PROCESS FOR THE MANUFACTURE OF MILK PROTEINS

Abstract: The invention relates to a method for the isolation of total milk protein or whey protein content of milk, in a concentrated and functional form. The protein product is suitable for use in food formulations and dietetic products, where it performs as well as sodium caseinate, but with the added benefit of having more bland flavour characteristics. The product has enhanced nutritional properties and better flavour characteristics when compared to sodium caseinate. The process involves the acidification of skimmed milk or whey to a pH below the isoelectric point, followed by heating to at least 50 DEG C at the acidic pH.

Description: Process for the manufacture of milk proteins The present invention relates to a method for the isolation of the total milk protein content from milk. The method may also be applied to whey to extract the whey protein content, preferably in a concentrated and functional form. The product is suitable for use in food formulations and dietetic products. In particular, the product of the present invention will perform as well as sodium caseinate in food formulations, such as in enhancing the consistency of yoghurt and regulating the texture of processed cheese, but with the added benefit of having more bland flavour characteristics. When used in dietetic preparations the product of the invention is superior to sodium caseinate because it has enhanced nutritional properties due to the incorporation of whey proteins, and it has better flavour characteristics. In the present context functional relates to the role of ingredients in imparting desirable effects on the texture and consistency of the food product into which it is incorporated e.g. emulsification or emulsion stability, viscosity enhancement, water-binding and foaming/whipping ability. The protein content of milk comprises of caseins ( 80% of total protein content) and whey proteins including non-protein nitrogen (20%). Casein is usually isolated industrially from milk by means of precipitation either at its isoelectric pH of 4.6 or in its paracasein form by enzymatic coagulation of milk. In the former case, it is necessary to resolubilise the precipitated curd by neutralisation with a suitable alkali such as sodium hydroxide. Whey proteins are soluble under these conditions, and this distinguishing feature has led to the development of a range of technologies which are now widely used for the production of whey protein concentrates (protein content typically in the range of 20-80%) and whey protein isolates (protein content >90%) . Over time industrial manufacture has therefore tended to evolve around the manufacture of these two distinct groups of proteins, which are marketed as such or occasionally blended together, sometimes with other ingredients, to produce certain functional characteristics and/or economic benefit in food formulations. For example, sodium caseinate is blended with whey protein concentrate (and maybe other ingredients such as buttermilk powder and/or skim milk powder) to produce a blended or so-called "tailor-made" ingredient for use in yoghurt manufacture. Isolating the complete complement of protein in milk in a single manufacturing step offers the prospect of increasing yield and extending functional attributes of protein-based ingredients thus derived. However, early processing attempts at the co-precipitation of both proteins yielded products which possessed poor solubility characteristics, and thus were of limited use in food formulations. The earliest work on the manufacture of acid co-precipitates from heated milk are described in U.S. Patent No. 2 623 038 of Scott. Described is a process in which alkali is added to skim milk to reduce its acidity and to prevent initial precipitation of protein when heating the milk to 90°C. The curd produced by acidification of the heated milk is separated from the whey, washed and dried. U.S. Patent No. 2832 685 also by Scott describes the production of a soluble milk protein by dissolving a casein-lactalbumin fusion (also known as interaction or complex formation) in potassium hydroxide to neutral pH, increasing the pH to between 8.0 to 8.5 by the addition of ammonia followed by heating to 77 to 85°C and drying the solution. During drying ammonia was evaporated and the pH of the powder was reduced to between 6.6 and 7.3. In general, prior art methods of producing co-precipitates have relied on conditioning of milk at its natural pH (typically 6.7 to 6.8) before precipitation, by use of heat treatment alone or in combination with the addition of calcium. Conditioning is a classical processing step in the processing of co-precipitate in which the heat-induced interaction which takes place between casein and whey proteins (based specifically on kappa- casein/β-lactoglobulin fractions) is exploited. During the coagulation step that follows, the precipitation of whey protein along with casein is facilitated. Heat treatment takes place at about 80-90°C with a holding period, followed by acidification to induce precipitation of both casein and whey proteins at the isoelectric point. Variants of this process result in the production of co-precipitates with varying levels of calcium i.e. high-cal, mediu -cal and low-cal. These specifications result from the addition of a calcium salt e.g. calcium chloride (CaCl ? ) to milk before heat treatment in order to aid total protein recovery and improve the nature of the curd formed. These processes are generally referred to as traditional in that they are generally well-known, had reached a certain stage of commercial development in Australia and New Zealand in the 1960s and have been reviewed in an article by Southward and Goldman in Co-Precipitates - A Review, N.Z.J. Dairy Sci. Technol . 