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    PLANT AND PROCESS FOR RECOVERING CARBON DIOXIDE
    2.
    发明申请
    PLANT AND PROCESS FOR RECOVERING CARBON DIOXIDE 审中-公开
    回收二氧化碳的工厂和工艺

    公开(公告)号：US20110005389A1

    公开(公告)日：2011-01-13

    申请号：US12746972

    申请日：2008-12-12

    申请人： Paul Anthony Webley ,  Jun Zhang

    发明人： Paul Anthony Webley ,  Jun Zhang

    IPC分类号： B01D53/047

    CPC分类号： B01D53/0476 ,  B01D53/229 ,  B01D2253/102 ,  B01D2253/104 ,  B01D2253/106 ,  B01D2253/108 ,  B01D2256/22 ,  B01D2259/40043 ,  B01D2259/40064 ,  B01D2259/402 ,  Y02C10/04 ,  Y02C10/08

    摘要： The present invention relates to a process and plant for the recovery of carbon dioxide from a gas stream by means of pressure swing adsorption using an adsorbent, such as X or Y type Zeolite adsorbents. The gas feed stream suitably has a moderate concentration of carbon dioxide, such as gas emitted from the filling bowl of the carbonated drinks bottling plant and is recovered without rinsing or purging the adsorbent with a high purity carbon dioxide gas stream. The process therefore provides the advantage of being capturing carbon dioxide from the effluent that would otherwise be emitted to the atmosphere and captures the carbon dioxide in a manner that minimises operational and capital expenditure. The present invention also relates to a process for utilizing one dry stream from a gas separation unit (adsorption or membrane process) to conduct evaporative cooling of water, which is used as the water in a liquid ring vacuum pump thereby decreasing the vacuum level and improving the performance.

    摘要翻译： 本发明涉及使用吸附剂如X或Y型沸石吸附剂通过变压吸附从气流中回收二氧化碳的方法和设备。 气体进料流适当地具有中等浓度的二氧化碳，例如从碳酸饮料装瓶厂的填充碗排出的气体，并且在不用高纯度二氧化碳气流冲洗或清洗吸附剂的情况下回收。 因此，该方法提供了从流出物中捕获二氧化碳的优点，否则这些二氧化碳将被排放到大气中并以最小化操作和资本支出的方式捕获二氧化碳。 本发明还涉及利用来自气体分离单元（吸附或膜过程）的一个干燥流进行水的蒸发冷却的方法，该水用作液环真空泵中的水，从而降低真空度并提高 的表现。

    Reactor, plant and process
    3.
    发明授权
    Reactor, plant and process 有权
    反应堆，工厂和过程

    公开(公告)号：US08641805B2

    公开(公告)日：2014-02-04

    申请号：US12599751

    申请日：2008-05-12

    申请人： Geoff Stevens ,  Barry Hooper ,  Craig Dugan ,  Paul Anthony Webley

    发明人： Geoff Stevens ,  Barry Hooper ,  Craig Dugan ,  Paul Anthony Webley

    IPC分类号： B01D47/00

    CPC分类号： B01D53/1475 ,  B01D53/18 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06

    摘要： The present invention relates to reactor vessels such as absorbing or stripping columns that are suitable for capturing carbon dioxide from flue gas streams of fossil fuel fired powered stations such as coal fired power stations generating 100 to 500 MW. The side walls of the reactors are made of concrete or structural ceramics that are preferrably steel reinforced. The reactors are on a sufficiently large scale such that a flue gas stream in the order of at least 1,000 t/hr and normally greater than 2,000 or 3,000 t/hr can be scrubbed of carbon dioxide in a single absorption column and then recovered in a stripping column. The absorbing and stripping columns may be free standing structures or, alternatively, the absorbing column may be located at least partially within the stripping column.

