SYSTEM AND METHOD FOR THE PREPARATION OF A TEXTURIZED NON-MEAT FOOD PRODUCT
20210345642 · 2021-11-11
Inventors
- Youcef Ait Bouziad (Echandens, CH)
- Jean-Marc Flick (Pomy, CH)
- Sheldon Fernandes (La Tour-de-Peilz, CH)
Cpc classification
International classification
Abstract
The invention relates to a food system (100) for preparing a texturized non-meat food product from a dehydrated powder product with the appearance and the texture of meat, the system comprising: —a processing chamber (10) receiving the dehydrated food product, hydrating and structuring at least part of it, and extruding it into a mass of a certain shape; —driving means (20) driving in rotation primary and secondary processing tools (110, 111) within the processing chamber (10) for hydrating, structuring and extruding the mass of food product; —a fluid reservoir (30) supplying a fluid into the processing chamber for hydrating the food product and creating a food mass; such that the processing chamber (10) comprises three sequential sub-chambers: —a mixing sub-chamber (12) comprising a primary processing tool (110) for hydrating, optionally heating, homogenizing and/or structuring the dehydrated food product or at least part of it into a food mass in batch mode; wherein the volume of the mixing sub-chamber (12) is larger than the volume of the food product prepared in it, so that the mixture of fluid and dehydrated food product is processed in free surface flow regime; —an extrusion sub-chamber (13) comprising a secondary processing tool (111) to optionally heat and expel the food mass from the mixing sub-chamber (12) and push it to the next sub-chamber in continuous mode, the extrusion sub-chamber (13) operating in pressurized flow regime, when activated, emptying at least part of the content of the mixing sub-chamber (12); —a cooled down die sub-chamber (14) to shape the food mass into a certain cross-sectional profile; whe the temperature in the three sequential sub-chambers (12, 13, 14) is independently controlled by distinct thermal sensing means arranged in each one of the sub-chambers, the sub-chambers (12, 13, 14) being further thermally isolated between them; and where the rotational speed and/or direction of the primary and secondary processing tools (110, 111) in the mixing sub-chamber (12) and in the extrusion sub-chamber (13), respectively, are independently controlled, so as to differently structure by heating and/or shear stress the food material in each of the sub-chambers (12, 13, 14). The invention further relates to a method for preparing a food product from a dehydrated powder product in a food system as the one described.
Claims
1. Food system for preparing a texturized non-meat food product from a dehydrated powder product with the appearance and the texture of meat, the system comprising: a processing chamber receiving the dehydrated food product, hydrating and structuring at least part of it, and extruding it into a mass of a certain shape; a driving method driving in rotation primary and secondary processing tools within the processing chamber for hydrating, structuring and extruding the mass of food product; a fluid reservoir supplying a fluid into the processing chamber for hydrating the food product and creating a food mass; the processing chamber comprises three sequential sub-chambers: a mixing sub-chamber comprising a primary processing tool for hydrating, optionally heating, homogenizing and/or structuring the dehydrated food product or at least part of it into a food mass in batch mode; wherein the volume of the mixing sub-chamber is larger than the volume of the food product prepared in it, so that the mixture of fluid and dehydrated food product is processed in free surface flow regime; an extrusion sub-chamber comprising a secondary processing tool to optionally heat and expel the food mass from the mixing sub-chamber and push it to the next sub-chamber in continuous mode, the extrusion sub-chamber operating in pressurized flow regime, when activated, emptying at least part of the content of the mixing sub-chamber; a cooled down die sub-chamber to shape the food mass into a certain cross-sectional profile; the temperature in the three sequential sub-chambers is independently controlled by distinct thermal sensor arranged in each one of the sub-chambers, the sub-chambers being further thermally isolated between them; and wherein the rotational speed and/or direction of the primary and secondary processing tools in the mixing sub-chamber and in the extrusion sub-chamber, respectively, are independently controlled, so as to differently structure by heating and/or shear stress the food material in each of the sub-chambers.
