Gas exchange system and method

Abstract

A gas exchange system, said system comprising: a plurality of cartridges, each having a casing, said casing having a cartridge inlet adjacent to a first end and a cartridge outlet adjacent to an opposed second end; each casing having a bore in which is placed a gas permeable, liquid impermeable, hollow membrane; each hollow membrane having a membrane inlet arranged to receive a gas from an inlet chamber and a membrane outlet for venting said gas; each cartridge inlet in communication with a concentration zone, and arranged to receive a solvent from said concentration zone, so as to exit said solvent through said cartridge outlet; wherein said bore is arranged to flow said solvent adjacent to said hollow membrane so as to permit the exchange of gas through said gas permeable, liquid impermeable membrane.

Claims

1. A gas exchange system comprising: a plurality of cartridges, each of the plurality of cartridges being sealed around the periphery thereof by a casing, the casing having a cartridge inlet adjacent to a first end and a cartridge outlet adjacent to an opposed second end; each casing having a bore in which is placed a gas permeable, liquid impermeable, hollow membrane; each hollow membrane having a membrane inlet arranged to receive a gas from an inlet chamber and a membrane outlet for venting the gas; each cartridge inlet in communication with a concentration zone, and arranged to receive a solvent from the concentration zone, so as to exit the solvent through the cartridge outlet; and wherein the bore is arranged to flow the solvent adjacent to the hollow membrane so as to permit the exchange of gas through the gas permeable, liquid impermeable membrane.

2. The gas exchange system according to claim 1, further comprising a housing within which the cartridges are positioned.

3. The gas exchange system according to claim 2, wherein the concentration zone is located in interstitial voids between the cartridges and between the cartridges and an inner wall of the housing.

4. The gas exchange system according to claim 3, comprising a baffle plate within the housing dividing the interstitial voids proximate to the cartridge inlet from a remaining portion of the interstitial voids, the interstitial voids proximate the inlet defining the concentration zone.

5. The gas exchange system according to claim 4, wherein the housing comprises a solvent inlet in communication with the concentration zone.

6. The gas exchange system according to claim 2, wherein the housing comprises a solvent outlet in fluid communication with the cartridge outlets.

7. The gas exchange system according to claim 2, wherein the housing comprises a gas inlet in fluid communication with the inlet chamber.

8. The gas exchange system according to claim 2, wherein the housing comprises an outlet chamber and a gas outlet for venting the gas from the outlet chamber, the outlet chamber in fluid communication with the membrane outlets.

9. The gas exchange system according to claim 1, wherein the membrane inlet is arranged to receive high temperature gas and the concentration zone is arranged to receive CO.sub.2-laden solvent, the system arranged to strip CO.sub.2 from the CO.sub.2-laden solvent within the cartridges and vent the gas and CO.sub.2 through the membrane outlets, the CO.sub.2-stripped solvent arranged to exit the system through the cartridge outlets.

10. The gas exchange system according to claim 1, wherein the membrane inlet is arranged to receive CO.sub.2 and the concentration zone is arranged to receive solvent, the system arranged to exchange CO.sub.2 through the membrane to the solvent within the cartridges, the CO.sub.2-laden solvent arranged to exit the system through the cartridge outlets.

Description

BRIEF DESCRIPTION OF DRAWINGS

(1) It will be convenient to further describe the present invention with respect to the accompanying drawings that illustrate possible arrangements of the invention. Other arrangements of the invention are possible and consequently, the particularity of the accompanying drawings is not to be understood as superseding the generality of the preceding description of the invention.

(2) FIGS. 1A to 1D show various views of a regeneration module according to one embodiment of the present invention, and;

(3) FIGS. 2A and 2B are various views of a concentration zone for a module according to a further embodiment of the present invention.

