We have used a cellulose acetate, hollow-fibre (HF) ultrafiltration me
mbrane to refold bovine carbonic anhydrase, loaded into the lumen spac
e, by removing the denaturant through controlled dialysis via the shel
l side space. When challenged with GdnHCl-denatured carbonic anhydrase
, 70% of the loaded protein reptated through the membrane into the cir
culating dialysis buffer. Reptation occurred because the protein, in i
ts fully unfolded configuration, was able to pass through the pores. T
he loss of carbonic anhydrase through the membrane was controlled by t
he dialysis conditions. Dialysis against 0.05 M Tris-HCl for 30 min re
duced the denaturant around the protein to a concentration that allowe
d the return of secondary structure, increasing the hydrodynamic radiu
s, thus preventing protein transmission. Under these conditions a maxi
mum of 42% of carbonic anhydrase was recovered (from a starting concen
tration of 5 mg/mL) with 94% activity. This is an improvement over ref
olding carbonic anhydrase by simple batch dilution, which gave a maxim
um reactivation of 85% with 35% soluble protein yield. The batch refol
ding of carbonic anhydrase is very sensitive to temperature; however,
during HF refolding between 0 and 25 degrees C the temperature sensiti
vity was considerably reduced. In order to reduce the convection force
s that give rise to aggregation and promote refolding the dialyzate wa
s slowly heated from 4 to 25 degrees C. This slow, temperature-control
led refolding gave an improved soluble protein recovery of 55% with a
reactivation yield of 90%. The effect of a number of additives on the
refolding system performance were tested: the presence of PEG improved
both the protein recovery and the recovered activity from the membran
e, while the detergents Tween 20 and IGEPAL CA-630 increased only the
refolding yield. (C) 1998 John Wiley & Sons, Inc.