Brine solution set and method for in-line processing of food products

Abstract

To provide a method for in-line processing of food products that enhances the control of product characteristics of a coating material during the manufacture and the further life stages of the food products.SOLUTION: The present invention relates to a set of brine solutions for use in a method for in-line processing of food products, the method comprising the steps of a) co-extruding food dough into a flow of co-extruded food products having a protein-containing coating or a hybrid coating of a protein and a polymer, and b) subjecting the flow of co-extruded food products to a food product strengthening step. The food product strengthening step comprises the step of subjecting the flow of food products to a first brine solution comprising a salt solubilized in an aqueous medium, and a second brine solution comprising a buffer salt solubilized in an aqueous medium. The present invention further relates to a method for in-line processing of food products using the set of brine solutions of the present invention and a lactate salt comprising a brine solution.SELECTED DRAWING: None

Description

[Technical Field]

[0001] The present invention relates to a set of brine solutions and a method for in-line processing of food products using the set of brine solutions of the present invention. The present invention further relates to brine solutions having improved pH setting properties, a system for in-line processing of food products using the method of the present invention, and the use of the set of brine solutions of the present invention in a method for in-line processing of food products. [Background technology]

[0002] The co-extruded method for food production is generally known and is described, inter alia, in Dutch Patent NL6909339. This specification describes the coating of food dough strands with a proteinaceous, e.g., collagen, casing layer using co-extrusion. After extrusion, the coated strands are guided through a coagulation bath for strengthening purposes. Under the influence of the coagulation solution, the protein coagulates and / or precipitates, and the casing layer is strengthened. In this way, a food dough strand is formed that is at least partially coated with a strong proteinaceous, i.e., collagen-containing, casing-containing casing layer.

[0003] A drawback of known methods is that the properties of the casing material, and therefore the processability of the food product, can change during the production of a co-extruded food product stream, i.e., a stream of individual sausages, strands of food product, or a stream of connected sausages (head-tail connections). Changes in the properties of the casing material are difficult to predict. Furthermore, changes in the properties of the casing material are irreversible. Therefore, once the properties of the casing material change, the food product stream can no longer be processed to obtain a final food product, i.e., a sausage, of acceptable quality.

[0004] A particular drawback of known methods using proteins, or proteins containing viscous gelling agents, as casing materials for co-extrusion of elongated food products is the uncontrollable characteristics (particularly the surface condition) of the final food product. It has been observed that altering process settings after co-extrusion of the food dough strands and the casing material can irreversibly alter the properties of the protein casing material. Such alterations can include changes in the surface properties of the casing material that affect the surface smoothness of the food product, i.e., the "look and feel" of the food product. By altering post-co-extrusion process settings in subsequent processing steps, such as brining, separating, crimping, smoking, drying, packaging, cooking, and / or chilling, the resulting food product can uncontrollably change from the normally desired smooth, aesthetically pleasing, and consistent surface to a food product with an undesirable surface condition, such as a sticky, uneven, and / or dirty surface. Such uncontrollable and irreversible changes in surface properties may result in poorer processability of the food product stream, and as a result, the food product stream (or at least a portion of the food product stream) may even have to be discarded. [Prior art documents] [Patent documents]

[0005] [Patent Document 1] Dutch Patent Application Publication No. 6909339 Summary of the Invention [Problem to be solved by the invention]

[0006] In view of the above, there is a need for increased control over the production of co-extruded food products, and more particularly, increased control over the product properties of coating (e.g., casing) materials during the manufacturing and further life stages of the food product. [Means for solving the problem]

