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    Process for catalytic reaction of gases
    2.
    发明授权
    Process for catalytic reaction of gases 失效
    气体催化反应方法

    公开(公告)号：US5366708A

    公开(公告)日：1994-11-22

    申请号：US997597

    申请日：1992-12-28

    申请人： Yurii S. Matros ,  Robert A. Yeo ,  David E. McCombs

    发明人： Yurii S. Matros ,  Robert A. Yeo ,  David E. McCombs

    IPC分类号： B01D53/86 ,  B01D53/94 ,  B01J8/04 ,  C01B3/38 ,  C01B17/04 ,  C01B17/80 ,  C01C1/04 ,  B01D53/00

    CPC分类号： B01J8/0496 ,  B01D53/864 ,  B01D53/9431 ,  B01J8/048 ,  C01B17/043 ,  C01B17/803 ,  C01B3/38 ,  C01C1/0417 ,  B01J2208/00274 ,  B01J2208/0053 ,  Y02P20/52

    摘要： Apparatus and process for the catalytic gaseous phase reaction of a feed gas mixture. The apparatus includes a reactor having two ends which alternately serve as an inlet for the feed gas mixture and as an outlet for reacted gas and two stationary heat exchange/reaction zones connected by a center zone. Each of the heat exchange/reaction zones contains a layer of catalyst and the center zone contains a feed gas mixture inlet. A first distribution/collection zone is between one of the heat exchange/reaction zones and one of the ends of the reactor and a second distribution/collection zone is between the other heat exchange/reaction zone and the other end of the reactor. In the process, the heat exchange/reaction zones are alternately heated and cooled by periodically reversing the direction of flow of gas through the reactor. As an intermediate step in each complete reversal of the direction of flow of gas through the reactor, the feed gas is introduced into the center zone and reacted in the heat exchange/reaction zone which was being heated immediately prior to the intermediate step, reacted gas is discharged from the end of the reactor which served as the reacted gas outlet immediately prior to the intermediate step, unreacted feed gas trapped in the distribution/collection zone between the heat exchange/reaction zone which was being cooled and the end of the reactor which served as the feed gas inlet immediately prior to the intermediate step is displaced to the center zone, and the displaced unreacted gas is combined with feed gas mixture being introduced into the reactor.

    摘要翻译： 进料气体混合物的催化气相反应的装置和方法。 该装置包括具有两端的反应器，其交替地用作进料气体混合物的入口和作为反应气体的出口和由中心区域连接的两个固定的热交换/反应区域。 每个热交换/反应区包含一层催化剂，中心区含有进料气体混合物入口。 第一分配/收集区位于热交换/反应区之一和反应器的一端之间，第二分配/收集区在另一个热交换/反应区和反应器的另一端之间。 在此过程中，通过周期性地反转气体通过反应器的方向来交替地加热和冷却热交换/反应区域。 作为在通过反应器的气体的每次完全逆转的中间步骤中，将进料气体引入中心区域，并在中间步骤之前立即加热的热交换/反应区域中反应，反应气体 在刚好在中间步骤之前用作反应气体出口的反应器的末端排出未被反应的进料气体，其被捕获在被冷却的热交换/反应区域和反应器末端之间的分配/收集区中 作为在中间步骤之前的进料气体入口被移动到中心区域，并且将置换的未反应气体与被引入反应器中的进料气体混合物组合。

    Vertical sulfur recovery plant
    7.
    发明授权
    Vertical sulfur recovery plant 失效
    立式硫磺恢复厂

    公开(公告)号：US3607132A

    公开(公告)日：1971-09-21

    申请号：US3607132D

    申请日：1969-09-05

    申请人： AMOCO PROD CO

    发明人： SUDDUTH LAMAR F

    IPC分类号： B01D53/52 ,  C01B17/04 ,  B01J9/04

    CPC分类号： B01D53/523 ,  C01B17/0417 ,  C01B17/043

    摘要： Apparatus for recovery of sulfur from hydrogen sulfide is described in which the catalyst chambers, condensing and boiler sections, and liquid-gas separator compartments are serially arranged. A separate condensing section is provided for each of the catalyst chambers while sulfur produced in the boiler is condensed in the second pass tubes comprising the boiler section, and flows into a separator compartment. Liquid sulfur seals connect the separator compartments, and liquid sulfur is discharged from one of them.

    SOUR SYNGAS TREATMENT APPARATUSES AND PROCESSES FOR TREATING SOUR SYNGAS COMPRISING SULFUR COMPONENTS AND CARBON DIOXIDE
    9.
    发明申请
    SOUR SYNGAS TREATMENT APPARATUSES AND PROCESSES FOR TREATING SOUR SYNGAS COMPRISING SULFUR COMPONENTS AND CARBON DIOXIDE 有权
    用于处理包含硫组分和二氧化碳的原始数据的基本原理处理装置和处理方法

    公开(公告)号：US20160296878A1

    公开(公告)日：2016-10-13

    申请号：US14682636

    申请日：2015-04-09

    申请人： UOP LLC

    发明人： Lubo Zhou ,  Bart Beuckels ,  Ernest James Boehm

    IPC分类号： B01D53/14 ,  B01D53/18

    CPC分类号： B01D53/1462 ,  B01D53/1406 ,  B01D2252/2021 ,  B01D2252/2025 ,  B01D2252/20468 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2256/24 ,  B01D2257/302 ,  B01D2257/304 ,  B01D2257/308 ,  B01D2257/504 ,  C01B17/043 ,  C10K1/08 ,  C10K1/34 ,  Y02C10/06 ,  Y02P20/152

    摘要： Sour syngas treatment apparatuses and processes for treating a sour syngas stream are provided herein. In an embodiment, a process for treating a sour syngas stream that includes sulfur components and carbon dioxide includes absorbing the sulfur components and carbon dioxide from the sour syngas stream in a primary liquid/vapor phase absorption stage with a solvent to produce a liquid absorbent stream. The liquid absorbent stream includes the solvent, the sulfur components, and carbon dioxide. A portion of the sulfur components from the liquid absorbent stream is directly oxidized in the presence of a direct oxidation catalyst to produce elemental sulfur and a recycle stream. The recycle stream includes an unconverted portion of the sulfur components and carbon dioxide. The recycle stream is recycled for further absorption of the unconverted portion of the sulfur components and carbon dioxide through liquid/vapor phase absorption.

    摘要翻译： 本发明提供酸合成气处理装置和处理酸性合成气流的方法。 在一个实施方案中，用于处理包含硫组分和二氧化碳的酸性合成气流的方法包括在主要液/气相吸收阶段中用溶剂从酸性合成气流中吸收硫组分和二氧化碳，以产生液体吸收剂流 。 液体吸收剂流包括溶剂，硫成分和二氧化碳。 来自液体吸收剂流的一部分硫成分在直接氧化催化剂的存在下直接氧化以产生元素硫和再循环流。 再循环流包括未转化的部分硫成分和二氧化碳。 再循环物流被再循环，用于通过液/气相吸收进一步吸收未转化的部分硫成分和二氧化碳。