Patent Application
20140199436
The invention relates to methods for improving viscosity, solubility and particle size of milk proteins. More specifically, the invention relates to methods for using enzymes to improve viscosity, solubility and particle size of milk protein concentrates and milk protein isolates.
Whey protein compositions are popular for use in a variety of foods, beverages, and supplements because they are complete proteins, containing all the amino acids necessary for human nutrition. Whey protein has the highest biological value (i.e., efficiency of use) of any protein. The biological value of whey protein, for example, is 104, while the biological values of eggs, soy protein, and wheat are 100, 74, and 54, respectively. Whey proteins are particularly desirable for protein-enriched beverages because they are less viscous when solubilized in water or other aqueous formulations, such as beverages containing milk or water. In fact, whey is the standard for viscosity at pH 6-7.5. Products made using whey proteins are generally experienced by the consumer as having a smoother taste (i.e., they are less “gritty”). Whey proteins are generally produced as a by-product of cheese manufacturing. Therefore, the availability of whey protein concentrate and whey protein isolate, the two forms of whey protein most commonly used in the food, beverage, and supplement industries, may be contingent upon the demand for cheese. Because the popularity of whey protein concentrates and whey protein isolates as food and beverage ingredients, as well as supplements, has increased significantly in the past few years, the industry has reached a point at which the supply of the protein is limited, relative to the demand.
What are needed are compositions that are more readily available and less dependent upon the production of another food product, while providing the desirable ingredient properties that are associated with whey protein.
The present invention relates to a method for decreasing viscosity, increasing solubility and decreasing particle size of milk proteins, the method comprising admixing milk protein with at least one transglutaminase, and concentrating the protein in the presence of the transglutaminase in its active state. The invention also relates to a product or products made by the process. In various aspects, the method of the invention may be performed by the steps of adding at least one transglutaminase to skim or whole milk; concentrating the protein of the skim or whole milk by a method selected from the group consisting of reverse osmosis, filtration, ultrafiltration, microfiltration, evaporation, and combinations thereof; and performing a drying step comprising spray-drying the concentrated protein without inactivating the transglutaminase prior to the drying step. In other aspects, the step of adding the at least one transglutaminase is performed after the protein is concentrated, such as by the steps of admixing a concentrated milk protein product with at least one transglutaminase, and drying the concentrated milk protein product and transglutaminase admixture without first inactivating the transglutaminase. Aspects of the method of the invention also include performing the steps of treating the protein or filtering the protein in an in-line system, whereby the step of spray-drying is performed immediately following treatment/filtration or filtration/treatment by feeding the enzyme-treated protein into the spray dryer directly from either a filtration or a treatment chamber, depending upon whether the transglutaminase is added pre- or post-concentration.
Aspects of the invention also include rehydrating dried milk protein concentrate milk protein isolate, or a combination thereof, adding transglutaminase to the rehydrated MPC and/or MPI, and co-drying the transglutaminase with the MPC and/or MPI.
Milk protein concentrates (MPC) and milk protein isolates (MPI) are generally isolated from whole or skim milk, and are commercially available, as are whey protein concentrates (WPC) and whey protein isolates (WPI). MPCs contain both casein and whey proteins, and have been proposed as good substitutes for whey protein in the various foods, beverages, and supplements in which whey has been used. However, although they may exhibit acceptable solubility, they tend to produce a more viscous solution when they are mixed with water than do many of the whey protein compositions such as WPCs and WPIs. Whey protein generally sets the acceptable standard for viscosity.
Milk protein concentrates that contain 80% protein (MPC80) or higher have exhibited poor solubility when reconstituted into water, which restricts their use in food applications. Furthermore, because of the larger particle sizes in MPC/MPI, they may produce a gritty texture when used as an ingredient for beverages, an obvious disadvantage in meeting consumer preferences for smooth-tasting formulations. “Addition of NaCl during the diafiltration process can modify the strength of hydrophobic interactions and sulfhydryl-disulfide interchange reactions and thereby affect protein aggregation and the solubility of MPC powders” (Mao, X. Y. et al., Effect of NaCl addition during diafiltration on the solubility, hydrophobicity, and disulfide bonds of 80% milk protein concentrate powder, Journal of Dairy Science, July 2012, Volume 95, Issue 7 , Pages 3481-3488), but the addition of salt into a food product or its processing is not an attractive option if another cost-effective, safe option is available. Furthermore, the addition of ingredients such as vitamins and minerals, for example, may interfere with the salt treatment, excluding it as an option for the preparation of a variety of desirable MPC products.
