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    • 4. 发明授权
    • Air purification process
    • 空气净化过程
    • US5906675A
    • 1999-05-25
    • US940319
    • 1997-09-30
    • Ravi JainJames K. Tseng
    • Ravi JainJames K. Tseng
    • B01D53/047B01D53/26
    • B01D53/0462B01D53/047B01D53/261F25J3/04163F25J3/04169B01D2253/104B01D2253/108B01D2257/504B01D2257/80B01D2259/403B01D2259/4146B01D2259/416F25J2205/64F25J2205/82F25J2215/44Y02C10/08
    • An air prepurification process carried out in a battery of three adsorption vessels arranged in parallel. The process includes three steps: a first step in which non-steady state PSA is carried out in the first and second vessels operated in alternating adsorption and bed regeneration mode while the adsorbent in the third vessel undergoes thermal regeneration; a second step in which non-steady state PSA is carried out in the second and third vessels operated in alternating adsorption and bed regeneration modes while the adsorbent in the first vessel undergoes thermal regeneration; and a third step in which non-steady state PSA is carried out in the first and third vessels operated in alternating adsorption and bed regeneration modes while the adsorbent in the second vessel undergoes thermal regeneration. Each vessel contains at least two adsorbent layers, including a first layer of activated alumina, which adsorbs substantially all moisture and some carbon dioxide from the feed air, and a second layer of zeolite, which adsorbs substantially all of the remaining carbon dioxide in the feed air. The feed air may be passed through beds of hydrogen oxidation and carbon monoxide oxidation catalysts positioned between the first and second layers, to convert any hydrogen and carbon monoxide in the feed air to water vapor and carbon dioxide, respectively, these components being removed from the feed air as it passes through the layer of zeolite.
    • 空气预净化过程是在三个并联布置的吸附容器的电池中进行的。 该方法包括三个步骤:在第三容器中的吸附剂经受热再生的同时,在交替吸附和床再生模式下操作的第一和第二容器中进行非稳态PSA的第一步骤; 在第二容器和第三容器中以不同的吸附和床再生模式运行的非稳态PSA进行第二步骤,同时第一容器中的吸附剂进行热再生; 以及第三步骤,其中在第一和第三容器中以不同的吸附和床再生模式运行的第一和第三容器中进行非稳态PSA,而第二容器中的吸附剂经历热再生。 每个容器包含至少两个吸附剂层,其包括第一层活性氧化铝,其从进料空气中吸收基本上所有的水分和一些二氧化碳,以及第二层沸石,其吸附进料中基本上所有剩余的二氧化碳 空气。 进料空气可以通过位于第一和第二层之间的氢氧化和一氧化碳氧化催化剂床,以将进料空气中的任何氢和一氧化碳分别转化成水蒸汽和二氧化碳,这些组分从 进料空气通过沸石层。