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РЕКОМБИНИРОВАННОЕ МОЛОКО ПАСТЕРИЗОВАННОЕ 2,5 % ЖИРНОСТИ И СПОСОБ ЕГО ПРОИЗВОДСТВА
专利权人:
ТОО "Марс-2"
发明人:
Фядаравичюс Витаутас
申请号:
RU2014114390
公开号:
RU2014114390A
申请日:
2014.04.11
申请国别(地区):
RU
年份:
2015
代理人:
摘要:
1. A method of producing a recombined pasteurized milk of 2.5% fat obtained with the addition of concentrated or dry product is water, characterized in that 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, then by the pump 4 is supplied to 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 the pasteurizer 6 wherein at 56,5-58,5 ° C contains up until alkaline fosfatozy sample does not become negative, is cooled in heat exchanger 7 to a temperature of 4,0-6,0 ° C and stored in intermediate tanks for further manufacturing process filters used performance 5000-20000 dm / h, concentrate throughput 100-1000 dm / h and the permeate flow rate dm 19000-19900 / h, operating temperature 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. A method according to claim 1, characterized in that water is 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 claim 1, characterized in that while stirring in a mixture of water and the filtrate added to skim milk and skim milk thick stabilizer for connecting and dehydrated milk fat dry milk substances at a temperature 35-60 ° C, Melt the fats and add to the mixture, mixed at a temperature of 40-75 ° C, homogenized 187-200 kp / smpri temperature of 40-75 ° C, pasteurized within1. Способ производства рекомбинированного молока пастеризованного 2,5% жирности, полученного с добавлением в сухое или концентрированное изделие воды, 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
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