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Evaporated milk, recombined 26.5 Condensed treated with ultra high temperature and manufacturing processes

机译:浓缩牛奶经重新调制后经过26.5%的超高温处理和制造工艺

摘要

1. A process for the production of condensed milk, recombined solution of 26.5% condensation, the treated ultra-high temperature, characterized in that skimmed milk with a pump 1 is fed into the heat exchanger 2, where it is heated to 45 ° -48 ° C, it is sent to bactofugeur 3 further by a 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, it is cooled in heat exchanger 7 to a temperature of 4,0 ° -6,0 ° C and accumulates in the intermediate containers 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 of 25 ° -52 ° C, ceramic filters, the capacity of which 1 , 1-1.6 mic., 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 membrane trub.3 . The method of claim 1, wherein the water soluble phosphate in 20 ° -45 ° C using an injector or mixer put triple thick stabilizer and skim milk at 20 ° -45 ° C, dissolved fats are placed in an aqueous mixture of the filtrate and skim milk at 20 ° -45 ° C, with 28-32 pasteurized at 78 ° -81 ° C, homogenized 72-75 kp / smpri 78 ° -81 ° C, cooled to 4 ° -5 ° C, kept 6.5 hr treated with ultra-high temperature of 140 ° -145 ° C 2-4 s, homo
机译:1.一种生产炼乳的方法,该炼乳是经处理的超高温的26.5%缩合的混合溶液,其特征在于,用泵1将脱脂的乳送入热交换器2,在其中将其加热至45°-在48℃下,通过泵4将其进一步送至噬菌体3,再将其供应至微滤单元5,在该过滤器中使用陶瓷ISOFLUX 6,9-8,9'',带宽为1.1-1.6 md。在48°-53°C的温度下,滤液被送入巴氏灭菌器6,其中在56.5°-58.5°C为止,直到碱性草磷样品不变为负值为止,在热交换器7中将其冷却至4 ,0°-6,0°C并积聚在中间容器中,用于进一步制造工艺过滤器所使用的性能为5000-20000 dm / h,精矿通过量为100-1000 dm / h,渗透液dm为19000-19900 / h,运行温度为25°-52°C,陶瓷过滤器,容量为1到1-1.6微米。过滤面积为25-52 m,浓缩的2-4,过滤器的数量10-16.2。 2.根据权利要求1所述的方法,其特征在于,在使用可逆渗透螺旋6,9-8,9'',过滤器数10-16,过滤器面积565-1500 m 2-6的纯化方法中使用水膜rub 3。 2.权利要求1的方法,其中将水溶性磷酸盐在20°-45°C下使用注射器或混合器放入三重稠稳定剂和脱脂乳中,在20°-45°C下,将溶解的脂肪置于滤液和在20°-45°C的脱脂牛奶中,在78°-81°C下用28-32巴氏灭菌,均质72-75 kp / smpri 78°-81°C,冷却至4°-5°C,保持6.5小时140°-145°C 2-4 s的超高温,均质

著录项

  • 公开/公告号RU2014114612A

    专利类型

  • 公开/公告日2015-10-20

    原文格式PDF

  • 申请/专利权人 ТОО МАРС-2;

    申请/专利号RU20140114612

  • 发明设计人 ФЯДАРАВИЧЮС ВИТАУТАС;

    申请日2014-04-14

  • 分类号A23C9/00;

  • 国家 RU

  • 入库时间 2022-08-21 14:56:48

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