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作 者:A. O. Okewale P. K. Igbokwe K. A. Babayemi
机构地区:[1]Department of Chemical Engineering, Federal University of Petroleum Resources, Effurun, Nigeria [2]Department of Chemical Engineering, Nnamdi Azikiwe University, Awka, Nigeria [3]Department of Chemical Engineering, Anambra State University, Uli, Nigeria
出 处:《Advances in Chemical Engineering and Science》2015年第2期152-157,共6页化学工程与科学期刊(英文)
摘 要:This use of biomass-based adsorbent has been explored for the column study of the adsorptive dehydration of water in ethanol-water mixtures. The column study was carried out using enzyme modified corn starch and the breakthrough curve parameters were used to design the packed bed column. The effect of flow rate on the breakthrough curves revealed that adsorption efficiency decreased with increased inflow rate. The empty bed contact time (τ) of the pilot plant packed column was 35.35 min while the breakthrough time is 40.78 min. 66.7% was the fraction of capacity left unused for the pilot plant from the design.This use of biomass-based adsorbent has been explored for the column study of the adsorptive dehydration of water in ethanol-water mixtures. The column study was carried out using enzyme modified corn starch and the breakthrough curve parameters were used to design the packed bed column. The effect of flow rate on the breakthrough curves revealed that adsorption efficiency decreased with increased inflow rate. The empty bed contact time (τ) of the pilot plant packed column was 35.35 min while the breakthrough time is 40.78 min. 66.7% was the fraction of capacity left unused for the pilot plant from the design.
关 键 词:ENZYME Modified CORNSTARCH DESIGN Fixed Column BREAKTHROUGH Curve DEHYDRATION ETHANOL-WATER Mixtures
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