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    Desulfurizer
    2.
    发明授权
    Desulfurizer 有权
    脱硫剂

    公开(公告)号：US08500875B2

    公开(公告)日：2013-08-06

    申请号：US13062893

    申请日：2009-08-12

    Applicant: Jun Yamamoto

    Inventor： Jun Yamamoto

    IPC: B01D53/02

    CPC classification number: C10L3/10 ,  B01D53/0423 ,  B01D53/0446 ,  B01D2257/30 ,  B01D2259/401 ,  B01D2259/41 ,  B01J8/008 ,  B01J8/0484 ,  B01J2208/0084 ,  B01J2208/00884 ,  B01J2208/00938 ,  C01B3/36 ,  C01B2203/0233 ,  C01B2203/066 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/1258 ,  C10L3/102 ,  H01M8/0675 ,  H01M2008/1293

    Abstract: A desulfurizer includes a filled chamber having a raw fuel passage through which a raw fuel flows, the filled chamber being filled with a desulfurizing agent, a supply chamber disposed upstream of the filled chamber, for uniformly supplying the raw fuel to the raw fuel passage, and a discharge chamber disposed downstream of the filled chamber, for uniformly discharging the raw fuel from the raw fuel passage. The raw fuel passage has first and second reversers for reversing the direction in which the raw fuel flows. The raw fuel passage has a cross-sectional area which is smaller in a downstream portion thereof than in an upstream portion thereof.

    Abstract translation: 脱硫器包括：填充室，其具有原燃料流过的原燃料通道，填充室中填充有脱硫剂，设置在填充室的上游的供给室，用于将原料燃料均匀地供给原料燃料通道; 以及设置在填充室的下游的排出室，用于从原燃料通道均匀排出原料燃料。 原燃料通道具有用于反转原燃料流动方向的第一和第二反向器。 原燃料通道的下游部分的横截面积比其上游部分的截面面积小。

    DESULFURIZER
    3.
    发明申请
    DESULFURIZER 有权
    脱硫剂

    公开(公告)号：US20110165477A1

    公开(公告)日：2011-07-07

    申请号：US13062893

    申请日：2009-08-12

    Applicant: Jun Yamamoto

    Inventor： Jun Yamamoto

    IPC: B01J19/00 ,  H01M8/06

    CPC classification number: C10L3/10 ,  B01D53/0423 ,  B01D53/0446 ,  B01D2257/30 ,  B01D2259/401 ,  B01D2259/41 ,  B01J8/008 ,  B01J8/0484 ,  B01J2208/0084 ,  B01J2208/00884 ,  B01J2208/00938 ,  C01B3/36 ,  C01B2203/0233 ,  C01B2203/066 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/1258 ,  C10L3/102 ,  H01M8/0675 ,  H01M2008/1293

    Abstract: A desulfurizer includes a filled chamber having a raw fuel passage through which a raw fuel flows, the filled chamber being filled with a desulfurizing agent, a supply chamber disposed upstream of the filled chamber, for uniformly supplying the raw fuel to the raw fuel passage, and a discharge chamber disposed downstream of the filled chamber, for uniformly discharging the raw fuel from the raw fuel passage. The raw fuel passage has first and second reversers for reversing the direction in which the raw fuel flows. The raw fuel passage has a cross-sectional area which is smaller in a downstream portion thereof than in an upstream portion thereof.

    Abstract translation: 脱硫器包括：填充室，其具有原燃料流过的原燃料通道，填充室中填充有脱硫剂，设置在填充室的上游的供给室，用于将原料燃料均匀地供给原料燃料通道; 以及设置在填充室的下游的排出室，用于从原燃料通道均匀排出原料燃料。 原燃料通道具有用于反转原燃料流动方向的第一和第二反向器。 原燃料通道的下游部分的横截面积比其上游部分的截面面积小。

    Catalytic reactor system
    7.
    发明申请
    Catalytic reactor system 审中-公开
    催化反应器系统

    公开(公告)号：US20040247498A1

    公开(公告)日：2004-12-09

    申请号：US10454159

    申请日：2003-06-04

    Inventor： Jonathan Phillips ,  John C. Weigle

    IPC: B01J008/02 ,  B01J010/00

    CPC classification number: B01J8/0484 ,  B01J8/0453 ,  B01J8/0492 ,  B01J23/44 ,  B01J23/83 ,  B01J35/0006 ,  B01J2208/00539 ,  B01J2208/00548 ,  C10G49/00 ,  C10G49/04

    Abstract: A catalytic reactor system especially useful for hydrogenation, dehydrogenation, hydrocarbon isomerization, and hydrocracking was demonstrated for isomerizing 1-butene to 2-butene. The reactor system includes a noble metal-containing catalyst bed and a base-metal catalyst bed in physical contact with but substantially unmixed with the noble metal catalyst bed. The reactor includes a gas inlet for sending hydrogen to the noble metal catalyst and an inlet for sending 1-butene to the second catalyst bed. An outlet is provided for product and unreacted hydrogen and 1-butene. The reactor system is configured such that hydrogen flows through the noble metal catalyst bed first and then through the base-metal catalyst bed, while 1-butene flows through the base metal catalyst bed, with minimal backflow through noble metal bed.

