Apart from considerations for hygienic operation, membrane cleaning is esse
ntial to maintain consistent permeability and selectivity of membrane syste
ms for clarifying beer and beverages where balanced fractionation of partic
les/macromolecules is necessary. Experiments involved formulating and optim
ising chemical cleaning methods for a ceramic microfiltration membrane, whi
ch had been severely fouled during clarification of a commercial beer. The
cleaning processes employed NaOH, HNO3, H2O2, and Ultrasil 11 as the chemic
al cleaning agents. The cleaning ability and cleaning kinetics of the proce
sses were evaluated in parallel with the study of the fouling mechanism, fo
rmation and strength so as to elucidate the synergetic relationship between
fouling and cleaning. A three-step cleaning mechanism was postulated. This
led to the development of a fast and effective combined simultaneous caust
ic cleaning and oxidation method (CSCCO), which was able to restore 87% of
the original membrane's water permeability within 8 min. Analysis suggested
the concept of a cleaning energy barrier E-c and a cleaning rate constant
k(c0). This study confirmed the existence of a synergetic relationship betw
een the prior fouling and optimum formulation of cleaner and optimal cleani
ng condition. The study varied beer filtration conditions. Transmembrane pr
essure (TMP) and crossflow velocity during fouling appeared to have a minim
al effect on the membrane's subsequent cleanability, especially when the po
werful CSCCO process was employed. The number of previous fouling/ cleaning
cycles was influential. A complete removal of the residual fouling, formed
on the virgin membrane's surface proved beyond the means of the harsh chem
ical cleaning used under any conditions, The degree of residual fouling eve
ntually reached a plateau and a level of 87% of the original water flux cou
ld be restored repeatedly. (C) 1999 Elsevier Science B.V. All rights reserv
ed.