SYSTEM AND METHOD FOR INTEGRATED ADSORPTIVE GAS SEPARATION OF COMBUSTION GASES
    4.
    发明申请
    SYSTEM AND METHOD FOR INTEGRATED ADSORPTIVE GAS SEPARATION OF COMBUSTION GASES 审中-公开
    用于气体吸收气体分离的燃烧气体的系统和方法

    公开(公告)号:US20150375161A1

    公开(公告)日:2015-12-31

    申请号:US14845764

    申请日:2015-09-04

    Inventor: Andre BOULET

    Abstract: An integrated fuel combustion system with adsorptive gas separation separates a portion of carbon dioxide from a combustion gas mixture and provides for recycle of separated carbon dioxide to the intake of the fuel combustor for combustion. A process for carbon dioxide separation and recycle includes: admitting combustion gas to an adsorptive gas separation system contactor containing adsorbent material; adsorbing a portion of carbon dioxide; recovering a first product gas depleted in carbon dioxide for release or use; desorbing carbon dioxide from the adsorbent material and recovering a desorbed second product gas enriched in carbon dioxide for sequestration or use; admitting a conditioning fluid into the contactor and desorbing a second portion of carbon dioxide to recover a carbon dioxide enriched conditioning stream; and recycling a portion of the carbon dioxide enriched conditioning stream to an inlet of fuel combustor to pass through the fuel combustor for combustion.

    Abstract translation: 具有吸附气体分离的综合燃料燃烧系统将一部分二氧化碳与燃烧气体混合物分离,并提供分离的二氧化碳再循环到燃料燃烧器的进气口进行燃烧。 二氧化碳分离和再循环的方法包括:将燃烧气体导入含有吸附材料的吸附气体分离系统接触器; 吸附一部分二氧化碳; 回收用于释放或使用的二氧化碳消耗的第一产品气体; 从吸附剂材料中解吸二氧化碳并回收富含二氧化碳的解吸附的第二产物气体用于封存或使用; 将调理流体接纳到接触器中并解吸第二部分二氧化碳以回收富含二氧化碳的调理流; 以及将一部分富含二氧化碳的调理流循环到燃料燃烧器的入口以通过燃料燃烧器进行燃烧。

    COMBUSTION SYSTEM INCORPORATING TEMPERATURE SWING ADSORPTIVE GAS SEPARATION

    公开(公告)号:US20190107009A1

    公开(公告)日:2019-04-11

    申请号:US16089700

    申请日:2017-03-30

    Abstract: A combustion system and process of operating the combustion system incorporating an electrostatic precipitator, an optional flue gas desulfurizer, and a temperature swing adsorptive gas separator, for post-combustion emission abatement is provided. A very low pressure steam stream may be employed as a first regeneration stream for the temperature swing adsorptive gas separator where the very low pressure steam stream may optionally be recovered from, a very low pressure steam turbine or an auxiliary boiler. A fluid stream at a suitable temperature for regeneration of at least one adsorbent material in the temperature swing adsorptive gas separator may be employed as a second regeneration stream where the fluid stream may optionally be recovered from an electrostatic precipitator, an oxidant preheater, or an auxiliary heater.

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