حصل حديثًا تطور في صناعة أغشية الترشيح مما يسمح بإمكانيات جديدة لفصل البروتينات من
المصل على نطاق واسع و بتكاليف منخفضة ، فبالترشيح الدقيق بأغشية من السيراميك أقطار مساماتها
5.0 تم الحصول على رشاحة تحتوي ميكرونًا لمصل الجبن بعد تعديل رقم حموضته إلى0.1 = pH
بصورة أساسية على الألفالاكتالبومين و البيتالاكتوغلوبلين و حجز البروتينات ذات الأوزان الجزيئية العالية
مثل غلوبيولينات المناعة، ألبومين المصل البقري و اللاكتوفيرين و توصلنا لاحقًا إلى زيادة نسبة
الالفالاكتاليومين بالنسبة إلى البيتالاكتوغلوبلين في رشاحة الترشيح الدقيق و ذلك بالترشيح فوق العالي
لهذه الرشاحة بأغشية من السيراميك ذات نقاط قطع جزيئيية مختلفة.
Recent advances in membrane filtration technology provided new
opportunities for large scale low – cost protein fractionation from whey .
Exposure of whey to a pH of 5.0 prior to micro filtration using a 0.1 μm
ceramic membrane led to optimised retention of higher molecular weight
proteins immunoglobulin, bovine serum albumin and lactoferrin. The resulting
permeate contained a protein fraction enriched in Alfa – lactalbumin and Beta
– lactoglobulin. Enrichment of Alfa –lactalbumin relative to Beta –lactoglobulin
was accomplished using new UF ceramic membranes with different molecular
weight cut – off.
References used
Donnelly W. J., Mehra R.. (1990). “Fractination of milk proteins” biochem. Soc. Trans. 18 (2) 1238
ElgarP., Novis C. S., Ayers J. S, Pitchard M. Otter D. E., PalmanoK. P. (2000). Simultaneous separation and quantification of the major bovine whey proteins including proteose peptone and caseinommacropeptide by reversed phase high performance liquid chromatography on polystrenedivinylbenezene. J. Chro. 878:183-196
Hurwitz M. F., Branthy J. S. (2000). “Shear separation : a promising method for protein fractionation.“ Lait (80) : 121 – 127
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