کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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644107 | 884414 | 2006 | 7 صفحه PDF | دانلود رایگان |

A commercial whey protein concentrate (WPC65, supplied by ILAS S.A., Spain) was used as raw material to obtain an alpha-lactalbumin (α-La) enriched solution. Firstly, α-La was simultaneously precipitated with bovine serum albumin (BSA) and immunoglobulins (Igs) by adding lactic acid as Ca2+ ion sequestrant at a pH value around 4.0. The α-La precipitation process was observed to be reversible. Therefore, when the original pH was recovered the protein became soluble again. The proposed process consists of the following steps: (1) precipitation, (2) centrifugation (I), (3) precipitate washing (twice), (4) centrifugation (II) and finally (5) solubilization of the precipitate. Steps 1 and 2 were studied in a previous work by the same authors. Steps 3–5 were investigated in this work. These steps were performed and optimized at laboratory scale. The final α-La enriched solution obtained had a purity of about 74%, while the recovery of this protein was about 86%. More than 99% of the β-lactoglobulin (β-Lg) present in the WPC was removed in the process. This α-La enriched solution can be considered as a good base to prepare infant formulas. This product is very interesting because of its high water solubility and the very low β-Lg concentration. The concentration of β-Lg in the supernatant fractions was higher than 85% (on a dry basis); therefore these fractions could be further concentrated by membrane technology (ultrafiltration) to obtain a β-Lg enriched concentrated product.
Journal: Separation and Purification Technology - Volume 52, Issue 2, December 2006, Pages 310–316