Single and two-component cation-exchange adsorption of the two pure major whey proteins

被引:17
作者
El-Sayed, Mayyada M. H. [1 ,2 ]
Chase, Howard A. [1 ]
机构
[1] Univ Cambridge, Dept Chem Engn & Biotechnol, Cambridge, England
[2] Natl Res Ctr, Cairo, Egypt
关键词
alpha-Lactalbumin; beta-Lactoglobulin; Cation exchange adsorption; Separation; Equilibrium studies; Packed-bed studies; LASER-SCANNING MICROSCOPY; BETA-LACTOGLOBULIN; ALPHA-LACTALBUMIN; KINETICS; CHROMATOGRAPHY; FRACTIONATION; SEPARATION; TRANSPORT; MECHANISM;
D O I
10.1016/j.chroma.2009.02.080
中图分类号
Q5 [生物化学];
学科分类号
071010 ; 081704 ;
摘要
Adsorption of pure alpha-lactalbumin (ALA) and beta-lactoglobulin (BLG) to the cation exchanger SP Sepharose FF was studied at pH 3.7 with the purpose of developing a process for isolating them from whey. Measurement of Langmuir parameters describing adsorption equilibrium in batch experiments and protein breakthrough time values in 1-ml packed-beds at a linear velocity of 158 cm/h and initial concentrations of 3 mg/ml for BLG and 1.5 mg/ml for ALA suggested the feasibility of using this adsorbent to separate the two proteins when present in a mixture. Subsequent experiments with 5-ml columns at the above concentrations and a linear velocity of 30 cm/h confirmed this and showed evidence of competitive adsorption as ALA displaced and eluted all BLG from the column in a pure form, and the remaining ALA could be eluted thereafter at high purity and with 91% recovery. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:8705 / 8711
页数:7
相关论文
共 25 条
[1]   Modeling of protein adsorption to DEAF sepharose FF: Comparison of data with model simulation [J].
Aboudzadeh, MR ;
Zhu, JW ;
Bin, W .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2006, 23 (01) :124-130
[2]   Quantitative description of protein adsorption by frontal analysis [J].
Avci, AK ;
Çamurdan, MC ;
Ülgen, KÖ .
PROCESS BIOCHEMISTRY, 2000, 36 (1-2) :141-148
[3]  
CAYOT P, 1997, STRUCTURE FUNCTION R
[4]   Dependence of pore diffusivity of protein on adsorption density in anion-exchange adsorbent [J].
Chen, WD ;
Dong, XY ;
Bai, S ;
Sun, Y .
BIOCHEMICAL ENGINEERING JOURNAL, 2003, 14 (01) :45-50
[5]   MODELING METHODS TO AID THE DESIGN AND OPTIMIZATION OF BATCH STIRRED-TANK AND PACKED-BED COLUMN ADSORPTION AND CHROMATOGRAPHY UNITS [J].
COWAN, GH ;
GOSLING, IS ;
SWEETENHAM, WP .
JOURNAL OF CHROMATOGRAPHY, 1989, 484 :187-210
[6]   Fractionation of proteins from whey using cation exchange chromatography [J].
Doultani, S ;
Turhan, KN ;
Etzel, MR .
PROCESS BIOCHEMISTRY, 2004, 39 (11) :1737-1743
[7]  
Etzel M.R., 1999, U.S. Patent, Patent No. 5986063
[8]   SEPARATION OF PROTEINS BY HIGH-PERFORMANCE ANION-EXCHANGE CHROMATOGRAPHY [J].
FLASHNER, M ;
RAMSDEN, H ;
CRANE, LJ .
ANALYTICAL BIOCHEMISTRY, 1983, 135 (02) :340-344
[9]   The influence of protein size on adsorption kinetics and equilibria in ion-exchange chromatography [J].
Garke, G ;
Hartmann, R ;
Papamichael, N ;
Deckwer, WD ;
Anspach, FB .
SEPARATION SCIENCE AND TECHNOLOGY, 1999, 34 (13) :2521-2538
[10]   Preparative ion-exchange chromatography of proteins from dairy whey [J].
Gerberding, SJ ;
Byers, CH .
JOURNAL OF CHROMATOGRAPHY A, 1998, 808 (1-2) :141-151