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    • 5. 发明授权
    • Process for the separation of a gaseous mixture
    • 分离气体混合物的方法
    • US4348213A
    • 1982-09-07
    • US248600
    • 1981-03-27
    • John W. Armond
    • John W. Armond
    • B01D53/04
    • B01D53/04B01D2253/102B01D2256/10B01D2256/12B01D2257/104B01D2259/402B01D53/047B01D53/053
    • In a gas separation process a pressurized gaseous mixture is passed through a first bed of adsorbent while a second bed is being regenerated by desorbing gas therefrom and venting or discharging such gas from the second bed. The adsorbent is of such a character that one component of the gaseous mixture is preferentially adsorbed. The non-adsorbed component or components are collected as product. After a chosen time flow of gas into the first bed and out of the second bed is stopped, and the two beds are placed in communication with one another through a flow restrictor means so as to reduce the pressure difference therebetween. The flow restriction means is effective to prevent fluidization of the beds. The intercommunication between the two beds is stopped before the pressure difference therebetween has been eliminated and the gas mixture is then passed through the second bed, while the first is regenerated. The pressure difference between the two beds is then reduced and the cycle of operations repeated.
    • 在气体分离过程中,加压的气体混合物通过第一吸附剂床,而通过从其中解吸气体并从第二床排出或排出这种气体而再生第二床。 吸附剂具有如下特征:气态混合物的一个成分被优先吸附。 作为产品收集未吸附的组分或组分。 在选择的气体进入第一床并离开第二床之后停止流动,并且两个床通过限流装置彼此连通,以便减小它们之间的压力差。 流量限制装置有效地防止床的流化。 在两个床之间的压力差已经消除之前停止两个床之间的相互通信,然后使气体混合物通过第二床,同时第一床被再生。 然后减小两张床之间的压差,并重复操作循环。
    • 7. 发明授权
    • Process and apparatus for separation of a gaseous mixture
    • 用于分离气体混合物的方法和装置
    • US4576614A
    • 1986-03-18
    • US314949
    • 1981-10-26
    • John W. ArmondKenneth C. Smith
    • John W. ArmondKenneth C. Smith
    • B01D53/04
    • B01D53/04B01D2256/10B01D2257/104B01D2257/504B01D2257/80B01D2259/40003B01D2259/40083B01D2259/402B01D53/0446Y02C10/08
    • A compressed gas mixture, for example air, is passed through one of beds 12 and 14 of adsorbent that selectively adsorbs oxygen from the air. Unadsorbed nitrogen-enriched gas flows into a buffer vessel 28, from which product gas is withdrawn through pipeline 30. While one of the beds 12 and 14 is adsorbing oxygen for air the other is being regenerated, and during this period the communication between the beds is denied. At the end of a chosen period of time the beds are placed in communication with one another by opening valves 54 and 56. Then the bed that was previously being regenerated is placed in communication with the source of compressed air and the other bed regenerated. The period of intercommunication between the beds lasts for as long as it takes the volume of product gas as measured by an integrating flow meter 31 from the start of the preceding adsorption step to reach a chosen value. The apparatus is able to supply nitrogen of a chosen purity at a variable flow rate.
    • 压缩气体混合物,例如空气,通过选择性吸附空气中的氧气的吸附剂床12和14之一。 未吸收的富氮气体流入缓冲容器28,产物气体从该容器28通过管道30排出。尽管床12和14中的一个吸附氧气用于空气,另一个正在再生,并且在此期间床之间的连通 被拒绝。 在所选择的时间段结束时,通过打开阀54和56将床彼此连通。然后将先前再生的床与压缩空气源连通并且另一床再生。 只要从先前的吸附步骤开始就通过积分流量计31测量的产品气体的体积达到选定的值,则床之间的相互通信时间将持续。 该装置能够以可变流量供应选定纯度的氮。