10 p. 101-112, (1975). The product of these processes has limited functional properties in food applications as an ingredient due to its poor solubility. European Patent No. 0 064 509 relates to a method of precipitating whey protein by use of a high alkaline pH, that is a pH above 9. Dairy whey and a normally acid insoluble protein which has an isoelectric point of between 4 and 5 are maintained at a temperature of about 55 C, and then alkalised to a pH of about 9 to 11, after which the mixture is acidified to a pH of about 2 to 4 and the pH is adjusted to the isoelectric point of the protein used in order to obtain whey protein and the protein as a precipitated protein complex. It appears necessary to use a second protein in order to "take out" the whey proteins" . This process promotes interaction of whey proteins with isoelectrically precipitable proteins by a process of alkylysing, acidification and isoelectric precipitation. The emphasis is placed on application to whey. However, exposure to a high alkaline pH is undesirable from a nutritional point of view. Other processes for co-precipitation rely on the use of protein complexing agents such as polysaccharides (SU 1597154-A), polymers (RU 2010534-C1) or polyphosphates (IL 40215-A). These processes involve a non-isoelectric precipitation process which uses polymer interaction chemistry to initiate phase separation. These processes exploit different separation phenomena. The major disadvantage is the contamination of the protein with the complexing agent so that additional steps for recovery of the polymer are needed in order to reduce costs. Additionally effluent loadings may be high. It is also known from European Patent No. 0 115 651 B to adjust the pH of milk to greater than 6.8 followed by heating to denature the protein, cooling and precipitation. The process involves moderate pH adjustment of milk on the alkaline side before heat treatment and acidification. This process avoids the classical casein/whey protein interaction by heating at a pH above 6.8, but it allows some whey protein aggregation. European Patent No. 91369 B describes a process of acidifying milk below pH 3.5 using cationic resin without coagulation, and without high heat treatment. The acidification uses ion-exchange resins rather than direct acid injection. The process also relies on the blending of acidified milk at approximately pH 3 with raw skim milk to produce a coagulu of pH 4.6. The process essentially is an alternative process for casein manufacture with some increase in yield due to the incorporation of proteose peptone fractions from milk. The process of the present invention enables both casein and whey proteins to be co-precipitated and isolated in a functional form. Additionally, the process has the advantage of improved yield in terms of casein manufacture by virtue of including the whey protein component of milk and also the resulting "whey" is deproteinated which saves on further processing costs to concentrate the whey protein separately. The process is also suitable for the manufacture of casein and caseinates with modified composition in accordance with Commission Regulation (EEC) No. 2921/90. "Co-precipitate" is a traditional term which acknowledged the complex formation between two distinct proteins so that during coagulation there was a genuine co-precipitation phenomenon. In the process of the present invention this does not take place so it is considered that the present invention relates to the production of a milk protein ingredient. According to the present invention there is provided a process for the manufacture of a milk or whey protein ingredient characterised in that skim milk or whey is acidified to below its isoelectric point and heated to at least 50 C while at the acidic pH. Temperatures greater than 50 C can be employed. For example, under atmospheric pressure milk can be heated up to 100 C and under appropriate pressurised conditions, temperatures above 100 C can be employed, such as in ultra-high temperature thermal processes. Preferably the skim milk or whey is chilled prior to acidification to a temperature of less than 30 C preferably less than 4 C. Preferably the milk or whey is subjected to rapid acid dosage and mixing following the chilling step. The mixture may then be heated to at least 50°C and held at that