摘要 |
<p>Multicomponent gas mixtures containing: (1) hydrogen as the primary component, (2) a secondary key component that is more strongly sorbed by the adsorbent than hydrogen, and (3) a minor quantity of one or more dilute tertiary components less strongly sorbed than the secondary key component, are subject to selective adsorption in an adiabatic pressure swing adsorption (PSA) cycle for the separate recovery of high purity hydrogen and the secondary component. A given example is the treatment of the effluent gas from a shift converter in a hydrocarbon reformer plant, wherein hydrogen and carbon dioxide are separately recovered as key components substantially freed of minor dilute components such as methane, carbon monoxide and nitrogen. <IMAGE></p> |
申请人 |
AIR PRODUCTS AND CHEMICALS, INC., ALLENTOWN, PA., US |
发明人 |
KUMAR, RAVI, ALLENTOWN, PA 18103, US;KRATZ, WILBUR CLYMER, MACUNGIE, PA 18062, US |