Packed bed column과 continuous stirred tank reactor에서 고정화된 glucoamylase의 catalytic activity를 비교하였다. Settling chamber를 이용한 연속애화, 당화 공정을 사용하여 액화된 전분으로부터 포도당을 연속적으로 생산하였다. . Chitin에 고정화된 glucoamylase에 의한 당화실험에 있어서는 dextrin의 농도가 100g/l일 때, 체류시간 20분 동안 20의 당화수율을 나타냈다.
The catalytic activities of immobilized gIucoamylase in a packed bed column and a continuous stirred tank reactor have been compared. Rapid production of glucose from liquefied starch have been studied through, the continuous liquefaction and saccharification using settling chamber. The immobilized glucoamylase with chitin gave the saccharification yield of 20% with the dextrin concentration of 100 g/l in a residence of 20 min. in a packed bed column. The half-life of immobilized glucoamylase with chitin was 19 days. The glucoamyalse immobilized in chitin and encapsulated with Ca-alginate gave the saccharification yield of 6% with the dextrin concentration of 50 g/l in a residence of 20 min. in a packed bed column. The Ca-alginate encapsulated and chitin immobilized glucomylase had a half-life of 25 days, which is 6 day larger than that of the immobilized glucoamylase with chitin only. In continuous liquefaction and saccharification, the glucose yield was 17% for the liquefied starch with naked barley concentration of 50gA in a residence of 20 min.
