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PROCESS FOR PREPARING AN ACIDIFIED AND CONCENTRATED MILK PRODUCT USEFUL FOR GELLIFYING AND FOR WHIPPING WHEN MAKING ACIDIFIED MILK DESSERTS

机译:制备用于酸化和搅打酸牛奶甜点时使用的浓缩浓缩乳制品的过程

摘要

For the Contracting States : BE, CH, DE, GB, IT, LT, NL, SE. 1. Process for the manufacture of an acidified dairy product suitable for gelling and for whipping , characterized in that is comprises the following stages : - a stage of acidifying whole or skimmed milk or of buttermilk to a pH below or equal to 3.8, the said acidifying being carried out by ion exchange with a cation exchange resin in H**+ form, either at a temperature of 0 degree to 4 degrees C, or in the presence of a tailing consisting of milk previously acidified to a pH below 3.8, - followed by a stage of concentrating the acidified product obtained to a protein content of at least 45 g/kg and capable for reaching 100 g/kg, the said concentration being produced by ultrafiltration or by reverse osmosis. For the Contracting State : AT 1. Process for the manufacture of an acidified dairy product suitable for gelling and for whipping , characterized in that is comprises the following stages : - a stage of acidifying whole or skimmed milk or of buttermilk to a pH below or equal ot 3.8, the said acidifying being carried out by ion exchange with a cation exchange resin in H**+ form, either at a temperature of 0 degrees to 4 degrees C, or in the presence of a tailing consisting of milk previously acidified to a pH below 3.8, - followed by a stage of concentrating the acidified product obtained to a protein content of at least 45 g/kg and capable of reaching 100 g/kg, the said concentration being produced by ultrafiltration or by reverse osmosis.
机译:对于缔约国:BE,CH,DE,GB,IT,LT,NL,SE。 1.制造适用于胶凝和搅打的酸化乳制品的方法,其特征在于包括以下步骤:-将全脂或脱脂牛奶或酪乳酸化至pH低于或等于3.8的步骤,酸化是通过与H ** +形式的阳离子交换树脂进行离子交换来进行的,或者在0度至4摄氏度的温度下进行,或者在存在由酸化至pH值低于3.8的牛奶组成的尾矿中进行-随后是将获得的酸化产物浓缩至蛋白质含量为至少45g / kg并且能够达到100g / kg的阶段,所述浓度通过超滤或通过反渗透产生。对于缔约国:AT 1.制造适于胶凝和搅打的酸化乳制品的方法,其特征在于,包括以下步骤:-将全脂或脱脂牛奶或酪乳酸化至pH低于或低于pH的步骤。等于3.8,所述酸化是通过与H ** +形式的阳离子交换树脂在0℃至4℃的温度下,或在由预先酸化为pH低于3.8,-随后是浓缩所获得的酸化产物至蛋白质含量为至少45g / kg并且能够达到100g / kg的阶段,所述浓度通过超滤或通过反渗透产生。

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