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    PROCESS FOR PRODUCING HIGH PURITY CO BY MEMBRANE PURIFICATION OF SOEC-PRODUCED CO
    61.
    发明申请
    PROCESS FOR PRODUCING HIGH PURITY CO BY MEMBRANE PURIFICATION OF SOEC-PRODUCED CO 审中-公开
    通过生产SOEC生产的CO的膜净化生产高纯度CO的方法

    公开(公告)号：US20160151739A1

    公开(公告)日：2016-06-02

    申请号：US14903186

    申请日：2014-06-13

    Applicant: Haldor Topsoe A/S

    Inventor： Niklas Bengt Jakobsson ,  Claus Friis Pedersen

    IPC: B01D53/22 ,  C25B15/08 ,  C25B1/00

    CPC classification number: B01D53/228 ,  B01D53/22 ,  B01D63/06 ,  B01D63/08 ,  B01D2256/20 ,  B01D2257/504 ,  B01D2258/0208 ,  B01D2311/25 ,  C25B1/00 ,  C25B15/08 ,  Y02C10/10 ,  Y02P20/152

    Abstract: A process for producing high purity carbon monoxide (CO) by membrane purification of CO produced in a solid oxide electrolysis cell (SOEC) comprises the steps of generating a gaseous mixture of CO and CO2 by SOEC electrolysis of CO2, applying a moderate pressure on the retentate side of the membrane in one or more membrane units connected to the exit of the SOEC via a compressor or an ejector, applying a lower pressure than the moderate pressure on the permeate side of the membrane, splitting the retentate stream, which is now enriched in CO, into two separate parts, expanding the first part of the retentate stream to reach the permeate low pressure conditions, leading the above-mentioned part of the retentate to the permeate side of the membrane to lower the partial pressure of CO2 on this side, and recycling the outlet permeate stream back to the SOEC as a feed gas together with fresh CO2. Preferably the membrane unit is designed with a tubular membrane or multiple planar membranes connected in series, and the retentate and permeate streams are operated in counter-current mode.

    Abstract translation: 通过在固体氧化物电解池（SOEC）中生产的CO的膜纯化来生产高纯度一氧化碳（CO）的方法包括以下步骤：通过SOEC电解CO 2产生CO和CO 2的气体混合物，在 通过压缩机或喷射器连接到SOEC出口的一个或多个膜单元中的膜的滞留侧，施加比膜的渗透侧上的中等压力更低的压力，分离现在富集的滞留物流 在CO中分成两部分，使第一部分的渗余物流膨胀以达到渗透物低压条件，将上述部分的渗余物引导到膜的渗透侧，以降低该侧的二氧化碳分压 ，并将出口渗透物流与新鲜的CO 2一起作为进料气体回收到SOEC。 优选地，膜单元设计有串联连接的管状膜或多个平面膜，并且滞留物和渗透物流以逆流模式操作。

    Production of hydrogen and carbon monoxide containing synthesis gas by partial oxidation
    65.
    发明申请
    Production of hydrogen and carbon monoxide containing synthesis gas by partial oxidation 失效
    通过部分氧化生产含氢和一氧化碳的合成气

    公开(公告)号：US20020058005A1

    公开(公告)日：2002-05-16

    申请号：US09955455

    申请日：2001-09-18

    Applicant: Haldor Topsoe A/S

    Inventor： Kim Aasberg-Petersen ,  Thomas Sandahl Christensen

    IPC: C01B003/26

    CPC classification number: C01B3/382 ,  C01B3/386 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/0844 ,  C01B2203/1241 ,  C01B2203/143 ,  C01B2203/82

    Abstract: A process for the preparation of a synthesis gas containing hydrogen and carbon monoxide by a combination of catalytic partial oxidation and further an autothermal reforming process, comprising (a) providing separate streams of predetermined proportions of a hydrocarbon feedstock, an oxygen source and of process steam, (b) injecting said separate streams into a catalytic partial oxidation reaction zone to react, and to form a prereformed product stream, (c) introducing the prereformed product and a predetermined proportion of a second oxygen source into a further partial oxidation process step forming a further partially oxidised process stream by flame reactions, (d) reacting the further partially oxidised process stream in the reaction zone constituting a steam reforming process step to form a synthesis gas product stream, and (e) withdrawing the synthesis gas product stream from the further partial oxidation process step and the steam reforming process step, the two steps constituting the autothermal reforming process.

