Radial flow tubular membrane bioreactor for enhanced enzymatic hydrolysis of lignocellulosic waste biomass

被引:5
|
作者
Al-Mardeai, Saleha [1 ]
Elnajjar, Emad [2 ]
Hashaikeh, Raed [3 ]
Kruczek, Boguslaw [4 ]
Van der Bruggen, Bart [5 ]
Al-Zuhair, Sulaiman [1 ]
机构
[1] UAE Univ, Chem & Petr Engn, Al Ain 15551, U Arab Emirates
[2] UAE Univ, Mech Engn, Al Ain 15551, U Arab Emirates
[3] New York Univ Abu Dhabi, Mech Engn, Abu Dhabi, U Arab Emirates
[4] Univ Ottawa, Chem & Biol Engn, Ottawa, ON, Canada
[5] Katholieke Univ Leuven, Dept Chem Engn, Heverlee, Belgium
关键词
Enzymatic hydrolysis; Kinetic model; Membrane bioreactor; Product inhibition; Product separation; DATE SEED; SIMULTANEOUS SACCHARIFICATION; CELLULOSE; FERMENTATION; PRETREATMENT; TECHNOLOGY; CONVERSION; REACTOR; DESIGN;
D O I
10.1016/j.fuel.2023.127648
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A tubular membrane bioreactor was used for enhanced enzymatic hydrolysis of waste biomass, palm date seeds. The bioreactor successfully handled high solid loadings with effective simultaneous product removal. The effects of substrate concentrations, 14.3, 21.4, and 39.6 g/L, and water flowrates, 0.4, 0.8, and 1.2 mL/min, on the production of total reducing sugars were examined. At substrate concentration of 21.4 g/L, the total reducing sugars yield increased from 28.9 % to 42.7 % after 8 h as the water flowrate increased from 0.4 to 1.2 mL/min. Substrate inhibition was observed at the highest tested substrate concentration of 39.6 g/L. A dynamic model was developed to describe the designed bioreactor, accounting for the simultaneous product separation and the dynamic changes in substrate structure. The nonhydrolyzable substrate fraction parameter was found to significantly affect the model prediction. The novel membrane bioreactor and the developed model enable the industrial valorization of lignocellulosic biomass for bioethanol production.
引用
收藏
页数:10
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