METHOD FOR THE CONTINUOUS COATING OF FOOD PRODUCTS, IN PARTICULAR FROZEN FOOD PRODUCTS, WITH CONTROLLED ROTOR HEATING

Abstract

A method for coating food products with a coating substance including: a step a) of supercooling the food products, by providing external frigories, to a temperature lower than the initial temperature of same, before contacting the food products with the coating substance, and subsequently, a step b) of contacting the supercooled food products obtained in step a) with the coating substance. In step b): (i) the supercooled food products are contacted with the coating substance in a treatment chamber, (ii) the food products are stirred by a motorised mechanised system, including at least one stirring member, internal to the treatment chamber, (iii) the at least one stirring member is heated, and the intensity of the heating is adjusted, without excess heating, so as to avoid the accumulation of materials on the stirring member.

Claims

1-17. (canceled)

18. A method for coating food products with a coating substance, comprising: a step a) of supercooling the food products, by providing external frigories, to a temperature lower than the initial temperature of same, before contacting the food products with the coating substance, and subsequently a step b) of contacting the supercooled food products obtained in step a) with the coating substance, the coating around the products being formed at this step by the freezing of said coating substance under only the action of the transfer of frigories from the food products to the coating substance, in other words without providing external frigories, characterised in that in step b): the supercooled food products are contacted with the coating substance in a treatment chamber, the food products are stirred by means of a motorised mechanised system, comprising at least one stirring member, internal to said treatment chamber, movable with respect to said treatment chamber, said at least one stirring member is heated, and the intensity of the heating is adjusted without excess heating, so that the distribution of the coating substance around the food products is made uniform and/or to avoid the accumulation of material on said stirring member, while ensuring the coating around the food products by the freezing of the coating substance under the action of the transfer of frigories from the food products to the coating substance.

19. The method according to claim 18, wherein said at least one stirring member is a rotor.

20. The method according to claim 18, wherein said motorised mechanised system comprises two stirring members formed by two juxtaposed contrarotating rotors.

21. The method according to claim 20, wherein said at least one rotor, where necessary each of the two contrarotating rotors, comprises radial members distributed along the rotor and configured so as to ensure the advance of the material along said treatment chamber during rotating of the rotor or, if necessary, during rotating of the contrarotating rotors.

22. The method according to claim 18, wherein the heating of the stirring member is electrical induction heating or resistive heating.

23. The method according to claim 22, wherein the heating of the stirring member is an electrical heating and wherein the power is controlled by pulse-width modulation, and the step of adjusting the intensity of heating is carried out by modifying the duty cycle of the pulse-width modulation power control.

24. The method according to claim 22, wherein the stirring member is a rotor, and wherein the electrical circuit for implementing the electrical heating comprises at least one portion embarked on the rotor, the embarked portion having, in particular, one or more electrical resistances, and a portion rigidly attached to the frame of the treatment chamber, connected to the electrical power source, sliding electrical contacts ensuring the electrical connection between the two portions of the electrical circuit, which can move with respect to one another.

25. The method according to claim 18, wherein the freezing of the coating substance around the food products is partial at the end of step b), the method comprising a step c) where the coated products obtained in step b) are provided with external frigories until total freezing of the coating substance is obtained forming the coating around the food products.

26. The method according to claim 18, wherein the heating of the stirring member is obtained by heat exchange between a heat transfer fluid and said stirring member.

27. The method according to claim 26, wherein a step of adjusting the intensity of heating is carried out by increasing or reducing the temperature of the heat transfer fluid, before it exchanges heat with said stirring member, and/or increasing or reducing the flow rate of heat transfer fluid arriving at said at least one stirring member.

28. The method according to claim 18, wherein the initial temperature of the products corresponds to a frozen state, for example being between 20 C. and 10 C.

29. The method according to claim 18, wherein the temperature of the supercooled food products at the end of step b) is between 65 C. and 25 C. and wherein the temperature of the coating substance before being contacted with the supercooled products is greater than 0 C., such as for example at ambient temperature.

30. The method according to claim 18, wherein the provision of external frigories in step a) and/or step c) is carried out by injection of a cryogenic fluid and the cryogenic fluid is directly contacted with the food products of step a), and/or with the coated food products of step c).

31. The method according to claim 18, for production capacities greater than 1 tonne/hour of coated food products, for example greater than 2 tonnes/hour, and for which said at least one stirring member is heated, and the intensity of the heating is adjusted, without excess heating, at least so as to avoid the accumulation of material on said stirring member.

32. The method according to claim 18, for production capacities less than 1 tonne/hour of coated food products, for example less than 500 kg per hour, and for which said at least one stirring member is heated, and the intensity of the heating is adjusted, without excess heating, at least so that the distribution of the coating substance around the food products is uniform.

33. The method according to claim 18, wherein the food products are selected from the group consisting of vegetables, legumes, meat, cereals, fruits, fish and combinations thereof.

34. The method according to claim 18, wherein steps a) and b), or even if necessary, c) are carried out continuously.

Description

DESCRIPTION OF THE FIGURES

[0047] The invention will be better understood on reading the accompanying description of the attached drawings, of which:

[0048] FIG. 1 is a view of a facility suitable for implementing the coating method according to the invention,

[0049] FIG. 2 is a view from above of the unit for coating and contacting the coating substance, of the facility of FIG. 1, which comprises an advancing and stirring system with two contrarotating rotors,

[0050] FIG. 3 is a schematic view of the shaft of a rotor of the advancing system of FIG. 2, which comprises in turn an electrical heating circuit with an assembly of electrical resistances, and

[0051] FIG. 4 is a graph of the electrical voltage as a function of time, illustrating the power control of the electrical circuit by pulse-width modulation.

