Method and membrane system for sterilizing and preserving liquids using carbon dioxide

• US 6,331,272 B1
• Filed: 01/12/1999
• Issued: 12/18/2001
• Est. Priority Date: 01/12/1999
• Status: Expired due to Term

• Current Assignee: Porocrit LLC
• Original Assignee: Porocrit LLC
• Inventors: Sims, Marc
• Primary Examiner(s): JASTRZAB, KRISANNE MARIE
• Application Number:
  US09/228,925
• Time in Patent Office: 1,071 Days
• Field of Search: 422/28, 422/1, 422/31, 422/33, 422/41, 422/48, 422/256, 422/905, 426/330, 426/330.3, 426/335, 426/424-425, 994/95, 210/634, 210/644, 210/648, 210/321.6, 210/321.64, 210/321.79
• US Class Current: 422/28
• CPC Class Codes: A23L 2/42 Preservation of non-alcoholic beverages
• CPC Class Codes: A23L 3/3409 in the form of gases, e.g. fumigation; Compositions or apparatus therefor
• CPC Class Codes: A61L 2/0088 Liquid substances
• CPC Class Codes: A61L 2/0094 Gaseous substances
• CPC Class Codes: B01D 61/00 Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor separation of gases or vapours by diffusion B01D53/22
• CPC Class Codes: B01D 63/02 Hollow fibre modules
• CPC Class Codes: B01D 63/033 Specific distribution of fibres within one potting or tube-sheet
• CPC Class Codes: B01J 19/2475 Membrane reactors
• CPC Class Codes: B01J 2219/00162 controlling the pressure
• CPC Class Codes: C02F 1/44 by dialysis, osmosis or reverse osmosis general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268
• CPC Class Codes: C02F 1/50 by addition or application of a germicide or by oligodynamic treatment C02F1/4606, C02F1/467, C02F1/76 take precedence
• CPC Class Codes: Y10S 422/905 Miscellaneous liquid sterilization means

Abstract

Microorganisms are destroyed and enzymes can be inactivated in liquids, such as juices for example, by continuously flowing the liquid and continuously flowing pressurized dense CO₂ along flow paths which are separated by membrane having minute pores at which the flows contact each other in a nondispersive manner. Pressures in the two flow paths are equalized and the dense CO₂ flow is continuously recirculated without depressurization. Contact between the flows can be maximized by using a plurality of parallel hollow fiber porous membranes with one of the flows being directed into the hollow fibers and the other of the flows being directed along exterior surfaces of the fibers. The process does not adversely affect properties of the liquid, such as taste, aroma and nutritional content, as heating of the liquid to a high temperature is unnecessary.

Claims

1. A method for preserving a liquid by exposure of the liquid to pressurized dense carbon dioxide comprising the steps of:

directing the flow of said liquid along a liquid flow path which extends along a first surface of a porous membrane and directing a flow of said pressurized dense carbon dioxide along a separate carbon dioxide flow path which extends along an opposite surface of said porous membrane including contacting said liquid and pressurized dense carbon dioxide at pores in said membrane, and

recirculating said flow of pressurized dense carbon dioxide through said carbon dioxide flow path including maintaining the pressurized dense carbon dioxide in the pressurized dense condition throughout the recirculation thereof.

2. The method of claim 1 including the further step of maintaining substantially the same elevated pressure in said liquid flow path and in said carbon dioxide flow path.

3. The method of claim 1 wherein said liquid has a constituent that is soluble in dense carbon dioxide and which becomes a solute in said dense carbon dioxide during passage of said dense carbon dioxide along said carbon dioxide flow path, including the further step of establishing saturation of said dense carbon dioxide with said solute and maintaining said saturation of said dense carbon dioxide with said solute during said recirculation of said dense carbon dioxide.

4. The method of claim 1 including the further steps of continuously receiving liquid from said liquid flow path in a first receiver tank and maintaining said first receiver tank at a pressure which is substantially the same as the pressure within said carbon dioxide flow path.

5. The method of claim 4 including the further steps of depressurizing said liquid while continuously releasing the liquid from said first receiver tank into a second receiver tank, recovering low pressure carbon dioxide from said second receiver tank, recompressing the recovered low pressure carbon dioxide and returning recompressed carbon dioxide to said carbon dioxide flow path.

6. The method of claim 1 wherein said liquid flow path and carbon dioxide flow path are defined by a plurality of hollow fiber porous membranes, including directing one of said flow of liquid and said flow of dense carbon dioxide through into said hollow fiber porous membranes and directing the other of said flow of liquid and said flow of dense carbon dioxide along external surfaces of said hollow fiber porous membranes.

7. The method of claim 1 including continuously flowing said liquid along said liquid flow path and continuously flowing said pressurized dense carbon dioxide along said carbon dioxide flow path.

