Energy-efficient evaporation process with means for vapor recovery

• US 4,466,202 A
• Filed: 03/07/1983
• Issued: 08/21/1984
• 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: Merten, Ulrich
• Primary Examiner(s): Schwartz, Larry I.
• Assistant Examiner(s): Westphal, David W.
• Application Number:
  US06/473,030
• Time in Patent Office: 533 Days
• Field of Search: 34/27, 34/32, 34/35, 34/73, 34/77, 34/79, 55/16, 55/158, 159/46, 203/26
• US Class Current: 34/470
• CPC Class Codes: F26B 21/04 partly outside the drying enclosure F26B21/006 takes precedence
• CPC Class Codes: F26B 21/08 Humidity
• CPC Class Codes: F26B 23/004 by compressing and condensing vapour in exhaust gases, i.e. using an open cycle heat pump system
• CPC Class Codes: F26B 25/006 Separating volatiles, e.g. recovering solvents from dryer exhaust gases
• CPC Class Codes: F28D 21/0014 the heat being recuperated from waste air or from vapors for air conditioning F24F12/001
• CPC Class Codes: Y02B 30/52 Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

A process is disclosed for the recovery and reuse of heat contained in the wet exhaust gases emanating from a solids dryer or liquor concentrator, particularly one in which drying or concentration is facilitated by purging the vapor with some noncondensable gas such as air or nitrogen. Water or solvent vapor in the moist exhaust mixture is separated from the noncondensable gas or gases by preferentially passing the vapor through a semipermeable membrane. The water or solvent vapor is then compressed and subsequently condensed in a heat exchanger, permitting recovery of its latent heat of vaporization for reuse in the evaporation process. In a drying process, this recovered energy is conveniently used to reheat the dry gases that exit from the membrane separator, permitting the hot, dry gases to be recirculated through the dryer. Alternatively, an indirect heat exchanger may be used to transfer this heat to the material being dried. In an evaporative process for the concentration of a liquor, the recovered energy may be used either to preheat the dry purge gases or to heat the dilute liquor being concentrated.

Claims

1. An energy-efficient process for the recovery of latent heat from a drying process comprising (1) contacting a material containing a volatile liquid with a gaseous drying medium and supplying heat to said drying medium or to said material and thereby producing an exhaust mixture of noncondensable gas and condensable vapor, (2) separating the condensable vapor in said exhaust mixture by passing it through a nonporous nonionic polymeric membrane which is substantially permeable to said condensable vapor and substantially impermeable to said noncondensable gas, (3) transferring said separated condensable vapor, together with the latent heat of condensation contained therein, to a compressor, (4) compressing in said compressor said separated condensable vapor, and (5) condensing said separated condensable vapor by heat exchange, thereby recovering the latent heat of condensation of said separated condensable vapor.

2. The process of claim 1 wherein the noncondensable gas from which said vapor has been separated, together with the sensible heat contained in said noncondensable gas, is recovered and reused.

3. The process of claim 1 wherein said condensable vapor is water vapor and its heat of condensation is reused.

4. The process of claim 3 wherein said nonporous nonionic polymeric membrane is prepared from a hydrophilic polymer.

5. The process of claim 3 wherein said nonporous nonionic polymeric membrane 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.

6. The process of claim 1 wherein said condensable vapor is an organic solvent vapor selected from chlorinated hydrocarbons, aliphatic hydrocarbons, aromatic hydrocarbons, ketones, ethers, alcohols, and carbon disulfide.

7. The process of claim 6 wherein said nonporous nonionic polymeric membrane is selected from polyamides, polyethylene, polypropylene, cellulose acetate, silicone rubber, poly(butadiene-acrylonitrile) rubber, polyethylene-styrene copolymers, polyvinylacetate, poly(ethyleneterephthalate), poly(tetrafluoroethylene)-poly(4-vinyl pyridine or N-vinyl pyrrolidone) graft copolymers, and acrylonitrilevinylacetate copolymers.

8. In an industrial drying process for drying material, said process utilizing hot, dry gas as the drying medium and producing moist or solvent-containing exhaust gas, the improvement comprising:

(a) separating the exhaust gas into a warm, dry noncondensable gas component and a condensable vapor component by passing the condensable vapor in said exhaust mixture through a nonporous nonionic polymeric membrane that is substantially permeable to said condensable vapor and substantially impermeable to said noncondensable gas;

(b) transferring said separated condensable vapor, together with the heat of condensation contained therein, to a compressor;

(c) compressing in said compressor the condensable vapor in said condensable vapor component;

(d) condensing the condensable vapor in said condensable vapor component by heat exchange, thereby recovering the heat of condensation of said condensable vapor; and

(e) transferring by heat transfer means said heat of condensation to said hot, dry gas-drying medium or to the material being dried.

9. The process of claim 8 wherein said condensable vapor component is compressed with a mechanical compressor or vacuum pump.

10. The process of claim 8 wherein said warm, dry noncondensable gas component is recirculated for reuse as the drying medium.

11. The process of claim 10 wherein said heat transfer means is a vapor-to-gas heat exchanger which effects a transfer of the heat of condensation of said vapor to said hot, dry gas drying medium.

12. The process of claim 8 wherein said condensable vapor component of said exhaust gas is water vapor.

13. The process of claim 12 wherein said nonporous nonionic polymeric membrane is prepared from a hydrophilic polymer.

14. The process of claim 13 wherein said nonporous nonionic polymeric membrane 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.

