Beer clarification by cross-flow microfiltration - effect of surface hydrodynamics and reversed membrane morphology

被引:32
作者
Gan, Q [1 ]
机构
[1] Queens Univ Belfast, Sch Chem Engn, Belfast BT9 5AG, Antrim, North Ireland
关键词
beer microfiltration; pulsatile flow; helical low; backflushing; reversed membrane morphology;
D O I
10.1016/S0255-2701(00)00127-6
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The separation characteristics in beer microfiltration is based on a fine balanced retention of particles (yeast cells, debris, and coagulated protein-polyphenol complexes) and transmission of dissolved macromolecules (proteins, carbohydrates, colour and flavour compounds) to achieve beer clarification whilst preserving the 'wholesome' quality of the filtered beer. The required porous transmission of large amount of macromolecular species led to an unavoidable and complex membrane fouling in terms of fouling constituents, formation and structure, which are the major obstacles to obtaining an economically viable flux and consistent permeate quality. This paper describes an experimental study of beer clarification by cross-flow microfiltration with the aim of increasing a low permeation rate to an economically acceptable level by employing and optimising some flux-enhancement techniques. These include, (i) modification of bulk feed flow hydrodynamic conditions by superimposing a helical-flow pattern and a two-way reversing flow pulsation; (ii) application of an automated high frequency backflush programme with controllable frequency and backpulse strength; and (iii) filtration at reversed membrane morphology to allow the open substructure of the asymmetric ceramic membrane (Ceramem) to face the feed flow and thereby a reversed transmembrane pressure (TMP) gradient. The increased bulk-flow turbulence generated by flow pulsation was found disappointingly ineffective, and the superimposed helical flow pattern was only marginally better. The backflush technique was a more effective method and application of an optimised backflush programme at normal cross-flow conditions achieved 410% flux increase. The most dramatic flux improvement was achieved when the filtration was carried out with high frequency backflush at a reversed membrane mounting configuration. The author attributed the large flux increase to a mechanism of reversible 'particle holding and releasing' by the open sub-structure of the membrane under the influence of high frequency backflush, which greatly reduced fouling in the critical membrane phase. (C) 2001 Elsevier Science B.V. AM rights reserved.
引用
收藏
页码:413 / 419
页数:7
相关论文
共 23 条
[1]   The effect of oscillatory flow on crossflow microfiltration of beer in a tubular mineral membrane system - Membrane fouling resistance decrease and energetic considerations [J].
Blanpain-Avet, P ;
Doubrovine, N ;
Lafforgue, C ;
Lalande, M .
JOURNAL OF MEMBRANE SCIENCE, 1999, 152 (02) :151-174
[2]   PROPERTIES OF MICROFILTRATION MEMBRANES .2. ADSORPTION OF BOVINE SERUM-ALBUMIN AT ALUMINUM-OXIDE MEMBRANES [J].
BOWEN, WR ;
HUGHES, DT .
JOURNAL OF MEMBRANE SCIENCE, 1990, 51 (1-2) :189-200
[3]  
*BRAUER GETR RUND, 1991, AN EBC EUR BREW CONV
[4]  
BURRELL KJ, 1994, MBAA TECH Q, V31, P42
[5]  
COURANT E, 1994, ICHEME FOOD PROCESS
[6]  
CZECH B, 1995, BREWER, V81, P103
[7]   Permeate flow in hexagonal 19-channel inorganic membrane under filtration and backflush operating modes [J].
Dolecek, P ;
Cakl, J .
JOURNAL OF MEMBRANE SCIENCE, 1998, 149 (02) :171-179
[8]   Charge effects on inorganic membrane performance in a cross-flow microfiltration process [J].
Elzo, D ;
Huisman, I ;
Middelink, E ;
Gekas, V .
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 1998, 138 (2-3) :145-159
[9]  
FILLAUDEAU L, 1999, EBC C CANN, P823
[10]  
FREEMAN GJ, 1995, FERMENTED BEVERAGE P