公开(公告)号：EP3045514A1

公开(公告)日：2016-07-20

申请号：EP16150478.2

申请日：2016-01-07

申请人： Wong, Alfred Y.

发明人： Wong, Alfred Y.

IPC分类号： C10G50/00 ,  B01J12/00 ,  B01J19/08 ,  B01J19/12 ,  H01J49/32 ,  B01D53/24 ,  B01D53/32 ,  C07C2/80

CPC分类号： C10G50/00 ,  B01J19/087 ,  B01J19/088 ,  B01J19/121 ,  B01J19/125 ,  B01J19/126 ,  B01J19/129 ,  B01J2219/0009 ,  B01J2219/0803 ,  B01J2219/0809 ,  B01J2219/083 ,  B01J2219/085 ,  B01J2219/0854 ,  B01J2219/0864 ,  B01J2219/0869 ,  B01J2219/0871 ,  B01J2219/0875 ,  C10G2300/1025 ,  C10G2300/40 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/06

摘要： A system and method are provided for the separation of hydrogen from natural gas feedstock to form hydrocarbon radicals. Aspects of the system include perpendicular magnetic and electric fields, a method of radical formation that separates hydrogen from the reaction process, and a separation method based on centrifugal forces and phase transitions. The gases rotate in the chamber due to the Lorentz force without any mechanical motion. Rotation separates gases and liquids by centrifugal force. The lighter species are collected from the mid region endpoint of the apparatus and fed back for further reaction. A new concept of controlled turbulence is introduced to mix various species. A novel magnetic field device is introduced comprised of two specially magnetized cylinders. A novel control of temperatures, pressures, electron densities and profiles by, RF, microwaves, UV and rotation frequency are possible especially when atomic, molecular, cyclotron resonances are taken into account. The electrodes can be coated with catalysts; the entire apparatus can be used as a new type of chemical reactor.

摘要翻译： 提供了用于氢从天然气原料分离以形成烃基的系统和方法。 该系统的各方面包括垂直磁场和电场，自由基形成的方法的确从反应过程中分离氢气，并且基于离心力和相变的分离方法。 该气体在所述腔室旋转，由于没有任何机械运动的洛伦兹力。 旋转分离气体和液体由离心力。 较轻的物质被从该装置的中间区域的端点并反馈用于进一步反应。 控制动荡的新概念引入到混合不同种类。 一种新颖的磁场装置被导入由两个专门磁化气缸。 温度，压力，电子密度和型材的新颖的控制通过，RF，微波，紫外线和旋转频率是特别当原子，分子，回旋加速器共振考虑可能的爱情。 电极可以涂覆有催化剂; 整个装置可作为一种新型化学反应器的。

公开(公告)号：EP1989160B1

公开(公告)日：2014-04-09

申请号：EP07704544.1

申请日：2007-02-13

申请人： BASF SE

发明人： BACHTLER, Michael ,  EHRHARDT, Kai Rainer ,  WITTE, Christopher P ,  HAYES, Michael L.

IPC分类号： C07C2/78 ,  C07C2/80 ,  C07C11/24

CPC分类号： C07C2/78 ,  C07C2/80 ,  Y10S585/921 ,  Y10S585/922 ,  C07C11/24

公开(公告)号：EP3045514B1

公开(公告)日：2024-03-06

申请号：EP16150478.2

申请日：2016-01-07

发明人： Wong, Alfred Y.

IPC分类号： C10G50/00 ,  C07C2/80 ,  B01D53/32 ,  B01D53/24 ,  H01J49/32 ,  B01J19/12 ,  B01J19/08 ,  B01J12/00 ,  C10G2/00

公开(公告)号：EP3845513A1

公开(公告)日：2021-07-07

申请号：EP20201205.0

申请日：2020-10-12

申请人： Shell Internationale Research Maatschappij B.V.

发明人： VAN BAVEL, Alexander Petrus ,  DE, Shauvik

IPC分类号： C07C2/80 ,  C07C11/24 ,  B01J12/00 ,  B01J19/08

摘要： The present invention provides a method of preparing acetylene (C 2 H 2 ), the method at least comprising the steps of:
a) providing a hydrocarbon-containing stream; and
b) subjecting the hydrocarbon-containing stream provided in step a) to pyrolysis at a temperature below 2500°C, thereby obtaining at least acetylene (C 2 H 2 ) and hydrogen (H 2 );
wherein, in step b), the hydrocarbon-containing stream is heated by passing it through a structured packing, which structured packing is resistively heated by means of direct electric heating.

公开(公告)号：EP2876097B1

公开(公告)日：2018-02-28

申请号：EP13193626.2

申请日：2013-11-20

申请人： Haldor Topsøe A/S

发明人： Modarresi, Hassan

IPC分类号： C07C2/80 ,  C01B3/38 ,  C07C2/76 ,  H01M8/0606 ,  H01M8/0612 ,  H01M8/0637 ,  H01M8/0662 ,  H01M8/04089 ,  H01M8/124 ,  H01M8/12

CPC分类号： C07C2/80 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/0405 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0495 ,  C01B2203/066 ,  C01B2203/1241 ,  C01B2203/127 ,  C01B2203/146 ,  C01B2203/148 ,  H01M8/04097 ,  H01M8/0606 ,  H01M8/0612 ,  H01M8/0637 ,  H01M8/0662 ,  H01M8/0675 ,  H01M8/12 ,  H01M2008/1293 ,  Y02E60/566 ,  Y02E70/20

摘要： A process for direct conversion of a hydrocarbon-containing gas, such as natural gas, biogas, synthetic natural gas or shale gas, to a higher hydrocarbons product is carried out in the anode compartment of a fuel cell reactor, in which produced hydrogen, limiting the conversion to the equilibrium, is either removed or reacted in situ with oxygen ions transferred from the cathode compartment to produce steam, thereby removing the equilibrium-limiting hydrogen from the reaction. The fuel cell reactor is preferably a solid oxide fuel cell (SOFC) reactor.