The inventors have developed a method for decreasing viscosity, increasing solubility and decreasing particle size of milk proteins (significantly reducing the gritty taste and producing a smooth-tasting beverage, for example) for
MPC/MPI so that it can be readily used as a food, beverage, and/or supplement ingredient as WPC/WPI have been. MPC/MPI substitution for WPC/WPI in a food product, for example, has been estimated to reduce the cost of producing the product by about twelve percent. Therefore, the invention also provides a method for producing an ingredient having the desirable properties of whey protein while decreasing the cost of production of the products into which it is incorporated.
In the method of the invention, whole or skim milk (the starting product of traditional MPC/MPI production) is treated with at least one transglutaminase. Preferably, this is done prior to performing further processing steps, as shown in
As used herein, the term “feeding directly” refers to moving an ingredient or product from a first chamber which is fluidly or otherwise operably connected to a second chamber. Preferably, the first chamber and second chamber will not be separated by an intervening chamber or there is no significant process which is performed in the time interval between the time when a process is performed in the first chamber and a process is performed in the second chamber. “Immediately following” refers to a next step or process performed without undue delay, or without any intentional delay. “Decreasing particle size of milk proteins” includes decreasing dry and/or hydrated particle size, decreasing the size of hydrated particles contributing significantly to the absence of a gritty mouth feel. “Reconstituting” includes, and preferably comprises, partially reconstituting—that is, rehydrating, while maintaining a protein product in its more concentrated state.
Transglutaminase treatment of proteins may result in both intra-molecular and inter-molecular cross-linking. While not being bound by theory, the inventors believe that the method shifts the Michaelis-Menten kinetics of the enzyme reaction and, especially if the method is performed at a pH of from about 6 to about 7.5, promotes more intra-molecular crosslinking of the proteins. This results in a decreased particle size as the proteins are folded more tightly. The present method of use for transglutaminase in the dairy industry generally involves treatment of milk proteins in solution, such as treatment of whole or skim milk, followed by inactivation of the enzyme (see, for example, Guyot, C. and U. Kulozik, Effect of transglutaminase-treated milk powders on the properties of skim milk yoghurt,” Int. Dairy J. 21 (2011), 628-635). This tends to result in a product with increased viscosity, which would be expected when inter-molecular cross-links are formed. By modifying the conditions under which the transglutaminase treatment is performed, the inventors believe that they have enabled the formation of more intra-molecular crosslinks, producing smaller particle size, decreased viscosity, and significantly increasing the solubility of milk protein concentrates of from about 70 to about 85 percent (MPC70, MPC80, for example).
Transglutaminases may be obtained from microbial fermentation processes and other sources, and are readily available commercially. Transglutaminases catalyze the post-translational modification of proteins by transamidation of available glutamine residues, resulting primarily in the formation of epsilon-(gamma-glutamyl)lysine cross-links. Tranglutaminases have been used to treat emulsions containing proteins to produce gelatinous, cross-linked gels (Japanese Patent Number 59059151). They have been used to produce cheese (see WO 1997/01961, for example). They have also been used to treat protein solutions to produce yogurt, jelly, and gel cosmetics. However, the commonality in all these processes is the increased viscosity/gelling that is expected to occur when transglutaminase is added. Given the fact that the function of transglutaminase is to cross-link proteins to form intra-molecular and/or inter-molecular crosslinks, and the fact that transglutaminase has traditionally been used for the purposes previously noted, it would therefore seem counterintuitive that addition of transglutaminase during production of a dairy ingredient would produce a product that would have a smaller particle size and be described as less viscous, but when used in the method of the present invention, that is the result that is produced. Furthermore, others have reported that treatment of skim milk powder (MPC) can be treated with transglutaminase to produce a product that can be added to yogurt to increase its viscosity (Guyot, C. and U. Kulozik, Effect of transglutaminase-treated milk powders on the properties of skim milk yoghurt,” Int. Dairy J. 21 (201 1), 628-635). The inventors have discovered that if the process to produce transglutaminase-treated MPC is modified, that modification results in a product that produces reduced viscosity, rather than increased viscosity, in the products into which it is admixed. This is a significant advance in the field of dairy processing and is especially useful for the addition of MPC into various liquids, such as beverages.
