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1. 发明申请

US20100222440A1 Process for the Treatment of a Product Stream 有权
标题翻译：产品流处理流程
公开(公告)号：US20100222440A1
公开(公告)日：2010-09-02
申请号：US12225317
申请日：2007-03-26
申请人： Vaughan Clifford Williams
发明人： Vaughan Clifford Williams
IPC分类号： C07C27/06 , B01D53/14
CPC分类号： B01D53/1456 , B01D53/1493 , C10G11/22 , C10G27/04 , C10G70/04 , C10G2400/20 , Y02C10/06 , Y02C10/08 , Y02P20/128 , Y02P30/40 , Y02P30/446 , Y02P30/464
摘要： The present invention relates to a process for the treatment of a product stream, more specifically of a product stream from an autothermal cracking process, said product stream comprising one or more olefins, hydrogen, carbon monoxide, carbon dioxide and one or more oxygenates, said process comprising contacting the product stream with at least one compound selected from those represented by formulas: (1) H2N—OR1, and (2) H2N—NR2R3, where: R1, R2 and R3 may each be independently selected from H and carbon containing substituents.
摘要翻译：本发明涉及一种用于处理产物流的方法，更具体地说是来自自热裂解方法的产物流，所述产物流包含一种或多种烯烃，氢气，一氧化碳，二氧化碳和一种或多种含氧化合物，所述方法包括使产物流与至少一种选自由式（1）H 2 N -OR 1和（2）H 2 N-NR 2 R 3表示的化合物接触的化合物接触，其中：R 1，R 2和R 3可各自独立地选自H和含有取代基。

2. 发明授权

US08002856B2 Process for contracting a hydrocarbon and an oxygen-containing gas with a catalyst bed 有权
标题翻译：用催化剂床收缩烃和含氧气体的方法
公开(公告)号：US08002856B2
公开(公告)日：2011-08-23
申请号：US12087922
申请日：2006-12-20
申请人： Vaughan Clifford Williams
发明人： Vaughan Clifford Williams
IPC分类号： C01B3/38 , C07C4/02 , C07C4/06
CPC分类号： B01J19/2485 , B01J8/0085 , B01J8/009 , B01J19/24 , B01J19/30 , B01J23/825 , B01J23/835 , B01J23/8926 , B01J35/04 , B01J2208/00362 , B01J2208/00557 , B01J2208/00814 , B01J2208/00849 , B01J2208/00884 , B01J2208/021 , B01J2208/025 , B01J2219/00123 , B01J2219/00166 , B01J2219/192 , B01J2219/1928 , B01J2219/3023 , B01J2219/30234 , B01J2219/30246 , B01J2219/30249 , B01J2219/30416 , B01J2219/30475 , B01J2219/3085
摘要： The present invention relates to a process for contacting a hydrocarbon and an oxygen-containing gas with a catalyst bed in a reactor at a space velocity of at least 10,000 h−1, said process being characterised in that a) the reactor has a polygonal internal cross-section at least in the section where the catalyst bed is held, b) the catalyst bed is made up of 2 or more layers of catalyst in the form of tiles of polygonal shape, said tiles have at least 4 sides, c) each layer of catalyst comprises at least 4 tiles which tessellate together to form said layer, and d) the edges where 2 tiles meet in one layer do not align with the edges where 2 tiles meet in an adjacent layer.
摘要翻译：本发明涉及使烃和含氧气体与催化剂床在反应器中以至少10,000h -1的空间速度接触的方法，所述方法的特征在于：a）反应器具有多边形内部至少在催化剂床保持部分的截面，b）催化剂床由多层形状的瓷砖形式的2层或更多层催化剂组成，所述砖具有至少4个侧面，c）每个催化剂层包括至少4块镶嵌在一起以形成所述层的瓦片，以及d）2瓦片在一层中相遇的边缘不与2瓦片在相邻层中相遇的边缘对准。

