Q. Gan et al., Beer clarification by microfiltration - product quality control and fractionation of particles and macromolecules, J MEMBR SCI, 194(2), 2001, pp. 185-196
Beer clarification by microfiltration demands a finely balanced retention o
f colloidal particulates (yeast cells, chill haze flocs, etc.) and transmis
sion of soluble macromolecules including carbohydrates, proteins, flavour,
and colour compounds which give the "whole some" quality of a beer. The req
uired porous transmission of these macromolecular species led to an unavoid
able, complex and dynamic in-pore membrane fouling in terms of fouling cons
tituents, formation, structure and kinetics, which are the main obstacles i
n obtaining an economically viable flux and consistency in permeate quality
.
This experimental study was carried out with the aims of understanding the
dynamic inter-relation between flux, fouling and system selectivity during
a cross-flow beer microfiltration process so that an effective operating st
rategy for flux optimisation could be formulated in conjunction with the pa
rallel objective of good product (permeate) quality control. Tubular cerami
c membranes (Ceramem) with nominal pore diameters of 0.2, 0.5, and 1.3 mum
were used. Simultaneous measurement of flux and permeate qualities, such as
specific gravity and chill haze level enabled identification of the effect
of anti-fouling techniques, such as backflushing on transmission of essent
ial beer components and on the filtered beer quality. The experimental evid
ence lead to an understanding that the drastic flux enhancement achieved by
employing backflushing at reversed membrane morphology was associated with
enhanced solute transmission which could, without careful control, upset a
balanced transmission of essential beer components and the retention of un
wanted "chill haze" components. Further operating parameters and varying sy
stem configurations were investigated over their effect on both flux perfor
mance and system selectivity. These include membrane pore size, filtration
temperature, and the addition of an amorphous silica particles as coagulati
on agent for hydrophilic proteins. (C) 2001 Elsevier Science B.V. All right
s reserved.