Simulated moving bed system for CO
A system and method for separating and/or purification of CO 2 gas from a CO 2 feed stream is described. The system and method include a plurality of fixed sorbent beds, adsorption zones and desorption zones, where the sorbent beds are connected via valve and lines to create a simulated moving bed system, where the sorbent beds move from one adsorption position to another adsorption position, and then into one regeneration position to another regeneration position, and optionally back to an adsorption position. The system and method operate by concentration swing adsorption/desorption and by adsorptive/desorptive displacement.
1. A method for the separation and/or purification of CO.sub.2 gas from a CO.sub.2 feed stream, comprising
providing
at least two adsorption positions, the first adsorption position having a second CO.sub.2 stream and producing a second CO.sub.2-depleted stream, and the second adsorption position having a first CO.sub.2 stream and producing a first CO.sub.2-depleted stream;
at least two desorption positions, the first desorption position having a second regeneration stream and producing a second CO.sub.2-enriched stream, and the second desorption position having a first regeneration stream and producing a first CO.sub.2-enriched stream; and
at least two fixed sorbent beds, each sorbent bed comprising a sorbent, a first port at an end of the bed and a second port at an end of the bed distal to the first port;
in a first step, exposing the first sorbent bed to the second CO.sub.2 stream at the first adsorption position, and the second sorbent bed to the first CO.sub.2 stream at the second adsorption position;
in a second step, exposing the first sorbent bed to the first CO.sub.2 stream at the second adsorption position and the second sorbent bed to the second regeneration stream at the first desorption position;
in a third step, exposing the first sorbent bed to the second regeneration stream at the first desorption position and the second sorbent bed to the first regeneration stream at a second regeneration position; and
in an optional fourth step, exposing the second sorbent bed to the second CO.sub.2 stream at the first adsorption position and the first sorbent bed to the first regeneration stream at the second desorption position,
wherein the method is conducted at substantially constant temperature and substantially constant pressure with neither a temperature swing nor pressure swing; and the regeneration streams comprise steam.
2. The method of claim 1 , further providing a system of valves and lines connecting the as least two fixed sorbent beds such that a bed advances from a first adsorption position to a second adsorption position to a first desorption position to the second desorption position, and optionally back to the first adsorption position.
3. The method of claim 1 , wherein the CO 2 -feed stream is directed into both the first CO 2 stream of the second adsorption position and the second CO 2 stream of the first adsorption position such that the two adsorption positions operate in parallel.
4. The method of claim 3 , wherein the first and the second CO 2 depleted streams from the second and first adsorption positions are combined together for collection.
5. The method of claim 1 , wherein the first CO 2 -depleted stream from the second adsorption bed is used as the second CO 2 stream in the first adsorption position such that the two adsorption positions operate in series, and the second CO 2 -depleted stream is collected.
6. The method of claim 1 , wherein a first portion of the second CO 2 depleted stream from the first adsorption position is diverted as a purge stream or as a recycle stream before the CO 2 -depleted stream is collected.
7. The method of claim 1 , wherein the first CO 2 -enriched stream from the second desorption position is used as the second regeneration stream in the first desorption position, such that the desorption positions operate in series.
8. The method of claim 1 , wherein the CO 2 streams enter each sorbent bed in the adsorption positions via the first port, and the CO 2 -depleted stream exits via the second port, and the regeneration streams enter each of the sorbent beds in the desorption positions via the second port, and the CO 2 -enriched stream exits via the first port.
9. The method of claim 1 , wherein the sorbent bed comprises an alkalized sorbent, the alkalized sorbent comprising a substrate and at least one alkali or alkaline earth component.
10. The method of claim 1 , wherein the sorbent bed comprises an alkalized alumina, the alkalized alumina comprising an alumina and at least one alkali or alkaline earth component.