    Abstract translation: 证明了将1-丁烯异构化为2-丁烯的催化反应器系统，其特别可用于氢化，脱氢，烃异构化和加氢裂化。 反应器系统包括含贵金属的催化剂床和与贵金属催化剂床物理接触但基本上不混合的贱金属催化剂床。 反应器包括用于将氢气输送到贵金属催化剂的气体入口和用于将1-丁烯送入第二催化剂床的入口。 为产物和未反应的氢气和1-丁烯提供出口。 反应器系统构造成使得氢气首先流过贵金属催化剂床，然后通过贱金属催化剂床，同时1-丁烯流过母体金属催化剂床，同时以极少的回流通过贵金属床。

    Reactive distillation
    8.
    发明申请
    Reactive distillation 审中-公开
    反应蒸馏

    公开(公告)号：US20030124038A1

    公开(公告)日：2003-07-03

    申请号：US10348801

    申请日：2003-01-21

    Applicant: Sulzer Chemtech AG

    Inventor： Peter Moritz ,  Willem Wiekert Levering ,  Raymond Charles Pluss

    IPC: B01J008/02 ,  B01J008/04

    CPC classification number: B01D3/009 ,  B01J8/048 ,  B01J8/0484 ,  B01J8/06 ,  B01J19/32 ,  B01J2219/3221 ,  B01J2219/3222 ,  B01J2219/32227 ,  B01J2219/32279 ,  B01J2219/32466

    Abstract: The reactive distillation is carried out in a column (1) with a packing (2) which is at least partly designed as a catalyst carrier (23). Fluids (3, 4) which form two phases of different densities flow through the packing. An internal volume flow (300) is set for the denser fluid (3), the value of which lies in an interval (I) about a distinguished value (a), with this value being associated with a dwell time distribution (32) of the denser fluid: For the distinguished value the variance (s) of the dwell time distributionnullas a function of the internal volume flownulltakes on a minimum; and at the boundaries of the named interval the internal volume flow does not differ from the distinguished value by more than 30%, preferably by more than 10%.

    Abstract translation: 反应蒸馏在具有至少部分设计为催化剂载体（23）的填料（2）的塔（1）中进行。 形成两个不同密度的相的流体（3,4）流过填料。 对于较稠密的流体（3）设置内部体积流（300），其中该值位于围绕识别值（a）的间隔（I）中，该值与停留时间分布（32）相关联 更稠密的流体：对于不同的值，驻留时间分布的方差（作为内部体积流量的函数）占最小值; 并且在所述间隔的边界处，内部体积流量与识别值没有差异超过30％，优选大于10％。

    Process and device for manufacturing synthesis gas and application
    10.
    发明授权
    Process and device for manufacturing synthesis gas and application 失效
    制造合成气和应用的工艺和装置

    公开(公告)号：US5755841A

    公开(公告)日：1998-05-26

    申请号：US631909

    申请日：1996-04-12

    Applicant: Pierre Boucot ,  Paul Gateau ,  Jerome Weill

    Inventor： Pierre Boucot ,  Paul Gateau ,  Jerome Weill

    IPC: B01J8/04 ,  C01B3/02 ,  C01B3/36 ,  C01B3/38 ,  C07C1/04 ,  C07C29/151 ,  C07C31/04 ,  C01B3/24

    CPC classification number: B01J8/0484 ,  B01J8/0453 ,  B01J8/0492 ,  C01B3/025 ,  C01B3/36 ,  C01B3/382 ,  C07C1/041 ,  C07C29/1516 ,  B01J2208/025 ,  C01B2203/142 ,  C01B2203/82

    Abstract: The present invention relates to a process and to a device for manufacturing synthetic gas. The reactor in accordance with the invention comprises within a single housing: a non catalytic combustion chamber (1) comprising at least one fuel injection element (2) and at least one oxidizer injection element (3) so as to achieve a partial combustion in said chamber referred to as "sufficient residence time chamber", and at least one catalytic bed (4) into which the gases coming from combustion chamber (1) run, and further comprising at least one additional oxidizer injection element (6) and at least one fuel injection element (7). The reactor and the process in accordance with the invention may be applied to any chemical manufacturing utilizing synthetic gas.

    Abstract translation: 本发明涉及一种制造合成气体的方法和装置。 根据本发明的反应器包括在单个壳体内：非催化燃烧室（1），其包括至少一个燃料喷射元件（2）和至少一个氧化剂注入元件（3），以便在所述 称为“足够的停留时间室”的室，以及至少一个催化床（4），来自燃烧室（1）的气体流入其中，并且还包括至少一个附加的氧化剂注入元件（6）和至少一个 燃料喷射元件（7）。 根据本发明的反应器和方法可以应用于利用合成气体的任何化学制造。

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