8. The method of claim 1 including contacting said liquid and said dense carbon dioxide for a period sufficient to sterilize said liquid.

9. The method of claim 1 including contacting said liquid and said dense carbon dioxide for a period sufficient to inactivate an enzyme in said liquid.

10. Apparatus for preserving liquids by exposure of the liquids to pressurized dense carbon dioxide comprising:

a membrane contractor having a liquid flow path and a pressurized dense carbon dioxide flow path therein, said flow paths being separated from each other by porous membrane having pores which enable contact of a liquid flowing in said liquid flow path with pressurized dense carbon dioxide flowing in the carbon dioxide flow path,

a liquid pressurizing pump having an outlet communicated with said membrane contactor to direct liquid into said liquid flow path, and

a pressurized dense carbon dioxide recirculation pump having an inlet communicated with said membrane contactor to receive pressurized dense carbon dioxide which flows out of said carbon dioxide flow path and having an outlet communicated with said membrane contactor to return the pressurized dense carbon dioxide to said pressurized dense carbon dioxide flow path.

11. The apparatus of claim 10 wherein said membrane contactor includes a shell and a plurality of hollow fiber porous membranes extending in a generally parallel direction within said shell, and wherein one of said flow paths extends through lumen regions of said hollow fiber porous membranes and the other of said flow paths extends along exterior surfaces of said hollow fiber porous membranes.

12. The apparatus of claim 10 further including a first receiver tank having an inlet communicated with said membrane contactor to receive liquid from said liquid flow path, further including a pressure equalizing flow conduit communicating said dense carbon dioxide flow path with said first receiver tank.

13. The apparatus of claim 12 further including a second receiver tank having an inlet communicated with said first receiver tank to receive liquid therefrom through a pressure reducer.

14. The apparatus of claim 13 further including a liquid carbon dioxide storage tank, means for releasing carbon dioxide from said storage tank to said carbon dioxide flow path to maintain a particular operating pressure therein, and a compressor recovering low pressure carbon dioxide from said second receiver tank and which liquefies the recovered carbon dioxide, said compressor having an outlet communicated with said liquid carbon dioxide storage tank.

15. The apparatus of claim 10 wherein said membrane contactor includes a tubular shell and a plurality of substantially parallel hollow fiber porous membranes extending in a generally axial direction therein and wherein one of said flow paths extends through lumen regions of said hollow fiber porous membranes and the other of said flow paths extends along exterior surfaces of said hollow fiber porous membranes further including:

a first receiver tank having an inlet communicated with said membrane contactor to receive liquid from said liquid flow path,

a pressure equalizing flow conduit communicating said dense carbon dioxide flow path with said first receiver tank, and

a second receiver tank having an inlet communicated with said first receiver tank to receive treated liquid therefrom through a pressure reducer.

16. A method for sterilizing a liquid by exposure of the liquid to pressurized dense carbon dioxide comprising the steps of:

directing a flow of said liquid along a liquid flow path which extends along a first surface of a porous membrane and directing a flow of said pressurized dense carbon dioxide along a separate carbon dioxide flow path which extends along an opposite surface of said porous membrane including contacting said liquid and pressurized dense carbon dioxide at pores in said membrane, and

recirculating said flow of pressurized dense carbon dioxide through said carbon dioxide flow path including maintaining the pressurized dense carbon dioxide flow in the pressurized dense condition throughout the recirculating thereof.

17. Apparatus for sterilizing liquids by exposure of the liquids to pressurized dense carbon dioxide comprising:

a membrane contactor having a liquid flow path and a pressurized dense carbon dioxide flow path therein, said flow paths being separated from each other by porous membrane having pores which enable contact of a liquid flowing in said liquid flow path with pressurized dense carbon dioxide flowing in the carbon dioxide flow path,

a liquid pressurizing pump having an outlet communicated with said membrane contactor to direct liquid into said liquid flow path, and

a pressurize dense carbon dioxide recirculating pump having an inlet communicated with said membrane contactor to receive pressurized dense carbon dioxide which flows out of said carbon dioxide flow path and having an outlet communicated with said membrane contactor to return the pressurized dense carbon dioxide to said pressurized dense carbon dioxide flow path.

18. A method for sterilizing a liquid by exposure of the liquid to pressurized dense carbon dioxide, which liquid contains at least one constituent which is soluble in said pressurized dense carbon dioxide, comprising the steps of:

directing a flow of said liquid along a liquid flow path which extends along a first surface of a porous membrane and directing said pressurized dense carbon dioxide to an opposite surface of said porous membrane including contacting said liquid and pressurized dense carbon dioxide at pores in said membrane to sterilize said liquid and to saturate said pressurized dense carbon dioxide with said soluble constituent of said liquid, and

maintaining the pressurized dense carbon dioxide at said opposite side of said porous membrane in the saturated condition during continued sterilization of said flow of liquid.