2. Food system according to claim 1 further comprising a control unit governing one or a plurality of: fluid dosing from the fluid reservoir into the processing chamber; ratio of fluid to be mixed with the food product; speed and/or torque and/or rotational direction of the driving method; temperature in each of the three sequential sub-chambers; dosing of food product into the processing chamber; processing time.
3. Food system according to claim 2 wherein the control unit is connectable to a database providing recipe preparation information for the food product prepared in the system comprising preparation steps and/or triggering values, as a function of the dehydrated powder product.
4. Food system according to claim 1 wherein the driving method comprises a motor with electronic feedback of its current to determine the motor torque and thus the food product viscosity in the mixing sub-chamber in order to use this value as triggering value to expel the prepared food product mass into the extrusion sub-chamber.
5. Food system according to claim 1 wherein the driving method comprises a motor with electronic feedback of its current to determine the motor torque and thus the food product shear stress in the extrusion sub-chamber in order to use this value to control the rotational speed of the secondary processing tool to increase or decrease the flow rate of the expelled food product mass into the die sub-chamber.
6. Food system according to claim 1 wherein the mixing sub-chamber and the extrusion sub-chamber are configured having substantially cylindrical shapes.
7. Food system according to claim 6 wherein the diameter of the extrusion sub-chamber is smaller than the diameter of the mixing sub-chamber in order to limit the extrusion forces of the food product mass in the extrusion sub-chamber.
8. Food system according to claim 1 wherein the dehydrated powder product is of vegetable protein composition.
9. Food system according to claim 8 wherein the vegetable protein composition comprises flavouring ingredients.
10. Food system according to claim 8 wherein the vegetable protein composition comprises a portion of starch and/or flour.
11. Food system according to claim 1 wherein the die sub-chamber comprises a shaping element that is interchangeable in order to provide different shapes for the food product delivered.
12. Food system according to claim 1 further comprising cutting means adjustable to provide different lengths of the food product.
13. Food system according to claim 1 wherein the primary and secondary processing tools are arranged along one single axis, the rotational speed and direction of which is adjustable, such that the primary processing tool arranged in the mixing sub-chamber comprises one or a plurality of mixing or kneading blades and at least a scrapping blade, and the secondary processing tool comprises a mono-screw extruder, helically shaped.
14. Method for preparing a food product from a dehydrated powder product in a food system for preparing a texturized non-meat food product from a dehydrated powder product with the appearance and the texture of meat, the system comprising a processing chamber receiving the dehydrated food product, hydrating and structuring at least part of it, and extruding it into a mass of a certain shape, a driving method driving in rotation primary and secondary processing tools within the processing chamber for hydrating, structuring and extruding the mass of food product, a fluid reservoir supplying a fluid into the processing chamber for hydrating the food product and creating a food mass, the processing chamber comprises three sequential sub-chambers, a mixing sub-chamber comprising a primary processing tool for hydrating, optionally heating, homogenizing and/or structuring the dehydrated food product or at least part of it into a food mass in batch mode; wherein the volume of the mixing sub-chamber is larger than the volume of the food product prepared in it, so that the mixture of fluid and dehydrated food product is processed in free surface flow regime, an extrusion sub-chamber comprising a secondary processing tool to optionally heat and expel the food mass from the mixing sub-chamber and push it to the next sub-chamber in continuous mode, the extrusion sub-chamber operating in pressurized flow regime, when activated, emptying at least part of the content of the mixing sub-chamber, a cooled down die sub-chamber to shape the food mass into a certain cross-sectional profile, the temperature in the three sequential sub-chambers is independently controlled by distinct thermal sensor arranged in each one of the sub-chambers, the sub-chambers being further thermally isolated between them, and wherein the rotational speed and/or direction of the primary and secondary processing tools in the mixing sub-chamber and in the extrusion sub-chamber, respectively, are independently controlled, so as to differently structure by heating and/or shear stress the food material in each of the sub-chambers, the method comprising the following steps: hydrating and mixing the dehydrated powder; heating the homogenized food mass in the extrusion sub-chamber to the temperature or over the temperature of phase-change for gelation and denaturation of the proteins of the food mass in the extrusion sub-chamber; and decreasing actively and/or passively the temperature of the proteins food mass to freeze the proteins' structure, form and shape along a certain direction, in the die sub-chamber.
