Energy-efficient process for the stripping of gases from liquids

• US 4,444,571 A
• Filed: 03/07/1983
• Issued: 04/24/1984
• Est. Priority Date: 03/07/1983
• Status: Expired due to Fees

• Current Assignee: Bend Research Inc. (Lonza Group AG)
• Original Assignee: Bend Research Inc. (Lonza Group AG)
• Inventors: Matson, Stephen L.
• Primary Examiner(s): Spitzer, Robert H.
• Application Number:
  US06/472,713
• Time in Patent Office: 414 Days
• Field of Search: 55/16, 55/46, 55/48-51, 55/53, 55/54, 55/89, 55/158, 55/73, 203/25, 203/39, 203/41, 423/232, 423/233
• US Class Current: 95/48
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: B01D 53/1443 Pretreatment by diffusion
• CPC Class Codes: B01D 53/229 Integrated processes (Diffusion and at least one other process, e.g. adsorption, absorption)

Abstract

A process is disclosed for the recovery and reuse of the heat contained in the gas/vapor overhead mixture from a stripping column in which a noncondensable gas is stripped from a liquid solution by contacting the solution with a hot vapor such as steam. The steam or other vapor in the overhead mixture is separated from the non-condensable gas or gases by preferentially passing the vapor through a semipermeable membrane. The water or other condensable vapor is then compressed and either reinjected at the bottom of the stripping column or condensed in the column reboiler, thus permitting its reuse in the stripping process. If the compressed vapor is reinjected into the stripping column, it serves as the stripping medium itself. If the compessed vapor is condensed in the column reboiler, its latent heat of vaporization is thereby recovered and used to generate the required stripping vapor by boiling the solution being stripped.

Claims

1. In a process for stripping noncondensable or high-vapor-pressure gases from a liquid by contacting said liquid with a stripping vapor and thereby producing an overhead mixture of gas and stripping vapor, the improvement comprising:

(a) separating said stripping vapor in said overhead mixture by passing it through a membrane that is substantially permeable to said separated stripping vapor and substantially impermeable to said gas;

(b) compressing and condensing said separated stripping vapor; and

(c) recovering said separated, condensed stripping vapor and the sensible and latent heat thereof.

2. The process of claim 1 wherein said separated stripping vapor is condensed in a reboiler whereby stripping vapor is generated from said stripped liquid.

6. The process of claim 1 wherein said stripping process takes place in a stripping column having a base for accumulating stripped liquid and wherein said compressed stripping vapor is condensed in a heat exchanger which is in heat exchange communication with said accumulated stripped liquid in said stripping column base.

19. The process of claims 1, 3, 4, 9, 12 or 16 wherein said stripping vapor is water vapor.

21. The process of claim 19 wherein said membane is selected from silicone rubbers, natural rubber, synthetic rubbers, cellulose, cellulose esters, polyvinyl alcohol, polyethyleneimine, arylene oxide polymers, arylene oxide ion-exchange polymers, polystyrene sulfonates, polyvinyl butyral, polyvinylacetate, polyethylmethacrylate, polybutadiene, aliphatic polyamides, aromatic polyamides, polyimides, and polybenzimidazoles.

22. The process of claims 1, 3, 4, 9, 12 or 16 wherein said stripping vapor is an organic solvent vapor selected from chlorinated hydrocarbons, aliphatic hydrocarbons, aromatic hydrocarbons, ketones, ethers, and alcohols.

23. The process of claim 22 wherein said membrane is prepared from a polymer selected from polyamides, polyethylene, polypropylene, cellulose acetate, silicone rubbers, poly(butadiene-acrylonitrile) rubber, polyethylene-styrene copolymers, polyvinylacetate, poly(ethylene terephthalate), poly(tetrafluoroethylene)poly(4-vinyl pyridine or N-vinyl pyrrolidone) graft copolymers, and acrylonitrile-vinylacetate copolymers.

3. In a process for stripping noncondensable or high-vapor-pressure gases from a liquid by contacting said liquid with a stripping vapor and thereby producing an overhead mixture of gas and stripping vapor, said process being conducted in a stripping column with a base, the improvement comprising:

(a) separating said stripping vapor in said overhead mixture by passing it through a membrane that is substantially permeable to said stripping vapor and substantially impermeable to said gas;

(b) compressing said separated stripping vapor; and

(c) injecting said compressed stripping vapor directly into the base of said stripping column as live stripping vapor.

