脂肪酶
酯交换
化学
生物柴油
生物柴油生产
磁性纳米粒子
催化作用
生产(经济)
酵母
纳米颗粒
化学工程
材料科学
有机化学
酶
纳米技术
生物化学
工程类
经济
宏观经济学
作者
Xiyue Cao,Hui Xu,Fosheng Li,Yijun Zou,Yulu Ran,Xiaorui Ma,Yu Cao,Qingrui Xu,Dairong Qiao,Yi Cao
标识
DOI:10.1016/j.renene.2021.02.065
摘要
To develop a method for direct transesterification of wet yeast using immobilized lipase, the oleaginous yeast Saitozyma podzolica Zwy-2-3 and the lipase producing Burkholderia pyrrolica WZ10-3 were used as materials for production of biodiesel. Fe3O4@SiO2-CHO prepared by modifying Fe3O4 with TEOS, APTES and glutaraldehyde. The biocatalysts covalently cross-linked with WZ10-3 lipase by Fe3O4@SiO2-CHO were characterized by FTIR, XRD and TEM. When the enzyme dosage, glutaraldehyde concentration, temperature and time were 30.22 mL, 2.0%, 40 °C and 4 h, the immobilized lipase activity and immobilization rate reached 10038.0 U/g and 96.9%, respectively. The optimum temperatures for immobilized and free lipase were 60 °C and 40 °C. The immobilized enzyme still had 80% enzymatic activity after 48 d storage at 4 °C. The optimized conditions for the direct conversion of immobilized lipase to esterified wet yeast (one-step) were: enzyme dosage 2.5 g, reaction temperature 35 °C; water content 15%; and molar ratio of n-hexane to methanol 3: 1. The transesterification rates of one-step method for oil and biomass were 98.12% and 56.11%, respectively. In contrast, the two-step method was only 88.75% and 51.21%. The immobilized enzyme had 90% enzyme activity after 10 times of reuse.
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