OZONE TREATMENT OF LIQUID FOODSTUFF

• US 20090263548A1
• Filed: 05/21/2009
• Published: 10/22/2009
• Est. Priority Date: 11/30/2006
• Status: Abandoned Application

• Current Assignee: Pastair AB
• Original Assignee: Pastair AB
• Inventors: Sjoholm, Johan
• Application Number:
  US12/470,025
• Publication Number:
  US 20090263548A1
• Time in Patent Office: Days
• US Class Current: 426/317
• CPC Class Codes: A23C 3/085 Inorganic compounds, e.g. lactoperoxidase - H2O2 systems
• CPC Class Codes: A23L 2/44 by adding preservatives
• CPC Class Codes: A23L 3/3409 in the form of gases, e.g. fumigation; Compositions or apparatus therefor
• CPC Class Codes: A23L 3/358 Inorganic compounds
• CPC Class Codes: A23V 2002/00 Food compositions, function of food ingredients or processes for food or foodstuffs
• CPC Class Codes: A23V 2200/10 Preserving against microbes
• CPC Class Codes: A23V 2250/128 Ozone
• CPC Class Codes: A61L 2/202 Ozone
• CPC Class Codes: C02F 1/78 with ozone C02F1/4672 takes precedence

Abstract

The present invention relates to a method for inhibiting bacterial growth in liquid media by means of ozone containing gas flow, whereby a liquid medium at ambient temperature is passed by a finely divided gas stream containing ozone, the liquid medium is passed to dwell time space while being mixed to provide complete mixing between liquid and ozone, whereupon the liquid medium is degassed to eliminate excess of ozone dissolved therein.

Claims

1. A method for inhibiting bacterial growth in a biological liquid media by means of ozone containing gas flow, whereby a biological liquid medium is passed by a finely divided gas stream containing ozone, whereby the ozone is distributed via a porous means providing ozone over a part of the pathway of the biological liquid medium being treated, whereby the amount of ozone is added at least 1 ppm of the liquid treated, the liquid medium is passes to a dwell time space while being mixed to provide complete mixing between liquid and ozone, whereby the dwell time of the ozone in the liquid is up to one minute, whereupon the liquid medium is degassed to eliminate excess of ozone dissolved therein.

2. The method according to claim 1, wherein the temperature of the biological liquid medium is ambient temperature.

3. The method according to claim 1, wherein the temperature of the biological liquid medium when milk is 4 to 15°

C., being ambient storage and transport temperature of milk.

4. The method according to claim 1, wherein the amount of ozone added is at least 3. 6. 24. 50, 75 or 100 ppm.

5. The method according to claim 4, wherein the amount of ozone added is 1 to 10 ppm.

6. The method according to claim 1, wherein the ozone is distributed into the liquid medium via a perforated inlet device at a pressure of less than 1 bar.

7. The method according to claim 1, wherein the ozone is distributed over an enlarged surface area to the liquid medium.

8. The method according to claim 1, wherein the dwell time space is tubular mixer having restricted mixing chambers.

9. The method according to claim 7, wherein the tubular mixer is a peristaltic pump.

10. The method according to claim 2, wherein the size of the ozone gas bubbles has a diameter of 0.5 to 5 μ

m.

11. The method according to claim 10, wherein the ozone gas bubbles have a diameter of 1 to 2 μ

m.

12. The method according to claim 1, wherein the dwell time is less than 30 sec. more preferably less than 20 sec. still more preferably less than 10 sec., still more preferably less than 5 sec.

13. The method according to claim 5, wherein the ozone amount is 3 to 6 ppm, and the dwell time is 6 to 7 seconds.

14. The method according to claim 1, wherein the degassing for eliminating excess ozone is carried out by applying a subpressure or vacuum.

15. The method according to claim 1, wherein the degassing for eliminating excess ozone is carried out by applying a vacuum, preferably at a reduced pressure of at least 10 mmHg (1.333 kPa).

16. The method according to claim 1, wherein the degassing for eliminating excess ozone is carried out by adding finely distributed nitrogen and/or carbon dioxide gas, while applying a subpressure.

17. The method according to claim 1, wherein a pre-treatment step is carried out prior to the treatment of the actual biological liquid according to one or more of claims 1-13 by having water passing the different steps of the method, while ozone treating such water.

18. The method according to claim 1, wherein a post-treatment step is carried out subsequent to cleansing operation of an apparatus in which the method of the present invention has been carried out according to claims 1-16, for the treatment of the actual biological liquid, by having water passing the different steps of the method, while ozone treating such water.

19. An apparatus for carrying out the method according to claim 1, where apparatus comprises a gas injection unit, a dwell time unit, and a degassing unit, whereby an ozone source is provided, preferably an ozone producing unit for an intermittent of continuous production of ozone, whereby a control unit is provided to control the process.

20. The apparatus according to claim 19, wherein the gas injection unit filter is made of a disposable material, as fluids treated may be very sensitive to contaminants.

21. The apparatus according to claim 19, wherein the gas injection unit further comprises a fluid meter and a controlling function to provide for an adequate amount of gas being provided.

22. The apparatus according to claim 19, wherein the injection site where the gas injection unit filter is introduced into a production line is designed to provide for the gas being introduced to become solved or mixed into the fluid to be treated

23. The apparatus according to claim 19, wherein the gas injection unit filter is present of a number of porous, ozone distributing fingers extending across a liquid flow passway.