专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明申请

US20150060326A1 PRODUCTION OF LIQUID HYDROCARBONS 有权
标题翻译：生产液体碳氢化合物
公开(公告)号：US20150060326A1
公开(公告)日：2015-03-05
申请号：US14389817
申请日：2013-04-05
申请人： IGTL TECHNOLOGY LTD
发明人： Richard John Hyman
IPC分类号： C10L1/04
CPC分类号： C10L1/04 , C10G2/332 , C10G2/343 , C10G35/04 , C10G45/58 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10L1/06 , C10L1/08 , C10L2200/0438 , C10L2200/0446 , C10L2200/0492 , C10L2270/023 , C10L2270/026
摘要： The invention relates to a process for the conversion of hydrogen and one or more oxides of carbon to hydrocarbons, which process comprises: contacting hydrogen and one or more oxides of carbon with a catalyst in a reaction zone; removing from the reaction zone an outlet stream comprising unreacted hydrogen, unreacted one or more oxides of carbon and one or more hydrocarbons and feeding the outlet stream to a separation zone in which the outlet stream is divided into at least three fractions, in which; a first fraction predominantly comprises unreacted hydrogen, unreacted one or more oxides of carbon and hydrocarbons having from 1 to 4 carbon atoms; a second fraction predominantly comprises hydrocarbons having 5 to 9 carbon atoms, at least a portion of which hydrocarbons having from 5 to 9 carbon atoms are olefinic; and a third fraction predominantly comprises hydrocarbons having 10 or more carbon atoms; characterised in that at least a portion of the second fraction is recycled to the reaction zone.
摘要翻译：本发明涉及一种将氢和一种或多种碳氧化物转化成烃的方法，该方法包括：使氢和一种或多种碳氧化物与反应区中的催化剂接触; 从反应区域除去包含未反应的氢，未反应的一种或多种碳和一种或多种烃的氧化物的出口物流，并将出口物流输送到分离区，其中出口物流被分成至少三个馏分。第一级分主要包括未反应的氢，未反应的一种或多种碳和碳原子数为1至4的氧化物; 第二部分主要包含具有5至9个碳原子的烃，其中至少一部分具有5至9个碳原子的烃是烯属的; 并且第三级分主要包含具有10个或更多个碳原子的烃; 其特征在于，所述第二级分的至少一部分被再循环至所述反应区。

2. 发明授权

US09783751B2 Production of liquid hydrocarbons 有权
公开(公告)号：US09783751B2
公开(公告)日：2017-10-10
申请号：US14389817
申请日：2013-04-05
申请人： IGTL TECHNOLOGY LTD
发明人： Richard John Hyman
IPC分类号： C10G2/00 , C10L1/04 , C10G35/04 , C10G45/58 , C10L1/06 , C10L1/08
CPC分类号： C10L1/04 , C10G2/332 , C10G2/343 , C10G35/04 , C10G45/58 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10L1/06 , C10L1/08 , C10L2200/0438 , C10L2200/0446 , C10L2200/0492 , C10L2270/023 , C10L2270/026
摘要： The invention relates to a process for the conversion of hydrogen and one or more oxides of carbon to hydrocarbons, which process comprises: contacting hydrogen and one or more oxides of carbon with a catalyst in a reaction zone; removing from the reaction zone an outlet stream comprising unreacted hydrogen, unreacted one or more oxides of carbon and one or more hydrocarbons and feeding the outlet stream to a separation zone in which the outlet stream is divided into at least three fractions, in which; a first fraction predominantly comprises unreacted hydrogen, unreacted one or more oxides of carbon and hydrocarbons having from 1 to 4 carbon atoms; a second fraction predominantly comprises hydrocarbons having 5 to 9 carbon atoms, at least a portion of which hydrocarbons having from 5 to 9 carbon atoms are olefinic; and a third fraction predominantly comprises hydrocarbons having 10 or more carbon atoms; characterized in that at least a portion of the second fraction is recycled to the reaction zone.

