedstream comprising predominantly light alcohols into liquid transportation fuels in the gasoline boiling range. In certain embodiments, the feedstream is a bio-waste stream derived from the conversion of sorbitol or glycerol to propanediol.
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3.发明申请公开(公告)号：US20160186074A1
公开(公告)日：2016-06-30
申请号：US14964749
申请日：2015-12-10
Applicant: PHILLIPS 66 COMPANY
Inventor： Jianhua YAO , William D. HENNING , Walter E. ALVAREZ
CPC classification number: C10G11/18 , C10G3/57 , C10G2300/1011 , C10G2300/1096 , Y02P30/20
Abstract: System relating to the conversion of ethanol in a stripper unit of a fluidized catalytic cracking system. An ethanol stream comprising at least 4 volume percent water mixes with a catalyst in the stripper unit under conditions of temperature that favor conversion of the ethanol to hydrocarbons, thereby increasing incorporation of ethanol into liquid transportation fuels without exceeding regulatory limits on fuel vapor pressure. Certain embodiments additionally combine the ethanol stream with a hydrocarbon stream in the stripper and react in the presence of a catalyst to produce hydrocarbons that may have an increased boiling point, increased octane rating, decreased vapor pressure, decreased benzene content, or combinations of these properties.
Abstract translation: 与流化催化裂化系统的汽提器单元中的乙醇转化有关的系统。 在有利于乙醇转化为烃的温度的条件下，包含至少4体积％的水与催化剂混合的乙醇料流，从而增加乙醇在液体运输燃料中的并入，而不超过对燃料蒸气压力的限制。 某些实施方案另外将乙醇料流与汽提塔中的烃物流组合并在催化剂存在下反应生成可能具有增加的沸点，增加的辛烷值，降低的蒸汽压，降低的苯含量或这些性质的组合的烃 。
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公开(公告)号：US20160160133A1
公开(公告)日：2016-06-09
申请号：US14955984
申请日：2015-12-01
Applicant: PHILLIPS 66 COMPANY
Inventor： William D. HENNING , Walter E. ALVAREZ , Jianhua YAO
CPC classification number: C10G50/00 , C10G3/57 , C10G29/205 , C10G29/22 , C10G2300/1088 , C10G2400/02 , C10G2400/04 , C10G2400/08 , Y02P30/20
Abstract: Processes relating to the conversion of ethanol in a stripper unit of a fluidized catalytic cracking system. An ethanol stream mixes with a catalyst in the stripper unit under conditions of temperature that favor conversion of the ethanol to hydrocarbons, thereby increasing incorporation of ethanol into liquid transportation fuels without exceeding regulatory limits on fuel vapor pressure. Certain embodiments combine the ethanol stream with a hydrocarbon stream and react in the presence of a catalyst in a stripper to produce hydrocarbons that may have an increased boiling point, increased octane rating, decreased vapor pressure, decreased benzene content, or combinations thereof.
Abstract translation: 与流化催化裂化系统的汽提器单元中的乙醇转化相关的方法。 在有利于乙醇转化为烃的温度的条件下，乙醇流与脱汽器单元中的催化剂混合，从而增加乙醇在液体运输燃料中的并入，而不超过对燃料蒸汽压力的调节限制。 某些实施方案将乙醇流与烃流合并，并在催化剂存在下在汽提器中反应，以产生可能具有增加的沸点，增加的辛烷值，降低的蒸汽压，降低的苯含量或其组合的烃。
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公开(公告)号：US20180207626A1
公开(公告)日：2018-07-26
申请号：US15871630
申请日：2018-01-15
Applicant: PHILLIPS 66 COMPANY
Inventor： Jianhua YAO , Hong XIE , Bruce B. RANDOLPH , Steven E. LUSK , Dhananjay B. GHONASGI , Jonathan R. MARDA
CPC classification number: B01J29/40 , B01J19/24 , B01J2219/24 , C07C2/12 , C07C4/04 , C07C4/06 , C07C5/03 , C07C2529/40
Abstract: The present disclosure relates generally processes and systems for converting a mixture of light hydrocarbons to liquid transportation fuels by first cracking the light hydrocarbons to an intermediate comprising olefins, which is converted by contacting with a catalyst comprising at least one zeolite in two separate conversion stages with an intervening recovery of liquid product. The first stage conversion favors oligomerization of larger olefins to form diesel range products that are collected prior to directing unconverted smaller olefins to be oligomerized in a second stage conversion conducted at a higher temperature and lower pressure.
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Patent Agency Ranking
公开(公告)号：US20160340594A1
公开(公告)日：2016-11-24
申请号：US14955961
申请日：2015-12-01
Applicant: PHILLIPS 66 COMPANY
Inventor： William D. HENNING , Walter E. ALVAREZ , Jianhua YAO
CPC classification number: C10G3/42 , B01J8/0055 , B01J8/388 , B01J2208/00823 , C10G11/18 , C10G2300/202 , Y02P30/20
Abstract: Systems relating to the conversion of ethanol in a stripper unit of a fluidized catalytic cracking system. An ethanol stream mixes with a catalyst in the stripper unit under conditions of temperature that favor conversion of the ethanol to hydrocarbons, thereby increasing incorporation of ethanol into liquid transportation fuels without exceeding regulatory limits on fuel vapor pressure. Certain embodiments combine the ethanol stream with a hydrocarbon stream and react in the presence of a catalyst in the stripper to produce hydrocarbons that may have an increased boiling point, increased octane rating, decreased vapor pressure, decreased benzene content, or combinations thereof.
