Extruder system and method for treatment of a gaseous medium
A system for treatment of a gaseous medium, comprises an extruder having a barrel. The extruder further comprises a first inlet port, a second inlet port, and a plurality of outlet ports coupled to the barrel. The first inlet port is configured for feeding a lean sorbent, the second inlet port is configured for feeding a gaseous medium, and the plurality of outlet ports are configured for releasing a plurality of components removed from the gaseous medium. Further, the extruder comprises a plurality of helical elements coupled to a plurality of kneading elements, mounted on a shaft, and disposed within the barrel. The barrel and the plurality of helical and kneading elements together form an absorption unit and a desorption unit. The first and second inlet ports are formed in the absorption unit and the plurality of outlet ports are formed in the absorption and desorption units.
1. A method for treatment of a gaseous medium, the method comprising:
reacting a lean sorbent with the gaseous medium within an absorption unit to absorb a component from the gaseous medium and generate a rich sorbent;
feeding the rich sorbent from the absorption unit to a desorption unit; and
desorbing the component from the rich sorbent in the desorption unit and regenerate the lean sorbent, wherein the reacting, feeding, and desorbing are performed via a plurality of helical elements and a plurality of kneading elements mounted on a shaft disposed within a barrel of an extruder, wherein the plurality of helical elements are coupled to the plurality of kneading elements, wherein the barrel, the plurality of helical elements and the plurality of kneading elements together form the absorption unit and the desorption unit.
2. The method of claim 1 , further comprising compressing a portion of the desorbed component released via at least one outlet port disposed proximate to an exit of the desorption unit.
3. The method of claim 1 , further comprising cooling the lean sorbent released from the desorption unit and recirculating a cooled lean sorbent to the absorption unit.
4. The method of claim 1 , further comprising feeding a cooling medium through at least one of a cooling unit coupled to a portion of the barrel in the absorption unit and a cooling channel disposed within the shaft, in the absorption unit.
5. The method of claim 4 , further comprising feeding a heating medium through at least one of a heating unit coupled to another portion of the barrel in the desorption unit and a heating channel disposed within the shaft, in the desorption unit.
6. The method of claim 5 , wherein the heating medium is at least one of the lean sorbent and a flue gas from a machine.
7. The method of claim 1 , further comprising generating a dynamic back pressure against a flow of the rich sorbent in at least one section of the desorption unit via at least one element from the kneading element and helical element.
8. The method of claim 1 , further comprising conveying the gaseous medium, the lean sorbent, and the rich sorbent via the plurality of helical elements and the plurality of kneading elements.
9. The method of claim 1 , wherein the reacting further comprises mixing the gaseous medium and the lean sorbent via the plurality of kneading elements.
10. The method of claim 1 , further comprising compressing the rich sorbent or the lean sorbent against an inner surface of the barrel, via the plurality of kneading or helical elements.