[0007] To this end, the present invention provides a set of brine solutions, including a first brine solution and a second brine solution, for use in a method for in-line processing of food products, comprising the steps of co-extruding a food dough into a co-extruded food product stream having a protein-containing coating or a protein-polymer hybrid coating, and subjecting the co-extruded food product stream to a food product fortification process, the food product fortification process comprising: i) subjecting the food product stream to a coating moisture content reduction process using a first brine solution, the first brine solution comprising a salt solubilized in an aqueous medium, and then ii) subjecting the food product stream to a coating pH fixation process using a second brine solution, the second brine solution comprising a buffer salt solubilized in an aqueous medium. It has been found that unexpected, irreversible changes in the processability and coating properties of co-extruded elongated food products are strongly dependent on the physical state of the protein or protein-containing hybrid coating. As a result, changes in coating properties, such as coating surface smoothness, can be controlled, i.e., prevented, by controlling the physical state of the protein. In particular, it has been found that by providing a brine solution set having coating moisture content reducing properties on one end and coating pH setting or buffering properties on the other end, not only can the pH of the brine solution be maintained over an extended period of time, but the pH of the coating of the food product stream can also be maintained during further processing of the food product stream, thus providing an improved method by which the physical state of proteins can be controlled in a more sustainable and reliable manner, i.e., significantly increasing the processability of the food product stream. DETAILED DESCRIPTION OF THE INVENTION

[0008] With respect to the physical state of a protein, it is noted that such physical state can include three types of physical states: a crystalline phase, a helical phase, and a random coil phase. It has been found that when a protein in a helical or crystalline form is converted to a protein having a random coil form, an irreversible change in coating properties is expected. Proteins comprising food product coatings containing proteins in a helical or crystalline form are characterized by a smooth, attractive appearance and / or a stable surface, whereas proteins comprising food product coatings containing proteins in a random coil form exhibit a more sticky, uneven, and / or dirty surface. Consequently, in certain embodiments of the methods of the present invention, the protein is in a helical and / or crystalline form.

[0009] In some embodiments of the present invention, during the process using the set of brine solutions of the present invention, the physical state of the protein may change between the helical and crystalline forms during subsequent food product processing steps, such as the heat treatment step and any post-heat treatment steps. Because either the helical or crystalline physical state of the protein has a positive effect on the coating properties of the food product, the actual state of the protein may change between these two states. However, it is particularly preferred that the physical state of the protein does not change after co-extrusion of the food product stream. Maintaining the same physical state of the protein during co-extrusion of the food product stream and any further processing steps is particularly advantageous in order to maintain the same product properties, such as surface smoothness, surface color, and cooking characteristics, of the resulting food product or the like. Furthermore, particularly good results are obtained with the protein in a crystalline form throughout the process using the set of brine solutions of the present invention. By providing a coating containing the protein in a crystalline form, the food product coating has the most optimal thermal stability, i.e., provides a product that can be partially or fully cooked without undesirable surface properties.

[0010] The protein of the present invention may be selected from the group consisting of edible proteins that are capable of forming a coating by gelation (aggregation and / or precipitation; whether in the presence of a coagulant) after coextrusion. Particularly preferred proteins include collagen.

[0011] The polymer included in the hybrid coating of the present invention can be selected from the group consisting of edible polymers that can be combined with the proteins present in the hybrid coating to form a coating. Preferably, the polymer is selected from the group consisting of polysaccharides. Preferred polymers can include alginate and / or cellulose.

[0012] The co-extruded food product stream may contain strands of co-extruded food products that still need to be separated into separate individual food products (e.g., sausages). The food product stream may contain intermediate forms of strands where the individual food products are still linked together (head-to-tail linked) to form a string of linked food products.

[0013] The first brine solution of the present invention preferably comprises a salt selected from the group consisting of edible salts such as sodium chloride. Preferably, the first brine solution consists essentially of solubilized salt in an aqueous medium.

[0014] In some embodiments of the invention, the first brine solution comprises a saturated salt solution. Alternately, the first brine solution may comprise at least 20% by weight salt, where weight percent is calculated based on the total weight of the brine solution. In preferred embodiments of the invention, the first brine solution may comprise at least 25% by weight salt, or preferably at least 30% by weight salt.

[0015] The second brine solution of the present invention preferably comprises a buffer salt selected from the group consisting of buffer salts having a pKa at 20°C of at least 2.5. In certain preferred embodiments, the buffer salt may be selected from the group consisting of buffer salts having a pKa at 20°C between 3.0 and 5.5. It has been found that by providing a second brine solution comprising a buffer salt having a pKa between 3.0 and 5.5, the pH of the brine solution can be maintained for a significantly longer period of time compared to a brine solution containing no buffer salt at all. Furthermore, the pH of the second brine solution can be maintained for an even longer period of time when the buffer salt is selected from the group consisting of buffer salts having a pKa at 20°C between 3.5 and 5.0.