15. Method for preparing a food product according to claim 14 wherein the first step takes place while the primary and secondary processing tools rotate in a certain direction, while the second and third steps occur when the primary and secondary processing tools have reversed their direction of rotation.
16. Method for preparing a food product according to claim 14 wherein the heating means are activated or deactivated separately on each sub-chamber, depending if the product needs to be structured via heating and/or shearing.
17. Method for preparing a food product according to claim 14 wherein the temperature and/or viscosity of the food mass in each of the sub-chambers is independently controlled.
18. Method for preparing a food product according to claim 14 wherein the preparation of the food product is done in batch mode in the mixing sub-chamber and sent in continuous rom the extrusion sub-chamber to the die sub-chamber.
19. Method for preparing a food product according to claim 14 wherein the temperature of the food mass in the mixing sub-chamber ranges from ambient temperature to 80° C., the temperature in the extrusion sub-chamber ranges from ambient to 150° C., and the temperature in the die sub-chamber ranges from ambient to 100° C.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0028] Further features, advantages and objects of the present invention will become apparent for a skilled person when reading the following detailed description of non-limiting embodiments of the present invention, when taken in conjunction with the appended drawings, in which:
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DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS
[0040] The object of the present invention is a food system 100 (as represented in
[0041] Looking at
[0042] The first mixing sub-chamber 12 receives the dehydrated food product, adds a fluid (typically water) to it from a fluid reservoir in the system 100, and homogenizes or structures the food product into a food mass by rotation of a primary processing tool 110 inside this sub-chamber 12. Optionally, and depending on the food product and its processing, it can be further heated in the mixing sub-chamber 12: heating is done preferably by means of an electric resistance embedded in the walls of the mixing sub-chamber 12. The temperature of the food mass (heated or not) inside the mixing sub-chamber 12 is controlled by a thermal probe 25. The volume of the mixing sub-chamber 12 is larger than the volume of the food product prepared in it, so that the mixture of fluid and dehydrated food product is processed in free surface flow regime, such that the food mass inside is subjected to zero perpendicular normal stress and zero parallel shear stress.
[0043] It is essential in the system of the invention that it works in batch mode, meaning that there is a certain time needed to prepare the food mass in the mixing sub-chamber 12. Contrary to the processes in the known prior art, where the food products are manufactured in continuous, the process in the system of the invention needs time to prepare a certain quantity of product and to deliver the final texturized non-meat food product. The process requires longer time than an industrial process, but the system of the invention is much more compact and can therefore be used for in-home applications.
[0044] After the first mixing sub-chamber 12, the product mass goes into a further extrusion sub-chamber 13: the extrusion sub-chamber 13 is provided with a rotating secondary processing tool 111 inside, that pushes the food mass into the following sub-chamber, the die sub-chamber 14. Contrary to the mixing sub-chamber regime of free flow surface (not pressurized) the extrusion sub-chamber 14 works in a pressurized flow regime, where the food product mass inside of it is under pressure, and so is pushed in continuous mode into the following sub-chamber, the die sub-chamber 14. As such, when the extrusion sub-chamber 13 is activated, it empties in continuous all or at least part of the content of the mixing sub-chamber 12, then processes it under pressure and sends it in continuous to the die sub-chamber 14. The extrusion sub-chamber 13 can also optionally heat the product inside, typically by an electric resistance embedded in the wall of the said sub-chamber 13.