DETAILED DESCRIPTION

(4) In general terms, the invention involves placing a concentration zone in fluid communication with inlets for a plurality of cartridges, the cartridges having hollow membranes within a bore of the cartridges, for transporting gas. The hollow membranes are gas permeable but liquid impermeable. By passing the solvent through the bore of the cartridges, so as to be proximate with the external surface of the membranes, a more efficient exchange of gas will occur. The gas is then vented from the membranes, and the solvent flowing out of the cartridges.

(5) FIGS. 1A to 1D, and FIGS. 2A and 2B, show a solvent regeneration module 5 according to one embodiment of the present invention. It will be appreciated that whilst reference is made to the module being used for regeneration, it is equally applicable to the reverse process whereby new solvent is infused with acidic gas. Therefore, whilst the following description makes reference to regeneration, the invention is not limited to the use with a regeneration process but is also applicable to the gas infusion process.

(6) FIG. 1A shows an elevation view of a module 5 having a housing 10 with end caps 15, 20. The end caps 15, 20 include a gas inlet 25 and a gas outlet 30, respectively. Further, the housing 10 includes an inlet 35 for receiving liquid solvent and outlet 40 for exiting said liquid solvent.

(7) FIGS. 1B and 1C show a plurality of cartridges 55 which are grouped in parallel and held in place by support plates 67, 75. The inlet end cap 15 and inlet support plate 67 define an inlet chamber into which the gas is injected through the inlet 25. Each cartridge 55 includes an open end 57 which permits the gas from the inlet chamber to enter into the cartridge 55 and specifically through hollow longitudinal membranes 77. Each cartridge may have one or more membrane located within, depending upon the required flow rate and optimal size of the membrane.

(8) The cartridge 55 further includes interstitial spaces 59 within the bore of the cartridge for receiving solvent, as will be discussed below. The entire cartridge 55 is then sealed around the periphery by a casing 53. The gas is permitted to vent 51 into an outlet chamber defined by outlet support plate 75 and outlet end cap 20 which feed the gas through to the outlet 30.

(9) The solvent enters the housing 10 through the inlet 35 which allows the liquid solvent to flow about the cartridges 55, within an interstitial space 80. The cartridge housing 53, however, prevents direct contact between the solvent within the interstitial space 80 from contacting the membranes 77. According to the present invention, the solvent entering 45 the housing 10 is directed to flow into ingress apertures 65 so as to flow through the cartridge 55 within the interstitial space 59 and thus contact with the membrane 77 before exiting the cartridge 55 through ingress apertures 70.

(10) This arrangement provides a fluid path for the solvent that places the solvent in close proximity to the membranes, and so solves the issue of having a sufficient flow for an efficient gas transfer.

(11) In a further embodiment, the invention provides baffle plates 60 which define concentration zones.

(12) With reference to FIGS. 2A and 2B, the baffle plates 60 define a concentration zone 85 that separates the interstitial spaces 90 near the inlet, ensuring all the solvent flows 95 into the ingress apertures 65 without the solvent escaping directly through the outlet 40. Thus, the use of baffle plates 60 defines a concentration zone 85 which is discrete from the outlet 40, ensuring a flow path for the solvent that is in close proximity to the membranes and thus fully utilizing each of the membranes within the group of cartridges. Once the solvent has flowed through the length of the cartridge 55 it exits from the ingress apertures 70 flowing 100 into the interstitial space 95 proximate to the outlet 40.

(13) It will be appreciated that whilst FIG. 1B shows the position of the baffle plate 60 at approximately two thirds the length of the module 5, in fact the position will be a function of the flow rate 45 into the module 5, the size of the apertures 65, 70 and the desired gas flow rate during the gas transfer within the cartridges. Accordingly, the size of the concentration zone may vary from application to application, subject to various design parameters based upon permeability, flow rate etc.

(14) Further still, in FIG. 1B the baffle plate 60 also acts as an intermediate support plate. The invention is not limited by the number of intermediate support plates and only those intermediate support plates defining a concentration zone may be considered a baffle plate.