15. The process of claim 8 wherein the hot, dry gas is air or nitrogen.

16. The process of claim 8 wherein said condensable vapor component of said exhaust gas is an organic solvent vapor selected from chlorinated hydrocarbons, aliphatic hydrocarbons, aromatic hydrocarbons, ketones, ethers, alcohols, and carbon disulfide.

17. The process of claim 16 wherein said nonporous nonionic polymeric membrane is selected from polyamides, polyethylene, polypropylene, cellulose acetate, silicone rubber, poly(butadiene-acrylonitrile) rubber, polyethylene-styrene copolymers, polyvinylacetate, poly(ethylene terephthalate), poly(tetrafluoroethylene)-poly(4-vinyl pyridine or N-vinyl pyrrolidone) graft copolymers, and acrylonitrilevinylacetate copolymers.

18. The process of claim 8 wherein the relative humidity of the moist or solvent-containing exhaust gas is from about 30% to about 100%.

19. The process of claim 8 wherein the temperature of the moist or solvent-containing exhaust gas is from about 40°

C. to about 125°

C.

20. The process of claim 8 wherein the partial pressure of water or solvent vapor in the moist or solvent-containing exhaust gas is at least 0.1 atm.

21. The process of claim 8 wherein the heat transfer means is an indirect heat exchanger and the heat of condensation is transferred to the material being dried.

32. The process of claims 6, 16 or 30 wherein said condensable vapor is recovered after condensation.

22. In a process for the concentration of a liquid mixture or solution by evaporation, said process comprising heating the liquid mixture or solution, contacting the liquid mixture or solution with a substantially dry, gaseous stream, and thereby producing a moist, gaseous exhaust mixture, the improvement comprising:

(a) separating the moist, gaseous exhaust mixture into a warm, dry noncondensable gas component and a condensable vapor component by passing said exhaust mixture through a nonporous nonionic polymeric membrane that is substantially permeable to said condensable vapor component and substantially impermeable to said noncondensable gas component;

(b) transferring said separated condensable vapor, together with the heat of condensation contained herein, to a compressor;

(c) compressing in said compressor the condensable vapor in said condensable vapor component;

(d) condensing the condensable vapor in said vapor component by heat exchange, thereby recovering the heat of condensation of said condensable vapor; and

(e) transferring by heat transfer means said heat of condensation to the gaseous drying medium or to the material being concentrated.

23. The process of claim 22 wherein said condensable vapor component is compressed with a mechanical compressor or vacuum pump, said compressor or pump being driven by a motor or a steam-driven turbine.

24. The process of claim 22 said warm, dry noncondensable gas component is recirculated for reuse as the substantially dry gaseous stream.

25. The process of claim 24 wherein said heat transfer means is a vapor-to-gas heat exchanger which transfers said heat of condensation to said gaseous drying medium.

26. The process of claim 22 wherein said condensable vapor is water vapor.

27. The process of claim 26 wherein said nonporous nonionic polymeric membrane is prepared from a hydrophilic polymer.

28. The process of claim 27 wherein said nonporous polymeric membrane is selected from silicone rubbers, natural rubber, synthetic rubbers, cellulose, cellulose esters, polyvinyl alcohol, polyethyleneimine, arylene oxide polymers, arlene oxide ion-exchange polymers, polystyrene sulfonates, polyvinyl butyral, polyvinylacetate, polyethylmethacrylate, polybutadiene, aliphatic polyamides, aromatic polyamides, polyimides, and polybenzimidazoles.

29. The process of claim 22 wherein the substantially dry gaseous stream is air or nitrogen.

30. The process of claim 22 wherein said condensable vapor component is an organic solvent vapor selected from chlorinated hydrocarbons, aliphatic hydrocarbons, aromatic hydrocarbons, ketones, ethers, alcohols, and carbon disulfide.

31. The process of claim 30 wherein said nonporous nonionic polymeric membrane is selected from polyamides, polyethylene, polypropylene, cellulose acetate, silicone rubber, poly(butadiene-acrylonitrile) rubber, polyethylene-styrene copolymers, polyvinylacetate, poly(ethylene terephthalate), poly(tetrafluoroethylene-poly(4-vinyl pyridine or N-vinyl pyrrolidone) graft copolymers, and acrylonitrilevinylacetate copolymers.

33. The process of claim 22 wherein the relative humidity of the moist, gaseous exhaust mixture is from about 30% to about 100%.

34. The process of claim 22 wherein the temperature of the moist, gaseous exhaust mixture is from about 40°

C. to about 125°

C.

35. The process of claim 22 wherein the partial pressure of water or solvent vapor in the moist, gaseous exhaust mixture is at least 0.1 atm.

36. The process of claim 22 wherein said condensable vapor component is compressed and condensed on one surface of an indirect heat exchanger, another surface of said indirect heat exchanger being in contact with said liquid mixture or solution whereby the heat of condensation of said condensable vapor component is transferred to said liquid mixture or solution.

37. The process of claim 22 wherein said heat transfer means is an indirect heat exchanger and said noncondensable vapor component is compressed and used to preheat said liquid mixture or solution by passing said compressed vapor to and condensing said compressed vapor in said indirect heat exchanger, one surface of which is in contact with said liquid mixture or solution.