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Production of Milk Powder

Milk destined for the production of powder must be of high chemical, organoleptical, and bacteriological quality. Acidity of milk must be below 0.15% (expressed as lactic acid), otherwise the solubility of the milk powder is reduced. Stored raw milk is not good even when it is kept under refrigerated conditions because it may lead to an increase in free fatty acidy in the resultant dried milk causing many fold increase in lipolysis in the powder produced from such milk. High bacterial counts increase the susceptibility of fat to oxidation during storage of the powder. Oxidation of milk fat reduces the shelf life of the resulting milk powder. Fat oxidation is accelerated by the presence of metals such as copper or iron. Care must be taken that all equipments,pipelines and accessories coming into contact with milk and cleaning solutions are made of stainless steel exclusively.

The basic operations in milk powder production consists of receiving and selecting milk, filtration/clarification, cream separation/standardization, preheat treatment, condensing, homogenisation, drying, packaging and storing of powder. Production of skim milk powder differs slightly from whole milk powder production.

i. Standadization

The objective of standardization is to adjust the ratio of milk fat and total solids to the level required in the final product. Production of skim milk powder differs slightly from whole milk powder production. For skim milk powder, it is necessary to reduce fat in skim milk to less than 0.1%.

ii. Preheat Treatment

The preheating of milk before condensing in the manufacture of dried milks is done for the production of safe and better stable milk powders and also for inducing in it other desirable attributes. Pasteurization at 72oC for 15 s is sufficient to address the safety requirements associated with processing of raw milk, though, higher temperatures and longer holding times may be necessary to meet requirements relating to ther moduric pathogens and specific food spoilage organisms. For milk powder solubility, which mostly depends on the state of the milk protein system, the high temperature short time (HTST) regime is more convenient when compared to prolonged thermal treatment at low temperatures, and has the same microbiological effect. The temperature most frequently used is in the range of 88-95oC for 15-30 sec. HTST regimes with direct or indirect heating are also used with temperatures ranging up to 130oC.

Preheat treatment contributes significantly to the shelf life of dried milks (e.g. whole milk powder) primarily through development of antioxidant or reducing substances.The formation of reactive or free sulphydryl groups, resulting from the heat treatment of milk, are responsible for preventing oxidized flavour development by acting as free radical scavengers, and thus as antioxidants. Products of Maillard reactions also contribute to the overall antioxidant effect in milk powders.

Milk may be heat-treated at temperatures to achieve various levels and types of protein denaturation, according to final product requirements. Skim milk powder is commonly graded according to the amount of undenatured whey protein nitrogen present in non-fat milk solids expressed by the whey protein nitrogen index (WPNI), which is defined as the amount of undenatured whey protein nitrogen measured in mg/g powder. Table 14.1 shows the heat classifications for skim milk powders as was introduced by the American Dry Milk Institute (ADMI) in 1971.
 
Heat classification of skim milk powders and associated heat treatments
                                                           Heat classification of skim milk powders and associated heat
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iii. Condensing

For spray drying, the milk is concentrated in multiple effect evaporators to 40-50 % total solids. For roller drying, the milk is concentrated to 18% total solids. Further concentration for spray drying would increase viscosity and cause difficulties during atomisation of the milk. During roller drying, a higher concentration of milk would form a thicker layer on the rollers, followed by inhibited drying and intensive irreversible changes to proteins, lactose and fat. Evaporators use much lesser thermal energy than driers for removal of equivalent amount of moisture from milk.

iv. Homogenization

Homogenization is not an obligatory operation in milk powder manufacture, but is usually applied to decrease free fat content. Higher free fat content in powder is,however, demanded in certain confections. Homogenization also helps to prevent clumping of fat during reconstitution and improves the keeping quality of powder.Homogenization is conducted after evaporation, or in partly concentrated milk, the concentration rate being not more than 3:1. At higher concentration, homogenization destabilizes milk proteins, thus decreasing powder solubility. The customary homogenization is 2500 to 3000 psi at 62.8 to 76.7oC.

v. Drying


Though a number of drying systems are available, practically only spray drying and roller drying are commercially used in dairy industry. Since the product quality and process economy are much better and are being constantly improved, spray drying has the highest potential today and in the foreseeable future

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