[0016] In an embodiment of the present invention, the second brine solution may contain a buffer salt selected from the group consisting of lactate, acetate, phosphate, and carbonate. Preferred salts may include sodium and / or potassium salts such as sodium lactate, potassium lactate, sodium acetate, potassium acetate, disodium phosphate, dipotassium phosphate, sodium carbonate, and potassium carbonate. It is noted that the second brine solution of the present invention may contain a combination of two or more of the above salts.

[0017] In a further embodiment of the present invention, the amount of buffer salt included in the second brine solution of the present invention is selected to provide a second brine solution having a pH of at least 5.0. In particular, the second brine solution containing the buffer salt of the present invention can have a pH between 5.0 and 8.0. It has been found that by providing a second brine solution of at least 5.0, the physical state of proteins, such as collagen, can be more reliably controlled. Also, by providing a second brine solution having a pH of less than 8.0, the color of the final food product still complies with the predetermined desired color of the resulting final food product.

[0018] The amount of buffer salt can be selected so that the pH of the second brine solution of the present invention is within a predetermined range, although it is also possible to provide a second brine solution that includes a saturated salt solution. Alternatively, the second brine solution can include at least 30% by weight of salt, where the weight percentage is calculated based on the total weight of the brine solution. In a preferred embodiment of the present invention, the second brine solution can include between 40% and 60% by weight of salt.

[0019] When a lactate salt, such as sodium lactate or potassium lactate, is used as the buffer salt, the second brine solution may contain between 50% and 80% lactate by weight. In a preferred embodiment, the second brine solution may contain about 60% lactate by weight.

[0020] When a carbonate, such as sodium carbonate or potassium carbonate, is used as the buffer salt, the second brine solution may contain between 50% and 70% by weight of the carbonate. In a preferred embodiment, the second brine solution may contain about 60% by weight of the carbonate.

[0021] When a phosphate, such as disodium phosphate or dipotassium phosphate, is used as the buffer salt, the second brine solution may contain between 30% and 50% by weight of the phosphate. In particular, the second brine solution may contain about 40% by weight of the phosphate.

[0022] In a further embodiment of the present invention, the second brine solution may include a salt that is not a buffer salt, such as sodium chloride. While a second brine solution that includes only buffer salts is preferred, it is noted that a combination, i.e., a second brine solution that includes a buffer salt and a salt that is not a buffer salt, provides good results in controlling and maintaining the pH of the second brine solution over an extended period of time.

[0023] In another aspect, the present invention relates to a method for in-line processing of food products comprising the step of co-extruding a food dough into a stream of co-extruded food products having a protein-containing coating or a protein-polymer hybrid coating, wherein said method subsequently comprises the following successive steps:

[0024] a) subjecting the co-extruded food product stream to a food product fortification step, wherein said food product fortification step comprises subjecting the food product stream to a set of brine solutions; and b) heat treating the food product stream obtained in step a), wherein in step a) the set of brine solutions comprises the set of brine solutions of the present invention.

[0025] It has been found that by providing a consolidation step in which the moisture content of the coating and the pH of the coating are controlled and maintained by using a set of brine solutions of the present invention, the consolidation step can then be advantageously combined with a heat treatment step.

[0026] In preferred embodiments of the present invention, the heat treatment step of step b) may comprise a step in which the food product stream is subjected to two or more heat treatment steps. Such a single multiphase process step may comprise subjecting the food product stream to at least two heat treatment steps. However, further heat treatment steps may also be applied to the food product stream. For example, in a further preferred embodiment, the food product stream may be subjected to a first and a second heat treatment step, followed by a third heat treatment step. Furthermore, four or more subsequent heat treatment steps may also be applied. Typically, a single multiphase process step may be configured to contain about six heat treatment steps. It is noted that the configuration of the heat treatment steps of step b) will depend on the specific food product being produced and the production line design to which the method is applied. For example, for one product, the heat treatment process may include four heat treatment steps, such as drying, heating, partially cooking, and (fully) cooking, while for another product, the heat treatment process may include three heat treatment steps, where the product leaving the single multi-phase process step is only partially cooked.

[0027] The thermal treatment step of step b) may be selected from the group consisting of drying, heating, partially cooking, cooking, and cooling the food product stream.