DETAILED DESCRIPTION

[0052] FIG. 1 also illustrates (by way of non-limiting example) a coating facility 1 suitable for implementing the method for coating food products P with a coating substance Se, according to the invention by implementing steps a) and b) as described above. This facility 1 comprises, successively, in the direction of treatment of products, a supercooling unit 3 and a unit 4 for coating and contacting the coating substance.

[0053] The food products P are supplied continuously (or discontinuously) into the supercooling unit 3.

[0054] The supercooling of step a) obtained by providing external frigories on the food products P, with the injection of cryogenic fluid (for example liquid nitrogen or CO.sub.2) in the super cooling unit 3 at one or more injection points.

[0055] The flow of the cryogenic fluid is controlled in order to obtain the determined temperature (for example 35 C.) of the supercooled products at the end of step a) which is higher than 65 C. and lower than 25 C., at the outlet of the supercooling unit 3. This control can be implemented by means of a proportional valve V.sub.N.

[0056] The supercooled products, coming from step a) continuously (or discontinuously) supplying the input of the unit 4 for coating and contacting the coating substance, in particular by gravity.

[0057] This coating unit 4 enables the implementation of step b) of the coating method, and comprises, for this purpose: [0058] a treatment chamber 40, forming a cradle for an advancing and stirring system, [0059] the advancing and stirring system which comprises two contrarotating rotors 41a, 41b, [0060] an injection system 42 for injecting the coating substance Se into the treatment chamber 40 of defined length, [0061] a length of the chamber (after the injection system 42) in order to allow the crusting of the coating substance Se, in other words without coating substance injection.

[0062] Each of the rotors comprises a shaft 43, in particular substantially cylindrical, along which members 44 are distributed, substantially radially. These members 44 are distributed along the length of the shaft following a helical path, and close to one another. During rotation of the rotor 41a or 41b, the members 44 enable stirring of the food products P. Their arrangement also allows the products to be pushed in a manner similar to an Archimedes' screw.

[0063] By rotating the rotors 41a and 41b in opposite directions, it is possible to cause the advance of the food products P along the treatment chamber 40, from the inlet to an outlet, and as illustrated by the double arrow of FIG. 2.

[0064] Over the first portion of the path, the coating substance Se is continuously injected at a plurality of injection points along the treatment chamber 40 by means of the system 42. The coating substance may be at ambient temperature, but in all cases higher than 0 C. The flow rate of the coating substance Se can be controlled by a proportional control valve V.sub.Se, as a function of the desired proportion of coating substance Se and of the flow rate of the food products P. The coating substance Se comes into contact with the supercooled food products in the enclosure 40: the coating is then at least partially crusted by transfer of frigories from the food products to the coating substance, in other words without supplying external frigories (i.e. without injecting cryogenic fluid into the chamber 40) and this over the length of the chamber 40 left free of the system 42.

[0065] Heating the Rotors

[0066] Notably, and according to the invention, and during the implementation of step b), the rotors 41a and 41b are positively heated in order to limit the transfer of frigories onto the shaft 43 and the members 44 of rotors 41a and 41b. The sufficient quantity of energy necessary for stopping the accumulation of the coating substance Se on the rotors 41a and 41b and their radial members 44 is thus provided, and/or again for slowing the freezing of the coating substance, but without excess heating under penalty of no longer obtaining the (at least partial) freezing of the coating substance which must result from step b).

[0067] Particular attention is therefore paid to controlling the intensity of heating sufficiently finely to achieve this objective; in the case of electrical (resistive) heating it has been possible to finely control the intensity of heating using power control by PWM (Pulse Width Modulation).

[0068] Such a control is illustrated by the graph of FIG. 4 which illustrates this power control, and more particularly the voltage U, as a function of time. The heating is controlled by a voltage pulse of width T, at each time period T. The duty cycle (in percent) is

[00001]$=\frac{100.Math..Math.T}{T}.$

[0069] By reducing the duty cycle of the PWM control, the heating intensity is reduced. By increasing the duty cycle of the PWM control, the heating intensity is increased. This duty cycle is adjusted to each production campaign in order to prevent the accumulation of the coating substance Se, and without excess heating as explained above. FIG. 4 illustrates the internal electrical heating circuit of the shaft 43 of each rotor 41a or 41 b which comprises an assembly of electrical resistances 45, mounted to rotate with the shaft 43 of the rotor. The electrical circuit comprises sliding electrical contacts 46, between the rotating part of the circuit embarked on the shaft 43 and the stationary part of the circuit connected to the electrical power source.

REFERENCE SIGNS

[0070] 1. Coating facility [0071] 3. Supercooling unit, [0072] 4. Unit for coating and contacting the coating substance, [0073] 40. Treatment chamber, [0074] 41a, 41b. Contrarotating rotors, [0075] 42. System for injecting the coating substance, [0076] 43. Shafts (rotors), [0077] 44. Radial members (rotors), [0078] 45. Electrical resistances (rotor heating), [0079] 46. Sliding electrical contacts. [0080] N.sub.2. Cryogenic liquid, [0081] Se. Coating substance, [0082] P. Food products, [0083] Tp. Temperature of the food products, [0084] V.sub.N. Valve for controlling flow of the cryogenic fluid, [0085] V Valve for controlling flow of the coating substance, [0086] U. Supply voltage of the electrical heating circuits inside the rotors.