Process and apparatus for treating food products with ozone

• US 6,162,477 A
• Filed: 02/04/1999
• Issued: 12/19/2000
• Est. Priority Date: 02/04/1998
• Status: Expired due to Fees

• Current Assignee: L'Air Liquide Societe Anonyme Pour L'Etude et L'Exploitation Des Procedes Georges Claude (L'Air Liquide SA)
• Original Assignee: L'Air Liquide Societe Anonyme Pour L'Etude et L'Exploitation Des Procedes Georges Claude (L'Air Liquide SA)
• Inventors: Le Royer, Sylvie, Crisinel, Pascal
• Primary Examiner(s): CANO, MILTON I
• Application Number:
  US09/244,654
• Time in Patent Office: 684 Days
• Field of Search: 426/253, 426/256, 426/312, 426/643, 426/644, 426/646, 426/647, 426/474, 426/488, 99/467, 99/477, 99/516
• US Class Current: 426/256
• CPC Class Codes: A23B 4/16 in the form of gases, e.g. fumigation; Compositions or apparatus therefor
• CPC Class Codes: A23B 4/24 Inorganic compounds
• CPC Class Codes: A23L 13/52 Comminuted, emulsified or processed products; Pastes; Reformed or compressed products from poultry meat
• CPC Class Codes: A23L 5/276 Treatment with inorganic compounds A23L5/273 takes precedence
• CPC Class Codes: A23L 5/49 Removing colour by chemical reaction, e.g. bleaching

Abstract

A process for decolorizing, sanitizing and deodorizing a food product with ozone. The food product and water are mixed to form an initial solution and supplied to a pumping device to pressurize the solution. An ozone containing gas is injected into the initial solution in order to allow the treatment of the food product, without the occurrence of liquid/gas demixing. The apparatus includes a pumping device for pressurizing the solution, a contactor into which the pressurized solution is fed, a source of ozone, and at least one injector for injecting ozone into the solution.

Claims

1. A process for treatment of a food product, comprising the steps of:

(i) premixing the product with water to form an initial solution;

(ii) injecting a treatment gas comprising ozone into the initial solution; and

(iii) contacting the initial solution under pressure with the treatment gas for a sufficient period of time to allow treatment of the food product without occurrence of liquid/gas demixing and to obtain a treatment solution.

2. The process according to claim 1, wherein the product is fish meat.

3. The process according to claim 2, wherein the product is fish meat obtained (1) by separating the meat from at least one of the bones and the heads of the fish or (2) after an operation of grinding fillets.

4. The process according to claim 1, wherein the product is butcher meat.

5. The process according to claim 4, wherein the butcher meat is obtained after an operation of separating the meat from the carcass.

6. The process according to claim 1, wherein the product is poultry meat.

7. The process according to claim 6, wherein the poultry meat is obtained after an operation of separating the meat from the carcass.

8. The process according to claim 1, wherein the product is fruit flesh or vegetable matter or a puree thereof.

9. The process according to claim 1, further comprising the step of washing the product, prior to said step of premixing, one or more times in an aqueous medium.

10. The process according to claim 1, further comprising, after the treatment, the step of draining the product from the solution resulting from the treatment and washing the product in an aqueous medium one or more times.

11. The process according to claim 1, wherein ozone is present in the product during the treatment in a dose between from 0.2 to 2 grams of ozone per kilogram of product.

12. The process according to claim 11, wherein the dose lies within the range going from 0.3 to 1 g/kg.

13. The process according to claim 12, wherein the dose lies within the range going from 0.4 to 0.9 g/kg.

14. The process according to claim 1, wherein said treatment gas mixture comprises ozone in an amount within the range going from 10 to 200 g/m³.

15. The process according to claim 14, wherein the amount of ozone in the treatment gas lies within the range going from 20 to 120 g/m³.

16. The process according to claim 15, wherein the amount of ozone in the treatment gas lies within the range going from 40 to 100 g/m³.

