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公开(公告)号：US20120104322A1
公开(公告)日：2012-05-03
申请号：US12917781
申请日：2010-11-02
Applicant: Colleen Costello , Lisa King , Paul Barger , Deng-Yang Jan , Robert B. James , Kurt Vanden Bussche
Inventor： Colleen Costello , Lisa King , Paul Barger , Deng-Yang Jan , Robert B. James , Kurt Vanden Bussche
CPC classification number: B01J8/26 , B01J23/002 , B01J35/0006 , B01J38/12 , B01J38/28 , B01J2523/00 , C01B3/38 , C01B3/42 , C01B2203/0261 , C01B2203/1041 , Y02P20/52 , Y02P20/584 , B01J2523/12 , B01J2523/24 , B01J2523/3706 , B01J2523/51 , B01J2523/842 , B01J2523/847
Abstract: Embodiments of a process for producing syngas comprising hydrogen and carbon monoxide from a gas stream comprising methane are provided. The process comprises the step of contacting the gas stream with a two-component catalyst system comprising an apatite component and a perovskite component at reaction conditions effective to convert the methane to the syngas.
Abstract translation: 提供了由包含甲烷的气流产生包含氢气和一氧化碳的合成气的方法的实施方案。 该方法包括使气流与包含磷灰石组分和钙钛矿组分的双组分催化剂体系在有效将甲烷转化为合成气的反应条件下接触的步骤。
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12.发明申请Method for Drying Regenerated Catalyst in Route to a Propane Dehydrogenation Reactor 失效在丙烷脱氢反应器中干燥再生催化剂的方法公开(公告)号：US20120053047A1
公开(公告)日：2012-03-01
申请号：US12871277
申请日：2010-08-30
Applicant: David N. Myers , Daniel N. Myers , Paolo Palmas , Laura E. Leonard , Wolfgang A. Spieker
Inventor： David N. Myers , Daniel N. Myers , Paolo Palmas , Laura E. Leonard , Wolfgang A. Spieker
IPC: B01J38/02
CPC classification number: B01J23/94 , B01J23/96 , B01J35/0026 , B01J38/02 , B01J38/04 , B01J38/12 , B01J38/28 , B01J38/30
Abstract: An apparatus and process are presented for drying a catalyst in a reactor-regenerator system. The process includes a continuous operating system with catalyst circulating between a reactor and regenerator, and the catalyst is dried before returning the catalyst to the reactor. The process uses air that is split between the drying stage and the combustion stage without adding equipment outside of the regenerator, minimizing energy, capital cost, and space requirements.
Abstract translation: 提出了用于干燥反应器 - 再生器系统中的催化剂的装置和方法。 该方法包括具有在反应器和再生器之间循环的催化剂的连续操作系统，并且在将催化剂返回到反应器之前将催化剂干燥。 该过程使用在干燥阶段和燃烧阶段之间分配的空气，而不需要在再生器外部添加设备，从而最小化能源，资本成本和空间要求。
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公开(公告)号：US08618012B2
公开(公告)日：2013-12-31
申请号：US12757594
申请日：2010-04-09
Applicant: Phillip K. Niccum , Alan M. Claude , Robert B. Peterson
Inventor： Phillip K. Niccum , Alan M. Claude , Robert B. Peterson
CPC classification number: B01J23/92 , B01J23/40 , B01J23/94 , B01J29/90 , B01J38/02 , B01J38/12 , B01J38/28 , B01J38/34 , B01J38/36
Abstract: Systems and methods for regenerating a spent catalyst are provided. The method can include mixing a spent catalyst with a carrier fluid to provide a mixture. The spent catalyst can include carbon deposited on at least a portion thereof. The carrier fluid can include an oxygen containing gas. The mixture can be introduced to or above an upper surface of a dense phase catalyst zone disposed within a regenerator. A gas can be introduced to a lower zone of the dense phase catalyst zone. At least a portion of the carbon deposited on the catalyst can be combusted to provide a flue gas, heat, and a regenerated catalyst.
