Adsorption process for recovering two high purity gas products from multicomponent gas mixtures
OwnerRavi Kumarinventor
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OwnerRavi Kumarinventor
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An improved pressure swing adsorption process is disclosed for the recovery of high-purity primary and secondary components from a multicomponent gas mixture. The process utilizes a first group of absorbent beds selective for the secondary component and a second group of adsorbent beds selective for retention of tertiary impurities in the mixture. The gas mixture is passed through a first and second bed in series, very high purity primary component product is discharged from the second bed, and high purity secondary component product is recovered by desorption from the first bed. A low-pressure purge of the first bed with high-purity secondary component product is utilized to minimize compression power and improve purity of the secondary product component. Several novel pressure equalization steps improve primary product recovery and reduce power consumption. Further increased product recovery is realized by recycling depressurization and purge streams from the first bed. The process can be used to recover high-purity hydrogen and carbon dioxide from a gas mixture containing these components along with minor amounts of methane, carbon monoxide, and nitrogen.
In the separation of a multicomponent gas mixture by pressure swing adsorption to recover as individual products a primary key component and a secondary key component, wherein the secondary key component is more strongly adsorbed than the primary key component and there is present in the multicomponent gas mixture one or more minor tertiary components at low concentrations which are less strongly adsorbed than the secondary key component, by passing the multicomponent gas mixture in an adsorption step through a first bed of adsorbent selective for retention of the secondary key component, passing the effluent from said first bed through a second bed of adsorbent selective for the retention of the secondary key component and of the one or more minor tertiary components, withdrawing from said second bed a high purity product stream of the primary key component, and continuing said passing of the multicomponent gas mixture through the first and second beds for a predetermined time period or until the concentration of the secondary key component in the effluent from the first bed or the concentration of at least one of the tertiary components in said high-purity stream of said primary key component from the second bed reaches a predetermined level;
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