    Abstract translation: 一种通过催化部分氧化和进一步的自热重整方法的组合制备含有氢和一氧化碳的合成气的方法，包括（a）提供预定比例的烃原料，氧源和工艺蒸汽的单独流 ，（b）将所述分离的物流注入催化部分氧化反应区以进行反应，并形成预重整的产物流，（c）将预转化产物和预定比例的第二氧源引入另外的部分氧化工艺步骤中形成 通过火焰反应进一步部分氧化的工艺流，（d）使构成蒸汽重整工艺步骤的反应区中的进一步部分氧化的工艺流反应以形成合成气产物流，和（e）从合成气产物流中取出合成气产物流 进一步部分氧化工艺步骤和蒸汽重整工艺步骤，两步组成 进行自热重整过程。

    Method for the removal of particulate matter from aqueous suspension
    66.
    发明申请
    Method for the removal of particulate matter from aqueous suspension 失效
    从水性悬浮液中除去颗粒物的方法

    公开(公告)号：US20020053543A1

    公开(公告)日：2002-05-09

    申请号：US09935804

    申请日：2001-08-23

    Applicant: Haldor Topsoe A/S

    Inventor： Niels Christiansen

    IPC: B01D063/00

    CPC classification number: B01D61/147 ,  B01D61/16 ,  B01D71/024 ,  B01D2311/04 ,  B01D2325/26 ,  C12H1/063 ,  B01D2311/18 ,  B01D2311/24

    Abstract: Method for the removal of particulate matter from aqueous suspension comprising steps of establishing value of pH and of Zeta potential of particles in the suspension; providing a porous filter having a membrane layer consisting of at least a metal-oxide with a Zeta potential at the pH value of the suspension having same polarity of the Zeta potential as the particles in the suspension; passing the suspension through the porous filter; and withdrawing a filtrate.

    Abstract translation: 从水性悬浮液中除去颗粒物的方法，包括确定悬浮液中颗粒的pH值和Zeta电位值的步骤; 提供一种多孔过滤器，其具有至少具有ζ电位的金属氧化物的膜层，其具有与悬浮液中的颗粒相同的Zeta电位极性的悬浮液的pH值; 使悬浮液通过多孔过滤器; 并取出滤液。

    High electrical power current limiter being useful in electrical power systems
    67.
    发明申请
    High electrical power current limiter being useful in electrical power systems 审中-公开
    高电流限流器在电力系统中有用

    公开(公告)号：US20020044037A1

    公开(公告)日：2002-04-18

    申请号：US09880316

    申请日：2001-06-13

    Applicant: Haldor Topsoe A/S

    Inventor： Jens Christiansen ,  Jorgen Gutzon Larsen

    IPC: H01H085/04

    CPC classification number: H02H7/001 ,  Y02E40/68

    Abstract: A high electrical power current limiter comprising a high temperature superconducting sacrificial fuse in series with superconductive or normalconductive equipment to be protected, wherein the high temperature superconducting fuse has a critical current density being lower than a fault current.

    Abstract translation: 一种高功率限流器，包括与要被保护的超导或常导电设备串联的高温超导牺牲熔断器，其中高温超导熔丝的临界电流密度低于故障电流。

    Process and reactor for the preparation of ammonia
    69.
    发明申请
    Process and reactor for the preparation of ammonia 有权
    用于制备氨的工艺和反应器

    公开(公告)号：US20010018039A1

    公开(公告)日：2001-08-30

    申请号：US09777097

    申请日：2001-02-05

    Applicant: Haldor Topsoe A/S

    Inventor： Erik A. Gam

    IPC: C01C001/04

    CPC classification number: C01C1/0405 ,  B01J8/0453 ,  B01J8/0465 ,  B01J2208/00212 ,  C01C1/0417 ,  Y02P20/52

    Abstract: Process and reactor for the preparation of ammonia at elevated pressure and temperature in an ammonia reactor, wherein a process stream of ammonia synthesis gas is successively passed through at least three catalyst beds with intermediate cooling of partially reacted synthesis gas leaving the catalyst beds by heat exchange in heat exchangers arranged between each catalyst bed. The process stream is obtained by combining prior to introduction into a first catalyst bed, a first feed stream of synthesis gas having been preheated through indirect heat exchange during the intermediate cooling of the partially converted synthesis gas and a second feed stream of synthesis gas for adjustment of temperature of the process stream. The first feed stream is passed successively through the interbed heat exchangers for cooling the partially converted synthesis gas and space velocity of the synthesis gas is adjusted to be substantially in the same range in all catalyst beds.

    Abstract translation: 用于在氨反应器中在升高的压力和温度下制备氨的工艺和反应器，其中氨合成气的工艺流连续通过至少三个催化剂床，通过热交换离开催化剂床的部分反应合成气的中间冷却 在布置在每个催化剂床之间的热交换器中。 工艺物流通过在引入第一催化剂床之前进行组合而得到，合成气的第一进料流在部分转化的合成气的中间冷却期间通过间接热交换被预热，以及用于调节的第二合成气进料流 的工艺流的温度。 第一进料流依次通过中间热交换器冷却部分转化的合成气，合成气的空间速度在所有催化剂床中调节至基本相同的范围。

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