The separation of racemic tryptophan analogs has been performed by two ways
: ultrafiltration in a solution system using bovine serum albumin (BSA) as
a free chiral selector and dialysis using BSA grafted nylon membrane. A com
plexation mechanism based on competitive binding of both D- and L-tryptopha
n zwitter-ionic form on the same unprotonated protein site has been used to
predict recovery and purity of both D- and L-tryptophan in the retentate a
nd permeate. The corresponding model gave correct prediction for a large se
t of experimental conditions (pH from 7 to 11, [BSA](0) from 1.5 x 10(-5) t
o 10(-3) M, [L](0)=[D](0) from 10(-4) to 5 x 10(-4) M). The operational par
ameters which can be used to optimize production criteria such as purity, r
ecovery and production rate have been discussed. For enantiomeric separatio
ns using BSA chiral selector (solution system or enantioselective membrane)
, a specific attention has to be taken to both filtration and complexation
parameters. (C) 2000 Elsevier Science B.V. All rights reserved.