4.7 Article

One-step direct transesterification of wet yeast for biodiesel production catalyzed by magnetic nanoparticle-immobilized lipase

Journal

RENEWABLE ENERGY
Volume 171, Issue -, Pages 11-21

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.renene.2021.02.065

Keywords

Direct transesterification; Biodiesel; Immobilized lipase; Magnetic nanomaterials; Saitozyma podzolica; Burkholderia pyrrolica

Funding

  1. Sichuan Science and Technology Program [2020YJ0304, 2020YFH0076, 2020YJ0305, 2018NZ0007]
  2. National Natural Science Foundation of China [32071479]

Ask authors/readers for more resources

A method for direct transesterification of wet yeast using immobilized lipase was developed in this study, which improved the efficiency of biodiesel production. The immobilized lipase covalently cross-linked with Fe3O4@SiO2-CHO showed high enzyme activity and immobilization rate. The optimal temperature for the immobilized lipase was 60 degrees C, and it still retained 80% activity after storage.
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 degrees 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 degrees C and 40 degrees C. The immobilized enzyme still had 80% enzymatic activity after 48 d storage at 4 degrees 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 degrees 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. (C) 2021 Elsevier Ltd. All rights reserved.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.7
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available