Negatively charged tangential flow ultrafiltration membranes for whey protein concentration

被引:42
作者
Arunkumar, Abhiram [1 ]
Etzel, Mark R. [1 ]
机构
[1] Univ Wisconsin, Dept Chem & Biol Engn, Madison, WI 53706 USA
关键词
Whey proteins; Ultrafiltration/diafiltration; Sieving coefficient; Charged ultrafiltration membranes; Flax enhancement; ALPHA-LACTALBUMIN; BETA-LACTOGLOBULIN; FILTRATION; FRACTIONATION; LENGTH; FLUX;
D O I
10.1016/j.memsci.2014.10.049
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
This work examines the use of wide-pore negatively charged ultrafiltration membranes for whey protein concentration. The hypothesis is that by placing a negative charge on the surface of an ultrafiltration membrane, negatively charged proteins are rejected by electrostatic repulsion and not simply sized based sieving. This allows using wide-pore membranes that have a higher flux without suffering a loss in protein recovery. It was found that negatively charged 100 kDa ultrafiltration membranes had the same protein recovery as 10 kDa unmodified membranes used in the dairy industry, but offered a flux that was at least two-fold higher. The new membranes were used for a 40-fold concentration of whey with subsequent diafiltration to mimic the industrial process for making whey protein concentrate. Mass balance models of concentration and diafiltration were developed and each agreed well with the experimental results. The experimental methods and mathematical models developed in this work can be used to design, simulate and optimize different process flow sheets, and explore the effect of various operating conditions on the membrane processing of whey. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:340 / 348
页数:9
相关论文
共 35 条
[1]
MASS-TRANSFER LIMITATIONS DURING ULTRAFILTRATION OF CHEESE WHEY WITH INORGANIC MEMBRANES [J].
AIMAR, P ;
TADDEI, C ;
LAFAILLE, JP ;
SANCHEZ, V .
JOURNAL OF MEMBRANE SCIENCE, 1988, 38 (03) :203-221
[2]
Fractionation of α-lactalbumin and β-lactoglobulin from bovine milk serum using staged, positively charged, tangential flow ultrafiltration membranes [J].
Arunkumar, Abhiram ;
Etzel, Mark R. .
JOURNAL OF MEMBRANE SCIENCE, 2014, 454 :488-495
[3]
Fractionation of α-lactalbumin from β-lactoglobulin using positively charged tangential flow ultrafiltration membranes [J].
Arunkumar, Abhiram ;
Etzel, Mark R. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2013, 105 :121-128
[4]
Development of an optimized dextran retention test for large pore size hollow fiber ultrafiltration membranes [J].
Bakhshayeshi, Meisam ;
Teella, Achyuta ;
Zhou, Hongyi ;
Olsen, Cathryn ;
Yuan, Wei ;
Zydney, Andrew L. .
JOURNAL OF MEMBRANE SCIENCE, 2012, 421 :32-38
[5]
A General Approach for Predicting the Filtration of Soft and Permeable Colloids: The Milk Example [J].
Bouchoux, Antoine ;
Qu, Peng ;
Bacchin, Patrice ;
Gesan-Guiziou, Genevieve .
LANGMUIR, 2014, 30 (01) :22-34
[6]
Importance of the control mode in ultrafiltration: case of raw cane sugar remelt [J].
Decloux, M ;
Tatoud, L .
JOURNAL OF FOOD ENGINEERING, 2000, 44 (02) :119-126
[7]
Whey protein isolate and glycomacropeptide recovery from whey using ion exchange chromatography [J].
Doultani, S ;
Turhan, KN ;
Etzel, MR .
JOURNAL OF FOOD SCIENCE, 2003, 68 (04) :1389-1395
[8]
Etzel M.R., 2008, Process scale purification of antibodies, P325
[9]
Manufacture and use of dairy protein fractions [J].
Etzel, MR .
JOURNAL OF NUTRITION, 2004, 134 (04) :996S-1002S
[10]
Fouling behavior of zwitterionic membranes: Impact of electrostatic and hydrophobic interactions [J].
Hadidi, Mahsa ;
Zydney, Andrew L. .
JOURNAL OF MEMBRANE SCIENCE, 2014, 452 :97-103