3. 发明授权

US07807860B2 Autothermal cracking process and reactor 有权
标题翻译：自热裂解过程和反应器
公开(公告)号：US07807860B2
公开(公告)日：2010-10-05
申请号：US10543696
申请日：2004-02-06
申请人： Derek Alan Colman , Michael John Alexander Matthewman , Ian Allan Beattie Reid , Vaughan Clifford Williams , William Terence Woodfin
发明人： Derek Alan Colman , Michael John Alexander Matthewman , Ian Allan Beattie Reid , Vaughan Clifford Williams , William Terence Woodfin
IPC分类号： C07C5/333
CPC分类号： B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J2208/00522 , B01J2219/00094 , B01J2219/00265 , C07C5/48
摘要： The present invention provides a reactor design that enables an auto-thermal cracking process to be conducted at any suitable pressure wherein the gaseous reactants are preheated separately before mixing and then presented to the reaction zone in a uniformly distributed manner. In particular, the present invention-relates to apparatus for reacting a first and second gaseous reactant to form a gaseous product wherein the apparatus comprises at least one first supply means for the first gaseous reactant, at least one second supply means for the second gaseous reactant, a resistance zone and a reaction zone, preferably comprising a catalyst, wherein the first supply means comprises a plurality of first outlets for delivery of the first gaseous reactant, and the second supply means comprises a plurality of second outlets for delivery of the second gaseous reactant, the resistance zone is porous, the reaction zone is positioned downstream of the resistance zone with respect to the flow of the first and second gaseous reactants and wherein the first supply means and the second supply means are arranged such that the first gas and the second gas are contacted in an essentially parallel manner and mixed prior to contacting the resistance zone. The present invention also provides a process for the production of a mono-olefin utilizing said apparatus.
摘要翻译：本发明提供一种反应器设计，使得能够在任何合适的压力下进行自热裂解过程，其中气态反应物在混合之前分别预热，然后以均匀分布的方式呈现给反应区。特别地，本发明涉及用于使第一和第二气体反应物反应以形成气态产物的装置，其中所述装置包括用于第一气态反应物的至少一个第一供应装置，用于第二气态反应物的至少一个第二供应装置，电阻区和反应区，优选包括催化剂，其中第一供应装置包括多个用于输送第一气态反应物的第一出口，第二供应装置包括多个第二出口，用于输送第二气态反应物，电阻区是多孔的，反应区相对于第一和第二气态反应物的流动位于阻力区的下游，并且其中第一供应装置和第二供应装置被布置成使得第一气体和第二气体以基本上平行的方式接触并在接触阻力区之前混合。本发明还提供了利用所述装置生产单烯烃的方法。

4. 发明申请

US20090094891A1 Process For Contacting a Hydrocarbon and an Oxygen-Containing Gas With a Catalyst Bed 有权
标题翻译：用催化剂床接触烃和含氧气体的方法
公开(公告)号：US20090094891A1
公开(公告)日：2009-04-16
申请号：US12087922
申请日：2006-12-20
申请人： Vaughan Clifford Williams
发明人： Vaughan Clifford Williams
IPC分类号： C01B3/24
CPC分类号： B01J19/2485 , B01J8/0085 , B01J8/009 , B01J19/24 , B01J19/30 , B01J23/825 , B01J23/835 , B01J23/8926 , B01J35/04 , B01J2208/00362 , B01J2208/00557 , B01J2208/00814 , B01J2208/00849 , B01J2208/00884 , B01J2208/021 , B01J2208/025 , B01J2219/00123 , B01J2219/00166 , B01J2219/192 , B01J2219/1928 , B01J2219/3023 , B01J2219/30234 , B01J2219/30246 , B01J2219/30249 , B01J2219/30416 , B01J2219/30475 , B01J2219/3085
摘要： The present invention relates to a process for contacting a hydrocarbon and an oxygen-containing gas with a catalyst bed in a reactor at a space velocity of at least 10,000 h−1, said process being characterised in that a) the reactor has a polygonal internal cross-section at least in the section where the catalyst bed is held, b) the catalyst bed is made up of 2 or more layers of catalyst in the form of tiles of polygonal shape, said tiles have at least 4 sides, c) each layer of catalyst comprises at least 4 tiles which tessellate together to form said layer, and d) the edges where 2 tiles meet in one layer do not align with the edges where 2 tiles meet in an adjacent layer.
摘要翻译：本发明涉及使烃和含氧气体与催化剂床在反应器中以至少10,000h -1的空间速度接触的方法，所述方法的特征在于：a）反应器具有多边形内部至少在催化剂床保持部分的截面，b）催化剂床由多层形状的瓷砖形式的2层或更多层催化剂组成，所述砖具有至少4个侧面，c）每个催化剂层包括至少4块镶嵌在一起以形成所述层的瓦片，以及d）2瓦片在一层中相遇的边缘不与2瓦片在相邻层中相遇的边缘对准。