[0045] In the embodiment shown in the Figures attached (particularly in
[0046] The final sub-chamber of the processing chamber 10 is the die sub-chamber 14, where the food product mass is shaped into a certain cross-sectional profile. The die sub-chamber 14 is cooled down either actively or passively. Passively means that the product is cooled down by passing through the die support mass 26, that is at ambient temperature, and is further cooled down when the product exits the die to the outside (see
[0047] In order to provide differential processing in each of the three sub-chambers 12, 13, 14 of the processing chamber 10, it is essential that the temperature in each of these chambers is controlled independently: in the configuration of the invention, distinct thermal sensing means are arranged in each one of these sub-chambers. In an exemplary embodiment represented in the attached Figures, there is a thermal probe 25 arranged in the mixing sub-chamber 12 and controlling the temperature of the product mass inside of it. Similarly, a distinct thermal probe 35 is arranged in the extrusion sub-chamber 13 to measure the temperature of the food mass inside this chamber. Another distinct thermal probe is arranged in the die sub-chamber 14 (though it is not shown in the Figures). In order to independently and properly control the temperature in each of the three sub-chambers, these sub-chambers are further isolated between them. Looking at
[0048] Moreover, the rotational speed and the direction of rotation of the primary and of the secondary processing tools, 110 and 111, respectively, in the respective mixing and extrusion sub-chambers, 12 and 13, are independently controlled: therefore, the food product mass in each of these sub-chambers can be structured differently, by heating and/or by shear stress.
[0049] The dehydrated food product, typically powder, is introduced in the mixing sub-chamber 13 through a powder feeding aperture 18, as represented in
[0050] The primary processing tool 110 comprises a plurality of mixing or kneading blades 15 and at least one scrapping blade 16. The blades 15, when rotating, mix and homogenize the food product mass. The scrapping blade 16 allows scrapping the mixture from the inner walls of the mixing sub-chamber 12, in order to create a mass of product that will be conveyed to the next sub-chamber, the extrusion sub-chamber 13. Inside the extrusion sub-chamber 13, the secondary processing tool 111 rotates and send in continuous the food product mass to the die sub-chamber 14. The secondary processing tool 111 typically comprises a single screw extruder 17 preferably with a helicoidal shape. The food mass in the extrusion sub-chamber 14 is subjected to pressure and sent to the next sub-chamber for being shaped in the die 27.
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[0052] The die sub-chamber 14 comprises a shaping element that is interchangeable in order to provide different shapes for the food product delivered. Cutting means, adjustable to provide different lengths of the food product, are further provided at the exit of the die sub-chamber 14 (not represented in the Figures).
[0053] Looking at
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[0055] In the system of the invention, there is provided electronic feedback of the motor current to the control unit in order to determine the motor torque and thus be able to know the food product viscosity in the mixing sub-chamber 12: this value is used as triggering value to expel the prepared food product mass from the mixing sub-chamber 12 and into the extrusion sub-chamber 13. Furthermore, electronic feedback of the motor current is provided in the system too, to determine the motor torque and thus the food product shear stress in the extrusion sub-chamber 13 in order to use this value to control the rotational speed of the secondary processing tool 111 in the extrusion sub-chamber 13 to increase or decrease the flow rate of the expelled food product mass into the die sub-chamber 14.
[0056] Depending on the type of food product processed and on the recipe, the parameters are different and so the control unit 40 manages the product processing accordingly. Preferably, the control unit 40 is connectable to a database providing recipe preparation information for the food product prepared in the system comprising preparation steps and/or triggering values, as a function of the dehydrated powder product (powder) introduced.
[0057] Preferably, the mixing sub-chamber 12 and the extrusion sub-chamber 13 are configured having substantially cylindrical shapes. The diameter of the extrusion sub-chamber 13 is smaller than the diameter of the mixing sub-chamber 12 in order to limit the extrusion forces of the food product mass in the extrusion sub-chamber 13; the extrusion process generates a certain pressure in the food mass in the extrusion sub-chamber 13, function of a given rotation speed and a given viscosity of the product.
[0058] The dehydrated powder product introduced in the mixing sub-chamber 12 can be of vegetable protein composition, comprising a portion of starch and/or flour, and can further comprise flavoring ingredients. The dehydrated powder product can be provided in a cartridge or recipient that will be poured through the funnel 19 and into the aperture 18. When provided in a cartridge or recipient, it will typically comprise identification means that will be read by reading means in the system: processing parameters will be then sent to the control unit so the process is managed according to these. Another alternative is that the consumer enters manually the recipe number or code reported in the powder pack or cartridge or recipient, via an interface on the system or smartphone. Another alternative is that the consumer directly pours the powder product desired into the mixing sub-chamber 13.