temperature for at least 5 minutes, preferably 10 minutes. The skimmed milk or whey initially used in the process should ideally have a fat content of 0.5% (w/v) or less. The isoelectric point is generally considered to be pH 4.6 for milk proteins since bulk milk is used for processing and the value does not substantially vary from 4.6. The pH may suitably be lowered by the use of mineral or organic acid addition. The most suitable acid for lowering the pH is hydrochloric acid, but other acids such as sulphuric acid or lactic acid may be used. The acid preferably is used to lower the pH to below 3.9, most preferably to between 2.5 and 3.5. Alternatively, ion-exchange or electrodialysis resin may be used to lower the pH. Skimmed milk or whey may be held at 50°C or above for up to 30 minutes, although a holding time of 20 minutes is preferred and most preferably 10 minutes. The preferred temperature is above 75°C, more preferably 85 to 90 C, most preferably above 90°C. The coagulum is then cooled to below 90°C, preferably below 70°C. Following cooling, the pH is raised to between 4.0 and 5.0, preferably 4.6. The pH is raised by the addition of a strong base such as NaOH, OH, NH 4 0H, most preferably NaOH. Preferably the precipitated curd is washed a number of times, preferably twice and separated from the supernatant wash water. The precipitated curd may be separated from the supernatant wash water using a centrifugal separator, preferably a decantor centrifuge. Alternatively a centrifugal clarifier may be used. In a particular aspect the invention provides a process for the manufacture of a milk or whey protein ingredient comprising the steps: (a) skimmed milk or whey is cooled to a temperature of less than 30°C, preferably 4 C or lower, (b) the pH is reduced below the isoelectric point of milk or whey proteins, preferably to between pH 2.5 and pH 3.5, (c) the milk or whey is heated to at least 50°C and held at that temperature for at least 5 minutes, preferably 10 minutes, (d) the pH is raised to between 4.0 and 5.0, (e) the product is allowed to coagulate, and (f) the precipitated curd is separated from the supernatant. The process of the present invention utilises the acid side of milk's or whey's natural pH in order to condition it for co-precipitation. The process thus uniquely acidifies skim milk or whey, without incurring premature coagulation while passing through the isoelectric point. This is facilitated by the prior chilling step, before rapid acid dosage of the mixture followed by heating. The heat treatment plays a significant role in modifying the whey proteins so that they co-precipitate along with casein at the usual isoelectric pH of 4.6. The invention also relates to a total milk protein ingredient or a whey protein ingredient whenever produced by the process. Example 1 Skim milk with a protein content of 3.44% was chilled to 3 C and fed into a vat with continuous pumping with optional variable speed controller. There was continuous dosing of 4N HC1 through a distributor inserted into the path of milk flow entering the coagulator. An in-line pH probe was linked to a set-point controller to regulate acid dosage of the milk to within pH 2.5-3.0. The flow path through the pipework of the coagulator created sufficient turbulence for acidification of the milk to reach equilibrium pH conditions rapidly. The heating step is performed by a steam injection system connected to the coagulator which enabled the acidified milk temperature to reach approximately 70°C. On discharging the hot acidified milk into an agitated tank, further heating was provided using a jacketed heating system on the tank so as to reach 90°C. The acidified milk was maintained at 90 C in the tank for 30 minutes, after which it was cooled to <80°C using chilled water flow through the jacket. The pH was then readjusted to pH 4.6 using 4N NaOH; the light curd displayed good settling characteristics once the agitation system was stopped. The coagulated skim milk was fed to a Westfalia Separator centrifugal clarifier model KNA 3 featuring bowl type CNB in order to separate the protein curd from the whey. In operating the separator using the clarifier mode, blank inserts were put in place of the 4 nozzles located on the periphery of the bowl. The collected curd was mixed with R0 (reverse osmosis treated) water to make up to approximately 80% of the original volume of skim milk used and the clarification process was repeated (Table 2). To solubilise the curd the washed curd was suspended using a S Siillvveerrssoonn mmiixxeerr wwhhiillee nneeuuttrraalliissiinngg ttoo ppHH 77.0 at 50 C using 30% NaOH. A total solids content of 18% was recorded The solubilised proteinate concentrate was spray dried in an Anhydro pilot-scale spray drier, model LAB 3 using inlet and outlet temperatures of 190 and 90 C, respectively. The gross chemical composition of the proteinate is given in Table 3. The soluble milk proteinate produced by the method which is the subject of this application comprises almost the full complement of casein and whey protein occurring