5. 发明授权

US07923595B2 Process for the treatment of a product stream 有权
标题翻译：用于处理产品流的方法
公开(公告)号：US07923595B2
公开(公告)日：2011-04-12
申请号：US12225317
申请日：2007-03-26
申请人： Vaughan Clifford Williams
发明人： Vaughan Clifford Williams
IPC分类号： C07C7/00 , C07C4/02 , C07C7/12 , C07C7/17 , C10G51/02 , C10G17/00
CPC分类号： B01D53/1456 , B01D53/1493 , C10G11/22 , C10G27/04 , C10G70/04 , C10G2400/20 , Y02C10/06 , Y02C10/08 , Y02P20/128 , Y02P30/40 , Y02P30/446 , Y02P30/464
摘要： Process for treating a product stream typically from an autothermal cracking process, the product stream comprising one or more olefins, hydrogen, carbon monoxide, carbon dioxide and one or more oxygenates, by contacting the product stream with at least one compound selected from (1) H2N—OR1, and (2) H2N—NR2R3, where R1, R2 and R3 may each be independently selected from H and carbon-containing substituents.
摘要翻译：通过将产物流与至少一种选自（1）的化合物的化合物接触，将产物流通常从自热裂解方法处理，所述产物流包含一种或多种烯烃，氢，一氧化碳，二氧化碳和一种或多种含氧化合物， H 2 N-OR 1和（2）H 2 N-NR 2 R 3，其中R 1，R 2和R 3可各自独立地选自H和含碳取代基。

6. 发明授权

US07683231B2 Catalyst and process for the production of olefins 失效
标题翻译：用于生产烯烃的催化剂和方法
公开(公告)号：US07683231B2
公开(公告)日：2010-03-23
申请号：US10558827
申请日：2004-05-18
申请人： Ian Allan Beattie Reid , Vaughan Clifford Williams
发明人： Ian Allan Beattie Reid , Vaughan Clifford Williams
IPC分类号： C07C4/06 , B01J23/00
CPC分类号： B01J35/04 , B01J23/56 , B01J23/92 , C07C5/48 , C10G2400/20 , Y02P20/584 , C07C11/02
摘要： A catalyst system capable of supporting combustion beyond the fuel rich limit of flammability comprising a catalytic component, a first support and a second support and wherein the catalytic component is present on both the first and the second support, and a process for the production of an olefin, said process comprising passing a mixture of a hydrocarbon and an oxygen-containing gas over said catalyst system to produce said olefin. The first support and the second support must differ in at least one of the following aspects: support material, support type and/or structural dimension.
摘要翻译：一种催化剂体系，其能够支持超过燃料富含燃烧极限的燃烧，其包括催化组分，第一载体和第二载体，并且其中所述催化组分存在于所述第一和第二载体上，以及用于生产所述方法包括使烃和含氧气体的混合物在所述催化剂体系上通过以产生所述烯烃。以下至少一个方面，第一个支撑和第二个支撑必须不同：支撑材料，支撑类型和/或结构尺寸。

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