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公开(公告)号：US20050065391A1
公开(公告)日：2005-03-24
申请号：US10844852
申请日：2004-05-13
Applicant: Sean Gattis , Edward Peterson
Inventor： Sean Gattis , Edward Peterson
IPC: C07C2/00 , C07C2/76 , C07C4/00 , C10G20060101 , C10G50/00
CPC classification number: C10G50/00 , Y10S585/943
Abstract: A process for converting natural gas to liquid hydrocarbons comprising heating the gas through a selected range of temperature for sufficient time and/or combustion of the gas at a sufficient temperature and under suitable conditions for a reaction time sufficient to convert a portion of the gas stream to reactive hydrocarbon products, primarily ethylene or acetylene. The gas containing acetylene may be separated such that acetylene is converted to ethylene. The ethylene product(s) may be reacted in the presence of an acidic catalyst to produce a liquid, a portion of which will be predominantly naphtha or gasoline. A portion of the incoming natural gas or hydrogen produced in the process may be used to heat the remainder of the natural gas to the selected range of temperature. Reactive gas components are used in a catalytic liquefaction step and/or for alternate chemical processing.
Abstract translation: 一种将天然气转化为液体烃的方法，包括将气体在选定的温度范围内加热足够的时间和/或在足够的温度和适当的条件下燃烧气体以使反应时间足以转化一部分气流 反应性烃产物，主要是乙烯或乙炔。 可以分离含乙炔的气体，使乙炔转化为乙烯。 乙烯产物可以在酸性催化剂的存在下反应以产生液体，其中一部分主要是石脑油或汽油。 在该过程中产生的一部分进入的天然气或氢气可用于将剩余的天然气加热到所选择的温度范围。 反应性气体组分用于催化液化步骤和/或用于替代化学处理。
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公开(公告)号：US20070021638A1
公开(公告)日：2007-01-25
申请号：US11383325
申请日：2006-05-15
Applicant: Marvin Johnson , Edward Peterson , Sean Gattis
Inventor： Marvin Johnson , Edward Peterson , Sean Gattis
IPC: C07C7/167
CPC classification number: B01J37/08 , B01J21/04 , B01J23/44 , B01J23/50 , B01J23/52 , B01J23/60 , B01J23/62 , B01J23/6562 , B01J23/66 , B01J35/008 , B01J35/08 , B01J37/18 , C07C7/167 , C07C2523/56 , C07C2523/60 , C07C2523/62 , C07C2523/64
Abstract: A process and catalyst for the liquid phase selective hydrogenation of alkynes to alkenes with high selectivity to alkenes relative to alkanes, high alkyne conversion, and sustained catalytic activity comprising a reactant comprising an alkyne and a non-hydrocarbon solvent/absorbent, contacting the reactant stream with a hydrogen-containing stream in the presence of a supported, promoted, Group VIII catalyst, removing the solvent/absorbent, and recovering the alkene product.
Abstract translation: 一种用于相对于烷烃对烯烃具有高选择性的烯烃至烯烃的液相选择性氢化的方法和催化剂，高炔转化率和持续的催化活性，其包含含有炔烃和非烃溶剂/吸收剂的反应物，使反应物流 在含有载体的促进的VIII族催化剂的存在下，将含氢的物流除去溶剂/吸收剂，并回收烯烃产物。
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Patent Agency Ranking
3.发明申请Process for the conversion of natural gas to reactive gaseous products comprising ethylene 有权将天然气转化为包含乙烯的反应性气体产物的方法公开(公告)号：US20050065392A1
公开(公告)日：2005-03-24
申请号：US10845569
申请日：2004-05-13
Applicant: Edward Peterson , Sean Gattis
Inventor： Edward Peterson , Sean Gattis
Abstract: A process for converting natural gas to reactive gaseous products, comprising heating the gas through a selected range of temperature for sufficient time, or combusting a portion of the gas at a sufficient temperature and under suitable conditions for a reaction time sufficient to convert a portion of the gas stream to reactive hydrocarbon products, primarily ethylene or acetylene. The gas containing acetylene may be separated such that acetylene is converted to ethylene. A portion of the incoming natural gas or hydrogen produced in the process may be used to heat the remainder of the natural gas to the selected range of temperature. Unrecovered gaseous products resulting from the reactions may be used to provide heat to the process by which reactive gas components are produced. Recovered gaseous products, together or individually, may be reserved for subsequent use or storage.
Abstract translation: 一种将天然气转化成反应性气体产物的方法，包括将气体加热到选定的温度范围足够的时间，或在足够的温度和适当的条件下将一部分气体燃烧足以使一部分 气流转化为反应性烃产物，主要是乙烯或乙炔。 可以分离含乙炔的气体，使乙炔转化为乙烯。 在该过程中产生的一部分进入的天然气或氢气可用于将剩余的天然气加热到所选择的温度范围。 由反应产生的未回收的气态产物可用于向生成反应性气体组分的方法提供热量。 回收的气态产品，一起或单独地可以保留用于随后的使用或储存。
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公开(公告)号：US20070191655A1
公开(公告)日：2007-08-16
申请号：US11669451
申请日：2007-01-31
Applicant: Sean Gattis , Edward Peterson
Inventor： Sean Gattis , Edward Peterson
CPC classification number: C10G50/00 , Y10S585/943
Abstract: A process for converting natural gas to liquid hydrocarbons comprising heating the gas through a selected range of temperature for sufficient time and/or combustion of the gas at a sufficient temperature and under suitable conditions for a reaction time sufficient to convert a portion of the gas stream to reactive hydrocarbon products, primarily ethylene or acetylene. The gas containing acetylene may be separated such that acetylene is converted to ethylene. The ethylene product(s) may be reacted in the presence of an acidic catalyst to produce a liquid, a portion of which will be predominantly naphtha or gasoline. A portion of the incoming natural gas or hydrogen produced in the process may be used to heat the remainder of the natural gas to the selected range of temperature. Reactive gas components are used in a catalytic liquefaction step and/or for alternate chemical processing.
