Pressure-swing adsorption method and device
Fractionation by adsorption of a hydrogen-containing gas mixture can be achieved by passing the gas mixture over an adsorption bed containing an activated-carbon layer a downstream molecular sieve layer of the 5 A type, and positioned between the activated-carbon layer and the downstream molecular sieve layer, an intermediate layer containing molecular sieve of the X type. A hydrogen-rich gas mixture is then removed. The molecular sieve(s) of the X type, can be a CaX type, an NaX type, or combinations thereof.
1 . A method for fractionation of a hydrogen-containing gas mixture by adsorption, comprising:
passing the gas mixture over an adsorption bed containing an activated-carbon layer, a downstream molecular sieve layer of the 5 A type, and between said activated-carbon layer and said downstream molecular sieve layer, an intermediate layer containing a molecular sieve of the X type; and
removing a hydrogen-rich gas mixture from said adsorption bed.
2 . A method according to claim 1 , wherein said molecular sieve(s) of the X type is a CaX type, an NaX type, or a combination thereof.
3 . A method according to claim 1 , wherein the ratio of activated-carbon layer:intermediate layer:molecular sieve layer in volume fractions is 0.1 to 0.5:0.1 to 0.5:0.2 to 0.8, preferably 0.3:0.2:0.5.
4 . A method according to claim 3 , wherein the ratio of activated-carbon layer:intermediate layer:molecular sieve layer in volume fractions is 0.3:0.2:0.5.
5 . A method according to claim 1 , wherein said hydrogen-containing gas mixture contains water and water is removed from said hydrogen-containing gas mixture in an adsorbent layer upstream of said activated-carbon layer.
6 . A device for fractionation by adsorption of a hydrogen-containing gas mixture, comprising:
an activated-carbon layer;
an intermediate layer containing a molecular sieve of the X type; and
a downstream molecular sieve layer of the 5 A type;
wherein said intermediate layer is positioned between said activated-carbon layer and said downstream molecular sieve layer of the 5 A type.
7 . A device according to claim 6 , wherein said molecular sieve(s) of the X type is a CaX type, an NaX type, or a combination thereof.
8 . A device according to claim 6 , wherein the ratio of activated-carbon layer:intermediate layer:molecular sieve layer in volume fractions is 0.1 to 0.5:0.1 to 0.5:0.2 to 0.8, preferably 0.3:0.2:0.5.
9 . A device according to claim 8 , wherein the ratio of activated-carbon layer:intermediate layer:molecular sieve layer in volume fractions is 0.3:0.2:0.5.
10 . A device according to claim 6 , wherein an adsorbent layer suitable for removing water is positioned upstream of said activated-carbon layer.
11 . A method according to claim 1 , wherein said intermediate layer consists of molecular sieve of the X type.
12 . A device according to claim 6 , wherein said intermediate layer consists of molecular sieve of the X type.
13 . A device for fractionation by adsorption of a hydrogen-containing gas mixture, comprising:
an absorber having an inlet and an outlet and, positioned between said inlet and said outlet, an activated-carbon layer, an intermediate layer containing a molecular sieve of the X type, and a downstream molecular sieve layer of the 5 A type;
wherein said intermediate layer is positioned between said activated-carbon layer and said downstream molecular sieve layer of the 5 A type.
14 . In a pressure-swing adsorption system comprising a plurality of adsorbers connected in series, the improvement wherein said plurality of adsorbers includes at least one adsorber according to claim 13 .
15 . A method for fractionation of a hydrogen-containing gas mixture by adsorption, comprising:
Introducing the gas mixture into a pressure-swing adsorption system according to claim 14 ; and
removing a hydrogen-rich gas mixture from said adsorption system.