Abstract translation: 与流化催化裂化系统的汽提器单元中的乙醇转化有关的系统。 在有利于乙醇转化为烃的温度的条件下，乙醇流与脱汽器单元中的催化剂混合，从而增加乙醇在液体运输燃料中的并入，而不超过对燃料蒸汽压力的调节限制。 某些实施方案将乙醇流与烃流合并，并在催化剂存在下在汽提器中反应，以产生可能具有升高的沸点，增加的辛烷值，降低的蒸气压，降低的苯含量或其组合的烃。
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公开(公告)号：US20150376514A1
公开(公告)日：2015-12-31
申请号：US14750541
申请日：2015-06-25
Applicant: PHILLIPS 66 COMPANY
Inventor： Jianhua YAO , Sourabh S. PANSARE , Lianhui DING
IPC: C10G67/02
CPC classification number: C10G65/12 , C10G45/00 , C10G2300/1011 , C10G2400/02 , Y02P30/20
Abstract: Biomass derived gas oil is blended with petroleum derived gas oil and upgrading into more salable and more valuable products by co-processing the blended material in a gas oil hydrocracking system comprising two reactors where the blended material is first hydrotreated and then hydrocracked.
Abstract translation: 生物质衍生瓦斯油与石油衍生瓦斯油混合，并通过在包含两个反应器的瓦斯油加氢裂化系统中共混处理混合材料，将混合材料首先加氢处理然后加氢裂化，从而升级成更可销售和更有价值的产品。
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公开(公告)号：US20160186077A1
公开(公告)日：2016-06-30
申请号：US14964766
申请日：2015-12-10
Applicant: PHILLIPS 66 COMPANY
Inventor： Jianhua YAO , William D. HENNING , Walter E. ALVAREZ
CPC classification number: C10G57/005 , C10G3/42 , C10G11/18 , C10G50/00 , C10G57/02 , C10L1/04 , C10L2200/0469 , Y02P30/20
Abstract: Processes relating to the conversion of ethanol in a stripper unit of a fluidized catalytic cracking system. An ethanol stream comprising at least 4 volume percent water mixes with a catalyst in the stripper unit under conditions of temperature that favor conversion of the ethanol to hydrocarbons, thereby increasing incorporation of ethanol into liquid transportation fuels without exceeding regulatory limits on fuel vapor pressure. Certain embodiments additionally combine the ethanol stream with a hydrocarbon stream in the stripper and react in the presence of a catalyst to produce hydrocarbons that may have an increased boiling point, increased octane rating, decreased vapor pressure, decreased benzene content, or combinations of these properties.
Abstract translation: 与流化催化裂化系统的汽提器单元中的乙醇转化相关的方法。 在有利于乙醇转化为烃的温度的条件下，包含至少4体积％的水与催化剂混合的乙醇料流，从而增加乙醇在液体运输燃料中的并入，而不超过对燃料蒸气压力的限制。 某些实施方案另外将乙醇料流与汽提塔中的烃物流组合并在催化剂存在下反应生成可能具有增加的沸点，增加的辛烷值，降低的蒸汽压，降低的苯含量或这些性质的组合的烃 。
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公开(公告)号：US20160168044A1
公开(公告)日：2016-06-16
申请号：US14958198
申请日：2015-12-03
Applicant: PHILLIPS 66 COMPANY
Inventor： Tie-Pan SHI , Jianhua YAO , Brian C. DUNN , Edward L. SUGHRUE
CPC classification number: C07C1/20 , C07C2523/28 , C07C2523/30 , C07C2523/755 , C07C2523/888 , C10G3/46 , C10G3/50 , C07C11/06 , C07C9/08
Abstract: Processes relating to a one-step conversion to directly produce propylene from glycerol with a hydrotreating catalyst under a constrained hydrogen/glycerol feed ratio.
Abstract translation: 与一步转化相关的方法，在受限的氢/甘油进料比下，用加氢处理催化剂从甘油直接生产丙烯。
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公开(公告)号：US20140322087A1
公开(公告)日：2014-10-30
申请号：US14329592
申请日：2014-07-11
Applicant: PHILLIPS 66 COMPANY
Inventor： Jianhua YAO , Edward L. SUGHRUE, II , Ronald E. BROWN
IPC: B01J19/26
CPC classification number: B01J19/26 , C10G3/46 , C10G3/50 , C10G49/02 , C10G2300/1011 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , Y02E50/13 , Y02P30/20
Abstract: A method of hydrotreating liquefied biomass feedstock with diesel feedstock to produce alkanes is demonstrated that prevents damage to the reactor catalyst, reduces coke production, and converts nearly all of the polyols to alkanes. In order to mitigate the potential coking issue and to moderate the temperature of the catalyst bed while maintaining high conversion for sugar alcohol to hydrocarbon via a hydrotreating process, a diesel feedstock is fed over the reactor catalyst with multiple injections of polyol feedstock along the reactor.
Abstract translation: 证明了用柴油原料加氢处理液化生物质原料以生产烷烃的方法，其防止对反应器催化剂的损害，减少焦炭产生，并将几乎所有多元醇转化为烷烃。 为了减轻潜在的焦化问题并缓解催化剂床的温度，同时通过加氢处理方法保持糖醇与烃的高转化率，将柴油原料在反应器催化剂上沿反应器多次注入多元醇原料。
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