Several carrier materials were examined for endoinulinase immobilization. A
polystyrene carrier material (UF93(R)) gave the best immobilization capaci
ty (217 units/g carrier) and operational stability. Carbohydrate compositio
ns in the reaction product were quite similar irrespective of the support m
aterials even though each carrier material has different pore structure ass
ociated with diffusional restriction. After immobilization the optimal pH f
or enzyme activity was shifted from 5.0 to 4.5, whereas optimal temperature
(55 degrees C) was unaltered. Continuous production of inulo-oligosacchari
des from chicory juice was carried out using the polystyrene-bound endoinul
inase. The recommended operating conditions of the enzyme reactor for maxim
izing productivity were as follows: feed concentration, 100 g/l chicory jui
ce; flow rate, as superficial space velocity 2.0 h(-1); temperature, 55 deg
rees C. The enzyme reactor was run for 28 days at 55 degrees C achieving an
oligosaccharide yield of 82% without any significant loss of initial enzym
e activity, where the volumetric productivity was 200 g/l . h. Furthermore,
there was no marked difference in operational stability between the two re
actors fed with pure inulin solution and with chicory juice as a substrate
even though chicory juice contains a lot of impurities.