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СКВАШЕННАЯ СМЕТАНА 9% ЖИРНОСТИ ИЗ РЕКОМБИНИРОВАННОГО МОЛОКА И СПОСОБ ЕЕ ПРОИЗВОДСТВА
专利权人:
ТОО "Марс-2"
发明人:
Фядаравичюс Витаутас
申请号:
RU2014114606
公开号:
RU2014114606A
申请日:
2014.04.14
申请国别(地区):
RU
年份:
2015
代理人:
摘要:
1. A method of producing sour fermented 9% fat derived from recombined milk, wherein the skimmed milk with a pump 1 is fed into the heat exchanger 2, where it is heated to 45 ° -48 ° C, is sent to bactofugeur 3, further using 4 is supplied in pump microfiltration unit 5, where filters are used ceramic ISOFLUX 6,9-8,9 ", which is 1.1-1.6 md bandwidth., at a temperature of 48 ° -53 ° C, the filtrate is sent to the pasteurizer 6 wherein at 56,5 ° -58,5 ° C contains up until alkaline fosfatozy sample does not become negative, it is cooled in heat exchanger 7 to a temperature of 4,0 ° -6,0 ° C and stored in intermediate tanks for further the manufacturing process used filters productivity 5000-20000 dm / h, concentrate throughput 100-1000 dm / h and the permeate flow rate dm 19000-19900 / h, operating temperature of 25 ° -52 ° C, ceramic filters, which are bandwidth 1,1-1 , 6 md., filtration area of ​​25-52 m, the amount of conc. 2-4, the number of filters 10-16.2. The method of claim. 1, characterized in that the water used in the purification method using a reversible osmosis spiral 6,9-8,9 ", the number of filters 10-16, the filter area 565-1500 m 2-6 trub.3 membrane. A method according to any one of claims. 1 and 2, characterized in that used in the manufacture of cream recombined milk must ripen for complete hydration of milk proteins, while stirring in a mixture of water filtrate and skim milk are added thick skim milk and the stabilizer for connecting dehydrated milk fat and dry milk substances, stirred at 55 ° -60 ° C, more fat soluble and are added to the mixture, etc.1. Способ производства сквашенной сметаны 9%-ной жирности, полученной из рекомбинированного молока, отличающийся тем, что обезжиренное молоко при помощи насоса 1 подается в теплообменник 2, где подогревается до 45°-48°C, направляется в бактофугу 3, далее при помощи насоса 4 подается в микрофильтрационный блок 5, где применяются керамические фильтры ISOFLUX 6,9-8,9”, пропускная способность которых 1
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