Abstract translation: 提供了用于再生废催化剂的系统和方法。 该方法可以包括将废催化剂与载体流体混合以提供混合物。 废催化剂可以包括沉积在其至少一部分上的碳。 载体流体可以包括含氧气体。 混合物可以被引入设置在再生器内的致密相催化剂区域的上表面上方或上方。 可以将气体引入密相催化剂区的下部区域。 沉积在催化剂上的碳的至少一部分可以燃烧以提供烟气，热和再生催化剂。
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公开(公告)号：US08314043B2
公开(公告)日：2012-11-20
申请号：US12515208
申请日：2007-10-30
IPC: B01J38/40
CPC classification number: C10G2/342 , B01J23/94 , B01J38/28 , B01J38/30 , C10G2/332 , C10G2/344 , C10G2300/703
Abstract: A process is disclosed for the regeneration of a deactivated wax covered Fischer-Tropsch catalyst, a pumpable suspension of deactivated catalyst being injected into a hot gas stream and the regenerated catalyst then being separated off from the gas stream, optionally further treated by calcination and/or reduction.
Abstract translation: 公开了一种用于再生失活的蜡覆盖的费 - 托催化剂的方法，将失活的催化剂的可泵送悬浮液注入热气流中，再生的催化剂然后与气流分离，任选进一步通过煅烧和/ 或减少。
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Patent Agency Ranking
公开(公告)号：US07915191B2
公开(公告)日：2011-03-29
申请号：US12490008
申请日：2009-06-23
Applicant: Brian W. Hedrick
Inventor： Brian W. Hedrick
CPC classification number: F27B15/08 , B01J23/88 , B01J23/888 , B01J23/8885 , B01J23/94 , B01J38/02 , B01J38/20 , B01J38/28 , B01J38/34 , B01J38/70
Abstract: This invention is directed to a method and apparatus for regenerating a catalyst used in an FCC unit, including providing a spent catalyst into an upper portion of a regenerator, maintaining a calcination phase, a gasification phase, and a combustion phase of fluidized catalyst in the regenerator, combusting carbon in the combustion phase and producing a combustion flue gas, reacting carbon in the gasification phase with the combustion flue gas to form a carbon monoxide rich flue gas, and calcining the spent catalyst with the carbon monoxide rich flue gas.
Abstract translation: 本发明涉及一种用于再生FCC单元中使用的催化剂的方法和装置，包括将废催化剂提供到再生器的上部，维持煅烧阶段，气化阶段和流化催化剂的燃烧阶段 再生器，在燃烧阶段燃烧碳并产生燃烧烟道气，使气化阶段中的碳与燃烧烟道气反应，形成富一氧化碳烟道气，并用一氧化碳浓度烟气煅烧废催化剂。
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公开(公告)号：US20100081562A1
公开(公告)日：2010-04-01
申请号：US12515208
申请日：2006-10-30
Applicant: Hermanus Gerhardus Jozef Lansink Rotgerink
IPC: B01J20/34
CPC classification number: C10G2/342 , B01J23/94 , B01J38/28 , B01J38/30 , C10G2/332 , C10G2/344 , C10G2300/703
Abstract: A process is disclosed for the regeneration of a deactivated wax covered Fischer-Tropsch catalyst, a pumpable suspension of deactivated catalyst being injected into a hot gas stream and the regenerated catalyst then being separated off from the gas stream, optionally further treated by calcination and/or reduction.