    摘要翻译： 本发明涉及反应器容器，例如吸收或汽提塔，其适用于从化石燃料燃烧的动力站（例如产生100至500MW的燃煤发电站）的烟道气流中捕获二氧化碳。 反应器的侧壁由优选钢筋混凝土或结构陶瓷制成。 反应器的尺寸足够大，使得在单个吸收塔中可以将具有至少1000吨/小时，通常大于2,000或3,000吨/小时的烟道气流除去二氧化碳，然后在 剥离柱。 吸收和汽提塔可以是自由结构，或者，吸收塔可以至少部分地位于汽提塔内。

    REACTOR, PLANT AND PROCESS
    4.
    发明申请
    REACTOR, PLANT AND PROCESS 有权
    反应器，工厂和工艺

    公开(公告)号：US20110296994A1

    公开(公告)日：2011-12-08

    申请号：US12599751

    申请日：2008-05-12

    申请人： Geoff Stevens ,  Barry Hooper ,  Craig Dugan ,  Paul Anthony Webley

    发明人： Geoff Stevens ,  Barry Hooper ,  Craig Dugan ,  Paul Anthony Webley

    IPC分类号： B01D53/14 ,  B01D47/00

    CPC分类号： B01D53/1475 ,  B01D53/18 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06

    摘要： The present invention relates to reactor vessels such as absorbing or stripping columns that are suitable for capturing carbon dioxide from flue gas streams of fossil fuel fired powered stations such as coal fired power stations generating 100 to 500 MW. The side walls of the reactors are made of concrete or structural ceramics that are preferrably steel reinforced. The reactors are on a sufficiently large scale such that a flue gas stream in the order of at least 1,000 t/hr and normally greater than 2,000 or 3,000 t/hr can be scrubbed of carbon dioxide in a single absorption column and then recovered in a stripping column. The absorbing and stripping columns may be free standing structures or, alternatively, the absorbing column may be located at least partially within the stripping column.

    摘要翻译： 本发明涉及反应器容器，例如吸收或汽提塔，其适用于从化石燃料燃烧的动力站（例如产生100至500MW的燃煤发电站）的烟道气流中捕获二氧化碳。 反应器的侧壁由优选钢筋混凝土或结构陶瓷制成。 反应器的尺寸足够大，使得在单个吸收塔中可以将具有至少1000吨/小时，通常大于2,000或3,000吨/小时的烟道气流除去二氧化碳，然后在 剥离柱。 吸收和汽提塔可以是自由结构，或者，吸收塔可以至少部分地位于汽提塔内。

    VSA adsorption process with energy recovery
    5.
    发明授权
    VSA adsorption process with energy recovery 失效
    VSA吸附过程与能量回收

    公开(公告)号：US5656067A

    公开(公告)日：1997-08-12

    申请号：US606137

    申请日：1996-02-23

    申请人： Charles Franklin Watson ,  Rakesh Agrawal ,  Paul Anthony Webley ,  Joseph Gerard Wehrman

    发明人： Charles Franklin Watson ,  Rakesh Agrawal ,  Paul Anthony Webley ,  Joseph Gerard Wehrman

    IPC分类号： B01D53/047 ,  B01D53/053

    CPC分类号： B01D53/0476 ,  B01D53/053 ,  B01D2256/12 ,  B01D2259/40052 ,  B01D2259/40067 ,  B01D2259/40079 ,  B01D2259/40081 ,  B01D2259/403 ,  B01D53/0446

    摘要： A vacuum swing adsorption process for separating a feed gas mixture into a more strongly adsorbable component and a less strongly adsorbable component in a process employing two vacuum pumps and three adsorbent beds containing an adsorbent selective for the more strongly adsorbable component using countercurrent depressurization and cocurrent ambient feed repressurization simultaneous with product end to product end pressure equalization and a common-shaft machinery arrangement which allows the expansion energy contained in the countercurrent depressurization and cocurrent ambient feed repressurization streams to be recovered and utilized to reduce overall process power consumption. Addition of three valves and an expander element will also allow expansion energy in the product purge and pressure equalization streams to be recovered. Oxygen product can be recovered from air at low cost using the process.

    摘要翻译： 一种用于将进料气体混合物分离成更强吸附组分和较不易吸附的组分的真空挥发吸附方法，该方法使用两个真空泵和三个吸附床，该吸附床含有选择性较强吸附组分的吸附剂，使用逆流减压和并流环境 进料再加压同时与产品端到产品端压力均衡和共轴机械装置，其允许包含在逆流减压和并流环境进料再加压流中的膨胀能被回收和利用以减少总体过程功率消耗。 添加三个阀和膨胀元件也将允许产品吹扫和压力平衡流中的膨胀能被回收。 使用该方法可以以低成本从空气中回收氧气产物。