Device and method for removing water and carbon dioxide from a gas mixture using pressure swing adsorption
AssigneeMMR Technologies, Inc.
InventorsWilliam A. Little, Sam Spektor
Life of this patent
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Abstract
A pressure swing adsorption (PSA) dryer for separating water and carbon dioxide from a gas stream includes two compound adsorbent columns [32, 42]. Each column comprises a primary adsorption material for adsorbing water and a secondary adsorbent that adsorbs carbon dioxide. The secondary adsorbent comprises a solid amine. The secondary adsorbent may be, for example, a highly porous polystyrene matrix with amine groups bonded to the porous resin structure. Preferably, a mixture of the primary and secondary adsorbent materials forms an intermediate layer [38, 48] sandwiched between a top layer [34, 44] and bottom layer [36, 46] of pure water adsorbent material in each of the columns [32, 42].
Claims14
A pressure swing adsorption (PSA) dryer comprising two adsorption columns, wherein each of the adsorption columns comprises a mixture of primary and secondary adsorbents, wherein the primary adsorbent adsorbs water and the secondary adsorbent adsorbs carbon dioxide, wherein the secondary adsorbent comprises a solid amine;
- wherein the mixture is packed in the columns in three layers:
- a top layer, a bottom layer, and a middle layer sandwiched between the top layer and bottom layer,
- wherein both the top layer and the bottom layer contain just primary adsorbent material, and wherein the middle layer contains a mixture of the primary and secondary adsorbent materials.
A method for reducing the concentration of water and carbon dioxide in a gaseous stream using pressure swing adsorption, the method comprising:
- a) passing the gaseous stream through a first adsorbent column to produce a dry flow having reduced water and carbon dioxide content;
- b) dividing the dry flow into a product flow and a purge flow;
- c) increasing the volume and decreasing the pressure of the purge flow to produce an expanded purge flow;
- d) passing the expanded purge flow through a second adsorbent column to produce a moist exhaust flow having increased water and carbon dioxide content;
- and
- e) reversing the direction of flow through the first and second adsorbent columns;
- wherein each of the first and second adsorbent columns comprises a mixture of primary and secondary adsorbents, wherein the primary adsorbent adsorbs water and the secondary adsorbent adsorbs carbon dioxide, wherein the secondary adsorbent comprises a solid amine;
- wherein the mixture is packed in the columns in three layers:
- a top layer, a bottom layer, and a middle layer sandwiched between the top layer and bottom layer,
- wherein both the top layer and the bottom layer contain just primary adsorbent material, and wherein the middle layer contains a mixture of the primary and secondary adsorbent materials.
Dependencies are inferred from the claim text.