4. In a process for the purification of gases utilizing selective absorption of one or more gaseous components dissolved in a liquid absorbent solution followed by regeneration of the spent liquid absorbent solution in a steam or vapor stripping operation producing an overhead mixture of stripped gas and stripping vapor, the improvement comprising:

(a) separating said stripping vapor in said stripper overhead mixture by passing it through a membrane that is substantially permeable to said stripping vapor and substantially impermeable to said stripped gas;

(b) compressing and condensing said separated stripping vapor;

(c) recovering the heat of condensation of said stripping vapor; and

(d) transferring by heat transfer means said recovered heat of condensation to said liquid absorbent solution.

5. The process of claim 4 wherein said dissolved gaseous components are selected from hydrogen sulfide and carbon dioxide.

7. The process of claim 4 wherein said stripping process takes place in a stripping column having a base for accumulating stripped liquid and wherein said compressed stripping vapor is condensed in a heat exchanger which is in heat exchange communication with said accumulated stripped liquid in said stripping column base.

8. The process of claim 4 wherein said compressed stripping vapor component is condensed in a reboiler whereby stripping vapor is generated from said liquid absorbent solution.

10. The process of claims 4 or 9 wherein said separated stripping vapor is compressed with a mechanical compressor or a vacuum pump.

9. In a process for the purification of gases utilizing selective absorption of one or more gaseous components dissolved in a liquid absorbent solution followed by regeneration of the spent liquid absorbent solution in a steam or vapor stripping operation producing an overhead mixture of stripped gas and stripping vapor, said process being conducted in a stripping column with a base, the improvement comprising:

(a) separating said stripping vapor in said overhead mixture by passing the stripping vapor in said stripper overhead mixture through a membrane that is substantially permeable to said stripping vapor and substantially impermeable to said stripped gas;

(b) compressing said separated stripping vapor; and

(c) injecting said compressed stripping vapor directly into the base of said stripping column as live stripping vapor.

11. The process of claim 9 wherein said dissolved gaseous components are selected from hydrogen sulfide and carbon dioxide.

20. The process of claim 9 wherein said membrane is a hydrophilic polymeric membrane.

12. In a process for stripping high-vapor-pressure contaminants from an aqueous process stream by contacting said aqueous process stream with a condensable stripping vapor and thereby producing an overhead mixture of gas and stripping vapor, the improvement comprising:

(a) separating the stripping vapor in said overhead mixture by passing it through a membrane that is substantially permeable to said stripping vapor and substantially impermeable to said gas;

(b) compressing and condensing said separated stripping vapor; and

(c) recovering both said separated, condensed, stripping vapor and the sensible and latent heat thereof.

13. The process of claim 12 wherein said process takes place in a stripping column having a base for accumulating stripped liquid and wherein said compressed stripping vapor component is condensed in a heat exchanger which is in heat exchange communication with said accumulated stripped liquid in said stripper column base.

14. The process of claim 12 wherein said compressed stripping component is condensed in a reboiler whereby stripping vapor is generated from said stripped aqueous process stream.

15. The process of claims 6, 8, 13 or 14 wherein said recovered and condensed stripping vapor is returned to the top of said stripping column as liquid reflux.

17. The process of claims 12 or 16 wherein the high-vapor-pressure contaminant is selected from hydrogen sulfide and ammonia.

18. The process of claims 4, 9, 12 or 16 wherein the relative humidity, temperature and partial pressure of water or solvent vapor of said stripper overhead mixture are, respectively, from about 30% to about 100%, from about 100°

F. to about 300°

F., and at least 2 psi.

16. In a process for stripping high-vapor-pressure contaminants from an aqueous process stream by contacting said aqueous process stream with a condensable stripping vapor and thereby producing an overhead mixture of gas and stripping vapor, said process being conducted in a stripping column with a base, the improvement comprising:

(a) separating the stripping vapor in said overhead mixture by passing it through a membrane that is substantially permeable to said stripping vapor and substantially impermable to said gas;

(b) compressing said separated stripping vapor; and

(c) injecting said compressed stripping vapor directly into the base of said stripping column as live stripping vapor.