[0028] As used herein, the term "drying" refers to a process step in which excess water or moisture is removed from the surface of a food product stream to prevent solidification of the food product coating and / or cooking.

[0029] As used herein, the term "heating" refers to a process step in which the coating solidifies even though the food dough is not cooked.

[0030] As used herein, the term "cooking in portions" refers to a process step in which the food dough is only partially cooked, i.e., resulting in a food product that is not yet readily edible, and which still needs to be cooked, for example, in a further subsequent multi-phase processing step or by the end consumer while preparing the food product for eating.

[0031] As used herein, the term "cooking" refers to a process step in which a food dough is cooked, resulting in an edible food product. An alternative term for a food product that has been subjected to a cooking step is a "fully cooked" food product.

[0032] As used herein, the term "cooling" refers to a process step in which the temperature of a food product is reduced using a cooling medium such as tap water or cold air, typically having a temperature of about 10°C to 15°C.

[0033] As used herein, the term "chilling" refers to a process step in which food products are subjected to a chilling medium, which is a medium (e.g., water) that is intentionally made colder.

[0034] As already mentioned, different combinations of two or more heat treatment steps can be used in the method of the invention depending on the specific characteristics of the food product to be obtained, the starting materials used to produce the food product, the design of the production line to which the method is applied, and other parameters. An example of such a combination may relate to a method in which a first heat treatment step comprises b.1) drying the food product stream and / or a second heat treatment step comprises b.2) at least partially cooking the food product stream. Another example of such a combination may relate to a method in which a first heat treatment step comprises bi) drying the food product stream, a second heat treatment step comprises b.ii) heating the food product stream, and / or a third heat treatment step comprises b.iii) at least partially cooking the food product stream.

[0035] It is noted that with regard to the process conditions of the heat treatment step of the present invention, the temperature may range from 50°C to 150°C, the relative humidity may range from 0% to 100%, and the air velocity may range from 1 m / s to 10 m / s.

[0036] In a preferred embodiment, the heat treatment step comprises drying the food product stream at a temperature between 50° C. and 80° C., preferably between 60° C. and 75° C. The relative humidity during drying of the food product stream may be up to 10%, preferably up to 5%.

[0037] With regard to heating the food product stream, the heat treatment step may involve a temperature between 60° C. and 90° C., preferably between 70° C. and 80° C. The relative humidity during heating of the food product stream may be between 15% and 40%, more preferably between 25% and 35%.

[0038] Partially cooking the food product stream may involve a temperature between 70° C. and 100° C., more preferably between 80° C. and 90° C. The relative humidity during partial cooking of the food product stream may be between 30% and 60%, preferably between 40% and 50%.

[0039] In a further embodiment, the heat treatment step comprises cooking the food product stream at a temperature between 70° C. and 100° C., preferably between 80° C. and 90° C. The relative humidity of the food product stream during cooking may be between 60% and 80%, more preferably between 65% and 75%.

[0040] The method of the present invention may further comprise the step of separating the strands of co-extruded food product into individual food products. As already mentioned above, the food product stream may comprise strands of co-extruded food product, and the method of the present invention may further comprise the step of:

[0041] Separating the strands of co-extruded food products into individual food products before subjecting the stream of food products to step a).

[0042] Alternatively, the co-extruded food product strands may be divided into individual food products after subjecting the food product stream to step a) and preferably before subjecting the food product stream to step b). However, compared to the consolidation step which involves separation of the co-extruded food product strands into individual food products (typically totaling about 30 to 60 seconds), in a preferred embodiment the method of the present invention comprises an initial hardening step which has a significantly shorter duration (on the order of 0.1 to 0.5 seconds) immediately after or even during co-extrusion of the co-extruded food product strands. It is noted that the initial setting step provides a first initial strength to the coating of the co-extruded food product strands and promotes separation of the co-extruded food product strands into individual food products. It is further noted that the initial setting step may be carried out by applying a brine solution, for example a first brine solution, a second brine solution, or even a further brine solution, to the co-extruded food product strands. Thus, in a preferred embodiment, the method of the present invention comprises the following steps:

[0043] subjecting the co-extruded food product strands to an initial hardening step prior to separating the co-extruded food product strands into individual food products, wherein the initial hardening step comprises subjecting the co-extruded food product strands to a brine solution selected from the group consisting of a first brine solution, a second brine solution, an additional brine solution, and combinations thereof. In one embodiment, the brine solution used for the initial hardening step is preferably the first brine solution.

