Production of hydrogen and carbon monoxide containing synthesis gas by partial oxidation
    171.
    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

    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
    172.
    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

    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
    173.
    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

    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 for the production of alumina
    175.
    发明申请
    Process for the production of alumina 有权
    氧化铝生产工艺

    公开(公告)号:US20010046469A1

    公开(公告)日:2001-11-29

    申请号:US09773561

    申请日:2001-02-02

    Inventor: Keld Johansen

    CPC classification number: C01F7/24 C01F7/308

    Abstract: A process for the production of alumina comprising: (a) dissolution of Gibbsite (A12O3, 3H2O) in nitric acid providing an acid solution of aluminum nitrate products; (b) decomposition at 300-700null C. with free air supply of the acid solution to alumina and Nox; (c) regeneration of the formed NOX to concentrated nitric acid and recycling of produced nitric acid to step (a); and (d) recovery of the alumina product formed in step (b) by means selected from spraying onto the inner surface of one or more rotary kilns, drying in a fluid bed, and drying in a steel band conveyor furnace.

    Abstract translation: 一种生产氧化铝的方法,包括:(a)三水铝矿(A12O3,3H2O)在硝酸中溶解,得到硝酸铝产品的酸溶液; (b)在300-700℃下分解,将酸溶液自由供给氧化铝和Nox; (c)将形成的NO x再生成浓硝酸并将产生的硝酸再循环至步骤(a); 和(d)通过选择喷雾到一个或多个旋转窑的内表面,在流化床中干燥并在钢带式输送机炉中干燥的方法回收步骤(b)中形成的氧化铝产物。

    Process and reactor for the preparation of ammonia
    176.
    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

    Inventor: Erik A. Gam

    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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