The effect of high frequency backflushing on the microfiltration of yeast homogenate suspensions for the recovery of soluble proteins

被引:34
作者
Levesley, JA [1 ]
Hoare, M [1 ]
机构
[1] Univ London Univ Coll, Dept Chem & Biochem Engn, Adv Ctr Biochem Engn, London WC1E 7JE, England
基金
英国生物技术与生命科学研究理事会;
关键词
transmembrane pressure pulsing; backpulsing; microfiltration; yeast homogenate; enzyme recovery;
D O I
10.1016/S0376-7388(99)00031-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Periodic backflushing (backpulsing) of the membrane was used to improve the performance of a ceramic tubular membrane for the recovery of a soluble enzyme, yeast alcohol dehydrogenase (ADH), from a suspension of homogenised bakers' yeast cells. Suspensions from concentrations of up to 280 g/l packed cell weight were used. Short (0.1 s) pressure pulses were applied at high frequency (1 Hz) to the permeate side of the membrane by compressed air acting on a diaphragm, causing short periods of reverse flow through the membrane. The intention was that the reverse flow would disrupt the fouling layers on the membrane and enhance forward permeate flux and solute transmission. The result was an increase in solute transmission, by up to 5.4 times in the case of ADH, with a slight reduction in observed permeate flux. The increase in transmission during backpulsing was greater for ADH than for the background of total protein, so some additional product purification was achieved. The resultant effect was an increase in productivity for ADH recovery by backpulsing. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:29 / 39
页数:11
相关论文
共 20 条
[1]  
BERGMEYER HU, 1983, METHODS ENZYMATIC AN
[2]   YEAST ALCOHOL DEHYDROGENASE - SH GROUPS, DISULFIDE GROUPS, QUATERNARY STRUCTURE, AND REACTIVATION BY REDUCTIVE CLEAVAGE OF DISULFIDE GROUPS [J].
BUHNER, M ;
SUND, H .
EUROPEAN JOURNAL OF BIOCHEMISTRY, 1969, 11 (01) :73-&
[3]   PILOT-SCALE VERIFICATION OF BIOPROCESS MODELS [J].
CLARKSON, AI ;
BULMER, M ;
SIDDIQI, SF ;
TITCHENERHOOKER, NJ .
COMPUTERS & CHEMICAL ENGINEERING, 1994, 18 :S651-S655
[4]  
Clarkson AI, 1996, BIOPROCESS ENG, V14, P81
[5]   MODELING AND SIMULATION OF FRACTIONAL PRECIPITATION - COMPARISON WITH PILOT-PLANT DATA [J].
CLARKSON, AI ;
BOGLE, IDL ;
TITCHENERHOOKER, NJ .
COMPUTERS & CHEMICAL ENGINEERING, 1992, 16 :S441-S447
[6]   MODELING OF FOULING OF CROSS-FLOW MICROFILTRATION MEMBRANES [J].
DAVIS, RH .
SEPARATION AND PURIFICATION METHODS, 1992, 21 (02) :75-126
[7]  
FERRY JD, 1936, CHEM REV, V18, P375
[8]   KINETICS OF CONCENTRATION-POLARIZATION FORMATION IN CROSS-FLOW FILTRATION OF PLASMA FROM BLOOD - EXPERIMENTAL RESULTS [J].
JAFFRIN, MY ;
DING, LH ;
LAURENT, JM .
JOURNAL OF MEMBRANE SCIENCE, 1992, 72 (03) :267-275
[9]  
JONSSON G, 1994, WORKSH ASEAN EU MEMB, P157
[10]  
KRONER KH, 1984, PROCESS BIOCHEM, V19, P67