[0059] Another option is to add into the mixing sub-chamber 12 an already pre-mixed mixture (processed and prepared outside the system 100): this way, the batch mode and the extra timing needed for processing will be reduced significantly. Yet another option of the system of the invention is to process a certain food mass in the mixing sub-chamber 12, and leave it there until the moment when it will be processed in the extrusion and die sub-chambers 13, 14, also with the aim of limiting the overall processing time in the system. It is therefore clear that there are two processes in the processing chamber 10, conceptually different: a batch mode processing of the food mass in the mixing sub-chamber 12, with the processing tools rotating in a certain direction, and a continuous mode of processing and sending the prepared mass from the extrusion into the die sub-chamber, 13 and 14 respectively, when the processing tools have reversed their direction of rotation.
[0060] According to a second aspect, the invention also relates to a method for preparing a food product from a dehydrated powder product in a food system 100 as the one described. The method of the invention comprises the following steps: [0061] hydrating and mixing the dehydrated powder, optionally pre-heating the hydrated and structured food mass in the mixing sub-chamber 12; the mixture is preheated to a temperature below the structuration temperature of the proteins of the food mass, this being done by the processing of the mass through the primary processing tool 110, and the temperature can optionally be increased, if needed, by heating means on the said sub-chamber 12; [0062] the homogenized food mass in the extrusion sub-chamber 13 is heated to the temperature or over the temperature of the phase-change for gelation and denaturation of the proteins of the food mass in the extrusion sub-chamber 13, either by the processing of the mass through the secondary processing tool 111 or, in case the temperature has to be increased, by heating means on the said sub-chamber 13; [0063] decreasing actively and/or passively the temperature of the proteins food mass to freeze the proteins' structure, form and shape along a certain direction, in the die sub-chamber 14.
[0064] In the method of the invention, the first step (hydrating and mixing the dehydrated powder and preparing the mixture in the mixing sub-chamber 12) takes place while the primary and secondary processing tools, 110 and 111, rotate in a certain direction (typically, in counter clockwise direction), the extrusion sub-chamber 13 and thus the die sub-chamber 14 not being activated. For the second and third steps (the food mass is processed in the extrusion sub-chamber 13 and then goes through the die sub-chamber 14 for shaping), these sub-chambers 13 and 14 are activated, the primary and secondary processing tools, 110 and 111, having reversed their direction of rotation into clockwise direction, typically.
[0065] In the method of the invention, and in order to independently process the food mass in each sub-chamber, heating means can be activated or deactivated separately on the mixing sub-chamber and/or on the extrusion sub-chamber, depending if the product needs to be structured via heating and/or shearing. Particularly, the temperature and the viscosity of the food mass in each of the sub-chambers 12, 13 and 14 is independently controlled, such that the product does not go to the next sub-chamber until a certain value of temperature and/or viscosity has been reached in the previous sub-chamber. The control unit receives feedback from the temperature probes and therefore manages the process accordingly, according to the recipe desired.
[0066] Method for preparing a food product according to any of claims 14-16 wherein the preparation of the food product is done in batch mode in the mixing sub-chamber 12, thus requiring a certain preparation time. When the food mass is ready, according to the desired parameters (typically temperature and speed and/or torque values of the primary processing tool 110), as managed by the control unit 40, it is sent to the next sub-chamber, the extrusion sub-chamber 13. There, the product is prepared under pressure, extruded, and once ready, as controlled by the control unit, typically receiving speed and torque values from the processing tool 111, it is sent in continuous into the die sub-chamber 14, for the final shaping and delivery.
[0067] Even when depending on the product type and characteristics, the temperature of the food mass in the mixing sub-chamber 12 ranges from ambient temperature to 80° C., the temperature in the extrusion sub-chamber 13 ranges from ambient to 150° C., and the temperature in the die sub-chamber 14 ranges from ambient to 100° C.
[0068] Although the present invention has been described with reference to preferred embodiments thereof, many modifications and alternations may be made by a person having ordinary skill in the art without departing from the scope of this invention which is defined by the appended claims.