17. The process according to claim 1, wherein said initial solution satisfies a degree of dilution corresponding to one volume of product per 0.5 to 10 volumes of water.

18. The process according to claim 17, wherein the degree of dilution corresponds to one volume of product per 1 to 5 volumes of water.

19. The process according to claim 18, wherein the degree of dilution corresponds to one volume of product per 3 to 5 volumes of water.

20. The process according to claim 1, wherein the pressure during said contacting step lies within the range going from 0.1 to 10 bar relative.

21. The process according to claim 20, wherein the pressure range goes from 0.2 to 2 bar relative.

22. The process according to claim 1, wherein said initial solution comprises an organic acid.

23. The process according to claim 1, wherein said initial solution comprises a basic compound.

24. The process according to claim 1, further comprising the step of feeding said initial solution into a supply prior to said injecting step.

25. The process according to claim 1, further comprising the step of pressurizing the initial solution prior to said step of contacting the initial solution with ozone.

26. The process according to claim 25, further comprising the step of recycling all or part of the treatment solution to a point in the process prior to said pressurizing step so as to allow a new pass through said contacting step for treatment with said treatment gas comprising ozone.

27. The process according to claim 26, further comprising the step of temporarily storing the treatment solution, before it reaches the pressurizing step in a degassing column.

28. The process according to claim 25, wherein said pressurizing step is carried out with a pump.

29. The process according to claim 25, wherein said step of injecting the treatment gas comprising ozone into the initial solution occurs during at least one of:

between said premixing step and said pressurizing step;

between said pressurizing step and said contacting step; and

during said contacting step.

30. The process according to claim 29, further comprising the step of injecting the treatment gas into the initial solution at multiple locations during said contacting step.

31. The process according to claim 1, wherein said step of contacting said initial solution with the treatment gas occurs in a contactor.

32. The process according to claim 31, wherein said contactor is a liquid/gas static mixer.

33. The process according to claim 31, wherein said contactor is in the form of a tube reactor.

34. The process according to claim 33, wherein said tube reactor comprises a pipe following a non-straight path, an inlet for said initial solution and an outlet for the treated solution.

35. The process according to claim 34, further comprising the step of storing the treated solution from the outlet of said contactor or further processing the treated solution from the outlet of said reactor.

36. The process according to claim 34, wherein the pipe comprises, over all or part of the portion between the inlet and the outlet of the contactor, a structure formed by one or more circular or helical turns.

37. The process according to claim 31, further comprising the step of injecting the treatment gas into the initial solution at one or more points in the contactor.

38. The process according to claim 1, further comprising, after said contacting step, at least one of the steps of (1) storing and (2) further processing all or part of the treatment solution.

39. An apparatus for treating a food product comprising;

a) a supply of an initial solution comprising a premix of the food product and water;

b) a pumping device for pressurizing the initial solution provided by said supply;

c) a contactor into which the pressurized initial solution is fed and which is adapted to allow treatment of the food product with the treatment gas without occurrence of liquid/gas demixing;

d) a source of a treatment gas mixture comprising ozone; and

e) at least one injector for injecting the treatment gas mixture into the initial solution.

40. The apparatus according to claim 39, wherein said contactor is a liquid/gas static mixer.

41. The apparatus according to claim 39, wherein said contactor is in the form of a tube reactor comprising an inlet allowing said initial solution coming from the pumping device to enter and an outlet.

42. The apparatus according to claim 41, wherein said tube reactor comprises a pipe following a nonstraight path.

43. The apparatus according to claim 42, further comprising at least one of a device for storing the solution and an apparatus in which the solution may undergo an operation after said treatment, connected to said outlet of said tube reactor.

44. The apparatus according to claim 42, wherein the pipe comprises over all or part of the portion lying between the inlet and the outlet of the contactor, a structure comprising one or more circular or helical turns.

45. The apparatus according to claim 39, wherein said at least one injector is provided at one or simultaneously at several of the following locations:

between said initial supply and the pumping device;

between the pumping device and the contactor;

at one or more points in the contactor.