3. 发明授权

US09908110B2 Methods of preparation and forming supported active metal catalysts and precursors 有权
公开(公告)号：US09908110B2
公开(公告)日：2018-03-06
申请号：US14351920
申请日：2012-10-22
申请人： IGTL TECHNOLOGY LTD
发明人： Richard Hyman
IPC分类号： B01J23/02 , B01J29/80 , B01J29/14 , B01J37/18 , C10G2/00 , B01J35/00 , B01J29/40 , B01J37/03 , B01J37/02
CPC分类号： B01J29/80 , B01J29/146 , B01J29/40 , B01J35/0006 , B01J37/0207 , B01J37/035 , B01J37/18 , B01J2229/186 , B01J2229/38 , B01J2229/42 , B01J2523/00 , C10G2/334 , B01J2523/13 , B01J2523/17 , B01J2523/31 , B01J2523/3712 , B01J2523/41 , B01J2523/842
摘要： The invention relates to a method of preparing a supported catalyst, which method comprises the steps of; (i) providing a porous catalyst support comprising a framework having an internal pore structure comprising one or more pores which internal pore structure comprises a precipitant; (ii) contacting the catalyst support with a solution or colloidal suspension comprising a catalytically active metal such that, on contact with the precipitant, particles comprising the catalytically active metal are precipitated within the internal pore structure of the framework of the catalyst support. The invention also relates to supported catalysts made according to the above method, and to use of the catalysts in catalyzing chemical reactions, for example in the Fischer Tropsch synthesis of hydrocarbons.

4. 发明申请

US20150148573A1 OLIGOMERISATION OF OLEFINS FOR THE PRODUCTION OF SYNTHETIC FUEL 审中-公开
标题翻译：用于生产合成燃料的烯烃的低级化
公开(公告)号：US20150148573A1
公开(公告)日：2015-05-28
申请号：US14402526
申请日：2013-05-21
申请人： IGTL TECHNOLOGY LTD
发明人： Richard Hyman , Alfred Ecker
IPC分类号： C10L1/04 , C07C2/12
CPC分类号： C10L1/04 , C07C2/12 , C07C2529/06 , C10G50/00 , C10G69/126 , C10L1/08 , C10L2200/0469 , C10L2270/026 , C10L2270/04
摘要： The invention relates to a synthetic hydrocarbon fuel composition, and a process for making such a fuel composition, in which the fuel composition has the following properties: a) a boiling point distribution having (i) a 10% recovery of 205° C. or less and (ii) an end point of 300° C. or less; b) a freezing point of −47° C. or less; and c) a density at 15° C. of at least 775 kg/m3. A process for producing the fuel composition comprises the oligomerisation of olefins over an oligomerisation catalyst. In addition the invention relates to a process for producing hydrocarbons comprising contacting one or more olefins with an oligomerisation catalyst in a reaction zone under conditions sufficient to cause oligomerisation of olefins, and removing an outlet stream comprising products of olefin oligomerisation from the reaction zone, wherein the oligomerisation catalyst comprises a crystalline zeolite Brønsted acid catalyst, whose crystals comprise an inorganic oxide framework with an internal pore structure, and an external surface, in which the ratio of the number of Brønsted acid sites on the external surface compared to the internal pore structure is in the range of from 0.1 to 20% and/or the ratio of the surface area of the internal pore structure compared to the external crystal surface area is in the range of from 5 to 1000.
摘要翻译：本发明涉及一种合成烃燃料组合物及其制备方法，其中该燃料组合物具有以下特性：a）沸点分布，其具有（i）回收率为205℃的10％或（ii）终点为300℃以下; b）-47℃或更低的凝固点; 和c）在15℃下的密度为至少775kg / m 3。制备燃料组合物的方法包括在低聚催化剂上烯烃的低聚。此外，本发明涉及一种生产烃的方法，包括在足以使烯烃低聚的条件下在反应区中使一种或多种烯烃与低聚催化剂接触，以及从反应区除去包含烯烃低聚产物的出口物流，其中低聚催化剂包括结晶沸石布朗斯台德酸催化剂，其晶体包含具有内部孔结构的无机氧化物骨架和外表面，其中外表面上的布朗斯台德酸位数与内部孔结构相比的比率在0.1〜20％的范围内和/或内部孔结构的表面积与外部晶体表面积的比例在5〜1000的范围内。