Ultrafiltration is a preferred method for producing MPCs, but they may also be produced by precipitating the proteins out of milk or by dry-blending the milk proteins with other milk components. The method of the invention may be performed by adding at least one transglutaminase to whole or skim milk prior to the selected process that will result in concentration of the protein, then spray-drying the concentrated milk protein (MPC) in the presence of the active transglutaminase to produce an MPC powder that exhibits better solubility, decreased particle size (and therefore decreased gritty mouthfeel), and decreased viscosity when admixed to form an aqueous solution. The method of the invention may also be described as admixing reconstituted milk protein concentrate with at least one active transglutaminase prior to spray-drying the protein in the presence of the active transglutaminase. In various aspects of the invention, the step of treating a milk protein concentrate is performed by adding at least one transglutaminase to skim or whole milk, then concentrating the protein by a method including, but not limited to, reverse osmosis, filtration, ultrafiltration, evaporation, or a combination thereof, followed by spray-drying the concentrated protein. In this aspect of the method, the milk protein is concentrated in the presence of at least one active transglutaminase and under temperature conditions suitable for the continued action of the enzyme on the protein during and after concentration, thereby treating the milk protein in its more concentrated form. In other aspects, the step of adding the at least one transglutaminase is performed after the protein is concentrated and before it is dried. Concentrated milk protein product can be derived from at least one product selected from the group consisting of skim milk, whole milk, reconstituted skim milk, reconstituted whole milk, and combinations thereof. Milk protein concentrate may be hydrated sufficiently to allow admixing of the protein and transglutaminase, and the admixture components may be co-dried. Aspects of the invention also include performing the steps of treating the protein or filtering the protein in an in-line system, whereby the step of spray-drying is performed immediately following treatment/filtration or filtration/treatment by feeding the enzyme-treated protein into the spray-dryer directly from either a filtration or a treatment chamber, depending upon whether the transglutaminase is added pre- or post-concentration. Another option is also contemplated by the invention, and that is rehydration of dried milk protein concentrate, followed by the addition of at least one transglutaminase to treat the rehydrated milk protein concentrate. In some aspects, this may be performed by rehydrating a dried milk protein concentrate to maintain the MPC in a significantly more concentrated form than is found in milk, adding at least one transglutaminase to the rehydrated MPC, holding the MPC/transglutaminase for a sufficient time to allow the transglutaminase to act on the MPC, then spray-drying the MPC/transglutaminase.
The inventors found that strong heat treatment after the addition of enzyme negatively affects the enzyme treatment. Therefore, it is advisable to perform any pasteurization that may be desired prior to treatment of the MPC. Incubation temperatures during enzyme treatment may vary from about 77 degrees Fahrenheit to about 149 degrees Fahrenheit. The inventors have also discovered that results are significantly better if MPC is spray-dried immediately after treatment. That is, the treated MPC is not held in containers in a liquid form for extended periods of time, such as for a period of hours, or overnight, for example, and then dried. Making the spray-drying process a part of the on-site processing steps, preferably in an in-line manner directly from the treatment chamber, will produce superior results.
Equipment, equipment set-up, and methods for accomplishing the method of the invention, given the disclosure provided here by the inventors, are known to those of skill in the art. For example, it is well within the skill of on in the art of dairy processing to utilize various means, such as filtration, to concentrate milk proteins by removing the liquid and, preferably, lactose. Techniques such as microfiltration would generally not be used, however, unless it would be desired by the processor to filter out whey proteins. Spray-drying is frequently mentioned herein, but those of skill in the art may utilize other drying methods known to those in the industry, particularly those which produce more rapid drying effects.
Production of MPC from Milk:
Milk was run through a fat separator to remove fat and produce skim milk. The skim milk was collected into a tank and warmed to 104° F. Transglutaminase (2.5 g/gallon of milk) was added and the enzyme treatment was allowed to proceed for 4 hours by holding the skim milk at 104° F. during this time. The skim milk was then heat-treated and subjected to ultrafiltration (UF) to produce a milk protein concentrate (UF-MPC). The UF-MPC was then subjected to further filtration to produce a filtered MPC (F-MPC), and the F-MPC was spray-dried. Spray-drying was done in-line, without the presence of holding tanks or holding the F-MPC for a period of time prior to sending it to the spray-dryer.
The resulting product was admixed with water and allowed to sit for about 30 minutes. Four MPCs currently on the market were also individually admixed with water and allowed to sit for the same period of time, as comparison. Results are shown in
Viscosity of the reaction mix was measured at hourly time points. Results are shown in Table 1 and
This application claims the benefit of priority of U.S. Provisional Patent Application No. 61/752,957, filed Jan. 15, 2013, the contents of which are incorporated herein by reference where allowed by applicable law and/or regulation.
| Number | Date | Country | |
|---|---|---|---|
| 61752957 | Jan 2013 | US |
