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Delignification Kinetics of Alkaline and Ethanol Pretreatment of Broussonetia papyrifera
Received:July 26, 2019  
DOI:10.11981/j.issn.1000-6842.2020.04.15
Key Words:Broussonetia papyrifera;ethanol pretreatment;alkaline pretreatment;delignification;kinetics
Fund Project:国家自然科学基金(21978074,31500496);2016 年大学生创新创业湖北工业大学省级项目(201610500020)。
Author NameAffiliationPostcode
XIONG Long School of Material and Chemical Engineering, Hubei University of Technology, Wuhan, Hubei Province, 430068 430068
TU Hongfeng School of Material and Chemical Engineering, Hubei University of Technology, Wuhan, Hubei Province, 430068 430068
ZHENG Fangke School of Material and Chemical Engineering, Hubei University of Technology, Wuhan, Hubei Province, 430068 430068
YAO Lan School of Material and Chemical Engineering, Hubei University of Technology, Wuhan, Hubei Province, 430068 430068
XIE Yimin School of Material and Chemical Engineering, Hubei University of Technology, Wuhan, Hubei Province, 430068 430068
YANG Haitao School of Material and Chemical Engineering, Hubei University of Technology, Wuhan, Hubei Province, 430068 430068
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Abstract:
      The kinetic characteristics of delignification of Broussonetia papyrifera pretreated by sodium hydroxide and ethanol were analyzed in this study to compare their differences in delignification rate and activation energy. Results showed that delignification reactions during alkaline and ethanol pretreatment were a first order reaction. There were two delignification stages during both pretreatment processes, i.e., bulk delignification and supplement delignification. During the pretreatments with alkaline and ethanol, it entered the supplementary delignification stage as the temperatures were higher than 130℃ and 150℃, respectively. The delignification rate was increased with the increase of pretreatment temperature, and the delignification rate in the bulk delignification stage was higher than that of the supplementary delignification stage. Comparing the delignification kinetics of the two pretreatment processes, it was found that the delignification rates were almost the same at low temperature, while the delignification rate of the alkali pretreatment was slightly higher than that of the ethanol pretreatment at medium and high temperature. It was also found that the activation energies of alkaline and ethanol pretreatments were 100.2 kJ/mol and 82.3 kJ/mol respectively in bulk delignification stages, which indicated that in present study, lignin was easier to be removed during ethanol pretreatment process.
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