5. 发明申请

US20170253819A1 PRODUCTION OF LIQUID HYDROCARBONS 审中-公开
公开(公告)号：US20170253819A1
公开(公告)日：2017-09-07
申请号：US15485435
申请日：2017-04-12
申请人： IGTL TECHNOLOGY LTD
发明人： Richard John HYMAN
IPC分类号： C10L1/04 , C10L1/06 , C10G45/58 , C10G2/00 , C10G35/04 , C10L1/08
CPC分类号： C10L1/04 , C10G2/332 , C10G2/343 , C10G35/04 , C10G45/58 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10L1/06 , C10L1/08 , C10L2200/0438 , C10L2200/0446 , C10L2200/0492 , C10L2270/023 , C10L2270/026
摘要： The invention relates to a process for the conversion of hydrogen and one or more oxides of carbon to hydrocarbons, which process comprises: contacting hydrogen and one or more oxides of carbon with a catalyst in a reaction zone; removing from the reaction zone an outlet stream comprising unreacted hydrogen, unreacted one or more oxides of carbon and one or more hydrocarbons and feeding the outlet stream to a separation zone in which the outlet stream is divided into at least three fractions, in which; a first fraction predominantly comprises unreacted hydrogen, unreacted one or more oxides of carbon and hydrocarbons having from 1 to 4 carbon atoms; a second fraction predominantly comprises hydrocarbons having 5 to 9 carbon atoms, at least a portion of which hydrocarbons having from 5 to 9 carbon atoms are olefinic; and a third fraction predominantly comprises hydrocarbons having 10 or more carbon atoms; characterised in that at least a portion of the second fraction is recycled to the reaction zone.

6. 发明申请

US20140303266A1 METHODS OF PREPARATION AND FORMING SUPPORTED ACTIVE METAL CATALYSTS AND PRECURSORS 有权
标题翻译：制备和形成支持的活性金属催化剂和前体的方法
公开(公告)号：US20140303266A1
公开(公告)日：2014-10-09
申请号：US14351920
申请日：2012-10-22
申请人： IGTL TECHNOLOGY LTD
发明人： Richard Hyman
IPC分类号： B01J29/80 , B01J29/14
CPC分类号： B01J29/80 , B01J29/146 , B01J29/40 , B01J35/0006 , B01J37/0207 , B01J37/035 , B01J37/18 , B01J2229/186 , B01J2229/38 , B01J2229/42 , B01J2523/00 , C10G2/334 , B01J2523/13 , B01J2523/17 , B01J2523/31 , B01J2523/3712 , B01J2523/41 , B01J2523/842
摘要： The invention relates to a method of preparing a supported catalyst, which method comprises the steps of; (i) providing a porous catalyst support comprising a framework having an internal pore structure comprising one or more pores which internal pore structure comprises a precipitant; (ii) contacting the catalyst support with a solution or colloidal suspension comprising a catalytically active metal such that, on contact with the precipitant, particles comprising the catalytically active metal are precipitated within the internal pore structure of the framework of the catalyst support. The invention also relates to supported catalysts made according to the above method, and to use of the catalysts in catalysing chemical reactions, for example in the Fischer Tropsch synthesis of hydrocarbons.
摘要翻译：本发明涉及一种制备负载型催化剂的方法，该方法包括以下步骤：（i）提供多孔催化剂载体，其包含具有包含一个或多个孔的内孔结构的框架，该内孔结构包含沉淀剂; （ii）使催化剂载体与包含催化活性金属的溶液或胶体悬浮液接触，使得在与沉淀剂接触时，包含催化活性金属的颗粒在催化剂载体的框架的内孔结构内沉淀。本发明还涉及根据上述方法制备的负载型催化剂，以及催化剂催化化学反应的用途，例如在费托合成烃中。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式