Abstract translation: 公开了一种用于再生失活的蜡覆盖的费 - 托催化剂的方法，将失活的催化剂的可泵送悬浮液注入热气流中，再生的催化剂然后与气流分离，任选进一步通过煅烧和/ 或减少。
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公开(公告)号：US20060287562A1
公开(公告)日：2006-12-21
申请号：US11448680
申请日：2006-06-08
Applicant: Emmanuelle Guillon , Eric Sanchez
Inventor： Emmanuelle Guillon , Eric Sanchez
IPC: C07C2/68
CPC classification number: B01J8/12 , B01J29/06 , B01J29/084 , B01J29/90 , B01J35/023 , B01J38/28 , B01J38/56 , B01J2208/00292 , B01J2219/0004 , C07C2/66 , C07C2529/08 , C07C2529/18 , C07C2529/70 , Y02P20/584 , Y10S585/901 , C07C15/107
Abstract: A process for the production of phenyl alkanes by catalytic alkylation on a solid acid catalyst employs at least one moving-bed reactor. This process comprises a catalytic alkylation stage of an aromatic compound by at least one olefin that has 9 to 16 carbon atoms per molecule, combined with a catalyst reactivation circuit. Each reactor contains n reaction zones, whereby each of said zones consists of an acidic solid catalyst, optionally different from one zone to the next. Entering each reaction zone, a fraction of the total amount of olefins necessary to the alkylation reaction is introduced. The phenyl alkanes that are obtained by the process according to the invention are particularly suitable for the production of detergents.
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公开(公告)号：US06852668B2
公开(公告)日：2005-02-08
申请号：US09998222
申请日：2001-12-03
Applicant: Hugo Ignacio de Lasa , Tarek Ei Solh , Kai Jarosch
Inventor： Hugo Ignacio de Lasa , Tarek Ei Solh , Kai Jarosch
IPC: B01J21/04 , B01J23/755 , B01J29/14 , B01J35/02 , B01J35/10 , B01J37/02 , B01J38/28 , C01B3/40 , C01B3/44
CPC classification number: B01J37/0205 , B01J21/04 , B01J23/755 , B01J29/146 , B01J35/002 , B01J35/006 , B01J35/0073 , B01J35/023 , B01J35/10 , B01J35/1009 , B01J35/1019 , B01J38/28 , C01B3/40 , C01B3/44 , C01B2203/0233 , C01B2203/0238 , C01B2203/04 , C01B2203/0465 , C01B2203/1052 , C01B2203/1082 , C01B2203/1241 , Y02P20/52 , Y02P20/584
Abstract: A Nickel (Ni) catalyst for facilitating a hydrocarbon reforming process, and an improved process based on the catalyst. The catalyst comprising discrete Ni crystallites having a size in the range of between 150 and 250 Å and a distribution on said support element of no more than 0.14 square meters of exposed nickel/square meter of support.
Abstract translation: 用于促进烃重整过程的镍（Ni）催化剂和基于催化剂的改进方法。 该催化剂包括尺寸在150和250埃之间的离散的Ni微晶，并且在所述支撑元件上的分布不超过0.14平方米的暴露的镍/平方米的载体。
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公开(公告)号：US20030103893A1
公开(公告)日：2003-06-05
申请号：US09998222
申请日：2001-12-03
Inventor： Hugo Ignacio de Lasa , Tarek Eisolh , Kai Jarosch
IPC: C01B003/26 , B01J023/755
CPC classification number: B01J37/0205 , B01J21/04 , B01J23/755 , B01J29/146 , B01J35/002 , B01J35/006 , B01J35/0073 , B01J35/023 , B01J35/10 , B01J35/1009 , B01J35/1019 , B01J38/28 , C01B3/40 , C01B3/44 , C01B2203/0233 , C01B2203/0238 , C01B2203/04 , C01B2203/0465 , C01B2203/1052 , C01B2203/1082 , C01B2203/1241 , Y02P20/52 , Y02P20/584
Abstract: A Nickel (Ni) catalyst for facilitating a hydrocarbon reforming process, and an improved process based on the catalyst. The catalyst comprising discrete Ni crystallites having a size in the range of between 150 and 250 null and a distribution on said support element of no more than 0.14 square meters of exposed nickel/square meter of support
Abstract translation: 用于促进烃重整过程的镍（Ni）催化剂和基于催化剂的改进方法。 该催化剂包括分散的Ni微晶，其尺寸在150-250平方的范围内，所述支撑元件上的分布不超过0.14平方米的暴露的镍/平方米的载体
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