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Production of acid soluble soy protein isolate ('S800')

机译:酸溶性大豆分离蛋白的生产(“ S800”)

摘要

A soy protein product having a protein content of at least about 60 wt% (N x 6.25) d.b., preferably an isolate having a protein content of at least about 90 wt% (N x 6.25) d.b., is formed by extracting a soy protein source with water to form an aqueous protein solution having a pH of about 1.5 to about 11, preferably about 5 to about 7, and separating the resulting aqueous protein solution from residual soy protein source. The protein concentration of the aqueous protein solution is increased to about 50 to about 400 g/L while the ionic strength is maintained substantially constant by using a selective membrane technique. The resulting concentrated protein solution is optionally diafiltered and a calcium salt, preferably calcium chloride, is added to the concentrated and optionally diafiltered protein solution to a conductivity of 5 to about 30 mS. Precipitate formed as a result of the calcium salt addition is removed and the resulting clarified retentate is diluted into about 2 to about 20 volumes of water prior to acidification to a pH of about 1.5 to about 4.4 to produce an acidified clear protein solution. The acidified clear protein solution is then concentrated and optionally diafiltered and optionally dried. Variations of this procedure can be used to produce a soy protein product which is soluble, transparent and heat stable in acidic aqueous environments.
机译:通过提取大豆蛋白形成具有至少约60wt%(N×6.25)db的蛋白质含量的大豆蛋白产品,优选具有至少约90wt%(N×6.25)db的蛋白分离物。用水源形成蛋白质水溶液,其pH为约1.5至约11,优选约5至约7,并将所得的蛋白质水溶液与残留的大豆蛋白质来源分离。通过使用选择性膜技术,将蛋白质水溶液的蛋白质浓度增加至约50至约400g / L,同时使离子强度基本保持恒定。任选地对所得的浓缩蛋白溶液进行渗滤,并将钙盐,优选氯化钙添加至浓缩且可选地渗滤的蛋白溶液中,电导率为5至约30mS。除去由于添加钙盐而形成的沉淀物,将所得的澄清的渗余物稀释至约2至约20体积的水中,然后酸化至约1.5至约4.4的pH以产生酸化的澄清蛋白质溶液。然后将酸化的透明蛋白质溶液浓缩,并任选地进行渗滤和任选地进行干燥。该方法的变化可用于生产在酸性水性环境中可溶,透明和热稳定的大豆蛋白产品。

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