in milk. It has a flavour which is superior to that of casein/caseinate products. It is also superior to similar products which are produced by means of exposing milk at an early stage in the process to high alkaline pH levels, that is greater than pH 8, as this leads to a reduction in the bio availability of essential a ino acids such as lysine, and the increased risk of forming processing-based artifacts such as lysinoalanine. Table 1: Effect of Holding Time at 90°C on the Total Protein content of whey: The efficiency of the proposed process in terms of maximising the recovery of whey protein is improved by holding the heated coagulum for a minimum period of 10 minutes at the acidic pH recommended (<pH 3.5). The data in the table that follows illustrates the residual protein content in the filtrate after readjustment of the pH to 4.6 (the filtrate was obtained in the laboratory by pouring a sample of the coagulum on a filter funnel). The results indicate that improvements in reducing the protein content of they whey by extending the holding time beyond 10 minutes are only marginal. Sample Source T Toottaal Protein (N x 6.38) ex-pipe (entry to tanιk) 0.61 0 in 0.44 10 min 0.38 20 min 0.37 30 min 0.35 skim milk 3.71 Clarified AMP whey (ex KNA 3) 0.39 Table 2: Stepwise Curd Separation and Washing in Demonstrated Example: Step Wash-water Volume Notes Protein curd- Throughput: whey separation whey discharge rate from KNA 3 clarifier. 11.95 kg/min Wash No. 1 transferred separated curd (99.35 kg) back pH 4.92; temp 32°C into CPC tank; added RO water to restore to 80% original volume; Protein curd- KNA 3 clarifier wash water separation Wash No. 2 similar to Wash No. 1 pH 5.15; temp 31°C Protein curd- KNA 3 clarifier wash water separation (repeat) Table 3: Proximate compositional analyses (spray dried proteinate) Total Protein: 91.76% Ash: 3.51% Moisture: 2.67%

Claims: CLAIMS 1. A process for the manufacture of a milk or whey protein ingredient characterised in that skimmed milk or whey is acidified to below its isoelectric point and heated to at least 50 C while at the acidic pH. 2. A process as claimed in claim 1 wherein the skimmed milk or whey is chilled prior to acidification to a temperature of less than 30°C, preferably less than 4 C. 3. A process as claimed in claim 2 wherein the skimmed milk or whey is subjected to rapid acid dosage following chilling. 4. A process as claimed in claim 3 wherein the acid whey mixture is heated to at least 50 C and held at that temperature for at least 5 minutes and up to 30 minutes, preferably 20 minutes, most preferably 10 minutes. 5. A process as claimed in any preceding claim wherein the skimmed mi 1 k or whey has a fat content of 0.5% (w/v) or less. 6. A process as claimed in any preceding claim wherein the skimmed milk or whey is acidified by the use of a mineral or organic acid such as sulfuric acid, lactic acid or hydrochloric acid, preferably hydrochloric acid. 7. A process as claimed in any of claims 1 to 5 wherein ion exchange or an electrodialysis resin are used to lower the pH. 8. A process as claimed in any preceding claim wherein the skimmed milk or whey is acidified to a pH below 3.9, preferably between 2.5 and 3.5. 9. A process as claimed in any preceding claim wherein the skimmed milk or whey is held at a temperature above 75°C, more preferably between 85 and 90°C and most preferably above 90°C. 10. A process as claimed in any preceding claim wherein the coagulated skimmed milk or whey is cooled, following heating to 50 C, to a temperature below 90 C preferably below 70 C. 11. A process as claimed in claim 10 wherein, following cooling, the pH of the coagulum is raised to between 4.0 and 5.0, preferably 4.6. 12. A process as claimed in claim 11 wherein the pH is raised by the addition of a strong base such as sodium hydroxide, potassium hydroxide or ammonium hydroxide, most preferably sodium hydroxide. 13. A process as claimed in claim 12 wherein precipitated curd is washed, preferably twice, and separated from the supernatant wash water, preferably using a centrifugal separator or a centrifugal clarifier. 14. A process for the manufacture of a milk or whey protein ingredient comprising the steps: (a) skimmed milk or whey is cooled to a temperature of less than 30°C, preferably 4 C or lower, (b) the pH is reduced below the isoelectric point of milk or whey proteins, (c) the milk or whey is heated to at least 50°C and held at that temperature for at least 5 minutes, (d) the pH is raised to between 4.0 and 5.0, (e) the product is allowed to coagulate, and (f) the precipitated curd is separated from the supernatant. 15. A total milk or whey protein ingredient whenever produced by a process as claimed in any preceding claim.

Inventors: KELLY PHILIP M, O'KENNEDY BRENDAN T, KELLY, PHILIP, M., O'KENNEDY, BRENDAN, T.
Applicants: KELLY PHILIP M, KENNEDY BRENDAN T O, TEAGASC AGRIC FOOD DEV AUTHORI, KELLY, PHILIP, M., O'KENNEDY, BRENDAN, T., TEAGASC, THE AGRICULTURE AND FOOD DEVELOPMENT AUTHORITY
Application year: 1998
Main classification: A23J1
IPC codes: A23J1