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, mashing 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) mere disappointing, but ways of improving each step in the process are discussed.
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USDA ARS, Eastern Reg Res Ctr, Engn Sci Res Unit, Washington, DC 20250 USAUSDA ARS, Eastern Reg Res Ctr, Engn Sci Res Unit, Washington, DC 20250 USA
Tomasula, PM
Parris, N
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USDA ARS, Eastern Reg Res Ctr, Engn Sci Res Unit, Washington, DC 20250 USAUSDA ARS, Eastern Reg Res Ctr, Engn Sci Res Unit, Washington, DC 20250 USA
Parris, N
Boswell, RT
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USDA ARS, Eastern Reg Res Ctr, Engn Sci Res Unit, Washington, DC 20250 USAUSDA ARS, Eastern Reg Res Ctr, Engn Sci Res Unit, Washington, DC 20250 USA
Boswell, RT
Moten, RO
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USDA ARS, Eastern Reg Res Ctr, Engn Sci Res Unit, Washington, DC 20250 USAUSDA ARS, Eastern Reg Res Ctr, Engn Sci Res Unit, Washington, DC 20250 USA