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Title: Fluidized-bed immobilized-enzyme reactor for the hydrolysis of cornstarch to glucose

Journal Article · · Biotechnol. Bioeng.; (United States)

We have developed an economical fluidized-bed immobilized-enzyme cornstarch hydrolysis reactor employing an inexpensive glucoamylase-on-alumina (covalently bonded) catalyst having a high initial activity (130 units/g) and excellent long term stability (t/sub 1/2/ = 6450 hr at 50/sup 0/C). The reactor can give higher yields of dextrose from streams containing approx.30% (wt) low dextrose equivalent (DE) cornstarch than can a comparable fixed-bed reactor because its design exploits the fact that fluidization permits the use of very small catalyst particles (down to 50 ..mu..m in our case) which overcomes the yield-limiting diffusion-associated problems encountered in the use of conventional fixed-bed cornstarch hydrolysis reactors. Furthermore, even when small catalyst particles are used, the fluidized-bed reactor does not suffer from plugging and high pressure drop problems typical of fixed-bed reactors. The results of an initial economic analysis based on bench-scale results indicate that the processing cost for a plant using this new technology to produce 100 x 10/sup 6/ lb dextrose/year from low DE cornstarch would be as much as 33% lower than for a comparable plant employing conventional soluble-enzyme technology.

Research Organization:
Lehigh Univ., Bethlenem, PA
OSTI ID:
6295128
Journal Information:
Biotechnol. Bioeng.; (United States), Vol. 21:4
Country of Publication:
United States
Language:
English