AECI Bioproducts produces lysine by a microbial process utilizing a Co
rynebacterium glutamicum strain. Corn steep liquor is used as the prot
ein source and high test molasses as the carbohydrate source. Lysine i
s recovered from the bio-suspension and subsequently purified using tw
o ion-exchange units. Primary ion-exchange recovers lysine from the bi
o-suspension at a purity of about 97.5%, The eluate is further purifie
d by roughly 1% in secondary ion-exchange to yield a final product of
greater than 98.5% purity. Secondary ion-exchange uses a weak acid cat
ionic resin to remove inorganic impurities. Both unit operations utili
se ISEP(R) carousel ion-exchange units. The rotating chambers constitu
te a continuous bed which is contacted counter-currently with the feed
and elution streams. In actual operation the units proved to be relia
ble and very flexible. Counter-current operation has resulted in reduc
ed resin inventory and increased operating efficiency. Reagent consump
tion is close to stoichiometric and final product concentration is muc
h higher than an equivalent fixed bed system would allow. (C) 1997 Els
evier Science B.V.