Gésan-Guiziou G, Daufin G, Timmer M, Allersma D, van der Horst C
INRA, Laboratoire de Recherches de Technologie Laitière, Rennes, France.
J Dairy Res. 1999 May;66(2):225-36. doi: 10.1017/s0022029999003519.
Fractions enriched with alpha-lactalbumin (alpha-la) and beta-lactoglobulin (beta-lg) were produced by a process comprising the following successive steps: clarification-defatting of whey protein concentrate, precipitation of alpha-lactalbumin, separation of soluble beta-lactoglobulin, washing the precipitate, solubilization of the precipitate, concentration and purification of alpha-la. The present study evaluated the performance of the process, firstly on a laboratory scale with acid whey and then on a pilot scale with Gouda cheese whey. In both cases soluble beta-lg was separated from the precipitate using diafiltration or microfiltration and the purities of alpha-la and beta-lg were in the range 52-83 and 85-94% respectively. The purity of the beta-lg fraction was higher using acid whey, which does not contain caseinomacropeptide, than using sweet whey. With the pilot scale plant, the recoveries (6% for alpha-la; 51% for beta-lg) were disappointing, but ways of improving each step in the process are discussed.
富含α-乳白蛋白(α-la)和β-乳球蛋白(β-lg)的组分是通过以下连续步骤生产的:乳清蛋白浓缩物的澄清脱脂、α-乳白蛋白的沉淀、可溶性β-乳球蛋白的分离、沉淀物洗涤、沉淀物的溶解、α-la的浓缩和纯化。本研究首先在实验室规模上用酸性乳清,然后在中试规模上用高达干酪乳清评估了该工艺的性能。在这两种情况下,使用渗滤或微滤从沉淀物中分离出可溶性β-lg,α-la和β-lg的纯度分别在52-83%和85-94%范围内。使用不含酪蛋白巨肽的酸性乳清时,β-lg组分的纯度高于使用甜乳清时的纯度。对于中试规模的工厂,回收率(α-la为6%;β-lg为51%)令人失望,但文中讨论了改进该工艺各步骤的方法。