Abstract translation: 一种将天然气转化为液体烃的方法，包括将气体在选定的温度范围内加热足够的时间和/或在足够的温度和适当的条件下燃烧气体以使反应时间足以转化一部分气流 反应性烃产物，主要是乙烯或乙炔。 可以分离含乙炔的气体，使乙炔转化为乙烯。 乙烯产物可以在酸性催化剂的存在下反应以产生液体，其中一部分主要是石脑油或汽油。 在该过程中产生的一部分进入的天然气或氢气可用于将剩余的天然气加热到所选择的温度范围。 反应性气体组分用于催化液化步骤和/或用于替代化学处理。
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公开(公告)号：US20070021637A1
公开(公告)日：2007-01-25
申请号：US11346036
申请日：2006-02-02
Applicant: Edward Peterson , Sean Gattis
Inventor： Edward Peterson , Sean Gattis
CPC classification number: C07C7/10 , C07C7/163 , C07C7/167 , C07C2523/44 , C07C11/02
Abstract: A method for the absorption of alkynes and diolefins from an ethylene or propylene containing stream with conversion to alkenes by catalytic hydrogenation in a solvent over a fixed bed comprising a supported catalyst.
Abstract translation: 一种从含乙烯或丙烯的物流中吸收炔烃和二烯烃的方法，其通过在溶剂中通过在包含负载型催化剂的固定床上进行催化氢化而转化成烯烃。
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公开(公告)号：US20050049445A1
公开(公告)日：2005-03-03
申请号：US10728310
申请日：2003-12-04
Applicant: Marvin Johnson , Edward Peterson , Sean Gattis
Inventor： Marvin Johnson , Edward Peterson , Sean Gattis
IPC: B01J23/44 , B01J23/60 , B01J23/62 , B01J23/656 , B01J23/66 , C07C5/02 , C07C5/09 , C07C7/10 , C07C7/167
CPC classification number: B01J37/08 , B01J21/04 , B01J23/44 , B01J23/50 , B01J23/52 , B01J23/60 , B01J23/62 , B01J23/6562 , B01J23/66 , B01J35/008 , B01J35/08 , B01J37/18 , C07C7/167 , C07C2523/56 , C07C2523/60 , C07C2523/62 , C07C2523/64
Abstract: A process for the liquid phase selective hydrogenation of alkynes to alkenes with high selectivity to alkenes relative to alkanes, high alkyne conversion, and sustained catalytic activity comprising a reactant comprising an alkyne and a non-hydrocarbon solvent/absorbent, contacting the reactant stream with a hydrogen-containing stream in the presence of a supported, promoted, Group VIII catalyst, removing the solvent/absorbent, and recovering the alkene product.
Abstract translation: 将烯烃液相选择性氢化为烯烃的方法，其相对于烷烃具有对烯烃的高选择性，高炔转化率和持续的催化活性，其包括含有炔烃和非烃溶剂/吸收剂的反应物，使反应物流与 在负载的，促进的VIII族催化剂存在下，含氢的物流，去除溶剂/吸收剂，并回收烯烃产物。
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公开(公告)号：US20050048658A1
公开(公告)日：2005-03-03
申请号：US10727919
申请日：2003-12-04
Applicant: Marvin Johnson , Edward Peterson , Sean Gattis
Inventor： Marvin Johnson , Edward Peterson , Sean Gattis
IPC: B01J23/44 , B01J23/48 , B01J23/50 , B01J23/52 , B01J23/60 , B01J23/62 , B01J23/656 , B01J23/66 , B01J35/00 , B01J37/00 , B01J37/02 , B01J37/18 , C10G45/34 , C10G45/40 , G01N31/10
CPC classification number: B01J23/50 , B01J23/44 , B01J23/48 , B01J23/52 , B01J23/60 , B01J23/62 , B01J23/6562 , B01J23/66 , B01J35/002 , B01J37/0036 , B01J37/009 , B01J37/0205 , B01J37/18 , C10G45/34 , C10G45/40 , C10G2400/20
Abstract: A composition and method for preparation of a catalyst for the liquid phase selective hydrogenation of alkynes to alkenes with high selectivity to alkenes relative to alkanes, high alkyne conversion, and sustained catalytic activity comprising a Group VIII metal and a Group IB, Group IIB, Group IIIA, and/or Group VIIB promoter on a particulate support.
Abstract translation: 一种用于制备用于相对于烷烃对烯烃具有高选择性的炔烃至烯烃的液相选择性氢化的催化剂的组合物和方法，具有高炔烃转化率和持续催化活性的组合物和方法，其包含VIII族金属和IB族，IIB族， IIIA和/或VIIB族促进剂。
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