초록 ▼

Carbon dioxide is selectively adsorbed and separated from non-acidic gases such as nitrogen, hydrogen and methane using a pressure swing adsorption process in a fixed adsorption bed containing a faujasite type of zeolitic aluminosilicate containing at least 20 equivalent percent of at least one cati

Carbon dioxide is selectively adsorbed and separated from non-acidic gases such as nitrogen, hydrogen and methane using a pressure swing adsorption process in a fixed adsorption bed containing a faujasite type of zeolitic aluminosilicate containing at least 20 equivalent percent of at least one cation species selected from the group consisting of zinc, rare earth, hydrogen and ammonium and containing not more than 80 equivalent percent of alkali metal or alkaline earth metal cations.

대표청구항 ▼

Cyclic process for selectively separating CO2 from mixtures thereof with non-acidic gases by the selective adsorption of the CO2 which comprises the steps of: (a) providing a fixed adsorption bed containing a zeolitic molecular sieve of the faujasite type having a framework SiO2/Al2O3 molar ratio of

Cyclic process for selectively separating CO2 from mixtures thereof with non-acidic gases by the selective adsorption of the CO2 which comprises the steps of: (a) providing a fixed adsorption bed containing a zeolitic molecular sieve of the faujasite type having a framework SiO2/Al2O3 molar ratio of from 2 to 100 and containing at least 20 equivalent percent of one or a mixture of two or more cation species selected from the group consisting of zinc, rare earth, hydrogen and ammonium and containing not more than 80 equivalent percent of alkali or alkaline earth metal cations or mixtures thereof; (b) passing said gas mixture into said bed at a temperature of from -50°C. to 100°C. and at a pressure of from 0.2 to 1000 psia whereby CO2 is selectively adsorbed on said zeolite and recovering a gas product depleted with respect to CO2; (c) terminating the passage of said gas stream into said bed prior to the time of breakthrough of the CO2 from the egress end thereof; (d) regenerating the adsorption bed by desorbing CO2 therefrom by decreasing the pressure in said bed to below the adsorption pressure of step (b) and to within the range of 0.1 to 500 psia, and; (e) repeating steps (a) through (d).