[0044] Due to the short duration of the initial hardening step, maintaining the pH of the brine solution used in the initial hardening step is not as critical, and therefore, a brine solution containing only sodium chloride, such as the first brine solution, could be sufficient for such a step without risking causing changes in the physical state of the protein.

[0045] In an embodiment of the present invention, the durations of use of both brine solutions included in the set of brine solutions of the present invention are different. In a preferred embodiment, the duration of use of the first brine solution is shorter than the duration of use of the second brine solution. In an embodiment of the present invention, the duration of use of the first brine solution is significantly shorter than the duration of use of the second brine solution. As used herein, the term "significantly" may refer to a difference of a factor of 10 to about 20. Preferably, the duration of use of the first brine solution is about 1 second to about 5 seconds, and the duration of use of the second brine solution is about 30 seconds to about 60 seconds.

[0046] Furthermore, the method of the present invention may comprise the steps of:

[0047] applying liquid smoke to the food product stream before subjecting the food product stream to step b).

[0048] In a further aspect, the present invention relates to a brine solution comprising a salt of lactic acid. It has been found that by providing a brine solution, such as the second brine solution of the present invention, comprising a salt of lactic acid, not only is the visual and aesthetic attributes of the final product improved, but the taste of the final product is also significantly improved.

[0049] The salt of lactic acid may be potassium lactic acid or sodium lactic acid. The lactate salt of the brine solution of the present invention may be L-lactate. In a further preferred embodiment, the lactate salt is produced by fermentation from sugar. An example of such a suitable and preferred lactate salt is PURASAL (R) It is commercially available under the trade name HiPure P Plus (Corbion Inc.) The brine solution of the present invention may consist essentially of lactate salts solubilized in an aqueous medium.

[0050] In some embodiments of the present invention, the brine solution comprises a saturated lactate solution. Alternatively, the brine solution may comprise at least 30% by weight of lactate, where the weight percentage is calculated based on the total weight of the brine solution. In preferred embodiments of the present invention, the brine solution may comprise between 40% and 60% by weight of lactate.

[0051] The present invention further relates to a system for in-line processing of food products using the method of the present invention.

[0052] The present invention further relates to the use of the set of brine solutions of the present invention in a method for in-line processing of food products. In particular, the present invention relates to the use of the set of brine solutions in an enrichment step in a method for in-line processing of food products.

Claims

1. 1. A method for in-line processing of food products, comprising the steps of co-extruding a food dough into a stream of co-extruded food products having a protein-containing coating or a protein-polymer hybrid coating, wherein the method then comprises the following successive steps: a) subjecting the co-extruded food product stream to a food product fortification process, said food product fortification process comprising subjecting the food product stream to a set of brine solutions; and b) heat treating the food product stream obtained in step a); Including, The food product stream comprises strands of co-extruded food products, and the method comprises the steps of: - dividing the strands of co-extruded food products into individual food products before subjecting the stream of food products to step a), and - subjecting the co-extruded food product strands to an initial hardening step before separating the co-extruded food product strands into individual food products; further comprising 1. A method for in-line processing of a food product, wherein the initial hardening step comprises applying to the strands of co-extruded food product a brine solution selected from the group consisting of a first brine solution comprising sodium chloride, a second brine solution comprising a buffer salt, an additional brine solution, and combinations thereof.

2. 2. The method of claim 1, wherein in step b) the food product stream is subjected to two or more heat treatment steps.

3. 3. The method of claim 2, wherein the two or more thermal treatment steps are selected from the group consisting of drying, heating, partially cooking, cooking, and cooling the food product stream.

4. The method comprises the steps of: - applying liquid smoke to the stream of food products before subjecting said stream of food products to step b); 4. The method according to claim 1, further comprising:

5. A method described in any one of claims 1 to 4, wherein the second brine solution contains a salt of lactic acid.

6. 6. The method of claim 5, wherein the salt of lactic acid is selected from the group consisting of potassium lactate, potassium L-lactate, sodium lactate, and sodium L-lactate.