公开(公告)号：EP3044194A1

公开(公告)日：2016-07-20

申请号：EP14761340.0

申请日：2014-09-05

申请人： Evonik Degussa GmbH

发明人： MARKOWZ, Georg ,  WENZEL, Thomas ,  HEINECKE, Steffen ,  LUNT-RIEG, Ingrid ,  LIAUW, Surya

IPC分类号： C07C2/80 ,  C07C11/24

CPC分类号： C07C2/80 ,  B01J7/00 ,  B01J19/0046 ,  B01J2219/00006 ,  B01J2219/00452 ,  B01J2219/00585 ,  B01J2219/00716 ,  B01J2219/0072 ,  C07C2/78 ,  C07C2/82 ,  C07C11/24

摘要： The invention relates to a system, comprising a first device for producing ethyne by partially oxidizing at least one hydrocarbon, which first device produces a first product gas flow containing ethyne, a second device for electrothermally producing ethyne, which second device produces a second product gas flow containing ethyne, and a separating device for separating ethyne from a gas flow, to which separating device both the first product gas flow and the second product gas flow are fed. Said system can efficiently use excess electrical energy, in that the device for electrothermally producing ethyne is operated by means of excess electrical energy.

公开(公告)号：EP2876097A1

公开(公告)日：2015-05-27

申请号：EP13193626.2

申请日：2013-11-20

申请人： Haldor Topsøe A/S

发明人： Modarresi, Hassan

IPC分类号： C07C2/80 ,  C01B3/38 ,  C07C2/76

CPC分类号： C07C2/80 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/0405 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0495 ,  C01B2203/066 ,  C01B2203/1241 ,  C01B2203/127 ,  C01B2203/146 ,  C01B2203/148 ,  H01M8/04097 ,  H01M8/0606 ,  H01M8/0612 ,  H01M8/0637 ,  H01M8/0662 ,  H01M8/0675 ,  H01M8/12 ,  H01M2008/1293 ,  Y02E60/566 ,  Y02E70/20

摘要： A process for direct conversion of a hydrocarbon-containing gas, such as natural gas, biogas, synthetic natural gas or shale gas, to a higher hydrocarbons product is carried out in the anode compartment of a fuel cell reactor, in which produced hydrogen, limiting the conversion to the equilibrium, is either removed or reacted in situ with oxygen ions transferred from the cathode compartment to produce steam, thereby removing the equilibrium-limiting hydrogen from the reaction.
The fuel cell reactor is preferably a solid oxide fuel cell (SOFC) reactor.

摘要翻译： 一种用于含烃气体,:的直接转换，如天然气，沼气，合成天然气或页岩气，向更高的烃类产物的方法是在燃料电池中的反应器的阳极室中进行，在其中产生的氢，从而限制 转换到平衡，除去任一个或就地与从转移以产生蒸汽，从而去除从反应平衡限制的氢的阴极隔室的氧离子反应。 所述的燃料电池反应器优选为固体氧化物燃料电池（SOFC）反应器中。

公开(公告)号：EP1975144A1

公开(公告)日：2008-10-01

申请号：EP06805209.1

申请日：2006-11-10

申请人： Yang, Hongsheng ,  Sun, Dekun

发明人： Yang, Hongsheng ,  Sun, Dekun

IPC分类号： C07C2/76 ,  C07C2/80 ,  B01J19/12 ,  C07C11/04 ,  H05B7/00 ,  H05B6/78 ,  H05B6/80

CPC分类号： H05B6/806 ,  B01J19/008 ,  B01J19/126 ,  B01J2219/0869 ,  B01J2219/0875 ,  C07C2/76 ,  C07C2/80 ,  C07C11/04

摘要： The recess waveguide microwave chemical plant for production of ethene from natural gas and the process for production of ethene using said plant are disclosed. Said plant consists of recess waveguide (1), mode transducer and coupling orifice plate (2) on the left side of recess waveguide (1), short-circuiting plunger (3) on the right side of recess waveguide (1), and chemical reactor (4) across the recess waveguide (1).

摘要翻译： 用于由天然气乙烯和用于生产乙烯的方法的凹部波导微波化工厂使用所述计划是游离缺失盘。 所述上凹部波导（1），和化学的右侧besteht凹槽波导（1），时装换能器和耦合孔板（2）凹部波导（1）的左侧的图，短路柱塞（3） 反应器（4）横跨凹槽波导（1）。

公开(公告)号：EP1678274A4

公开(公告)日：2008-07-23

申请号：EP04752327

申请日：2004-05-14

申请人： SYNFUELS INT INC

发明人： PETERSON EDWARD R ,  GATTIS SEAN C

IPC分类号： C07C1/00 ,  C05C11/00 ,  C07C2/00 ,  C07C2/78 ,  C07C2/80 ,  C07C2/82 ,  C07C4/00 ,  C07C4/06 ,  C07C5/00 ,  C07C11/04 ,  C10G20060101

CPC分类号： C07C2/82 ,  C07C2/78 ,  C07C2/80 ,  C07C11/04 ,  Y10S585/943 ,  C07C11/24

摘要： 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.