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Biodiesel production by enzymatic process using Jatropha oil and waste soybean oil

Authors
Lee, Ja HyunKim, Sung BongYoo, Hah YoungSuh, Young JoonKang, Gyung BoJang, Woo InKang, JongwonPark, ChulhwanKim, Seung Wook
Issue Date
Jul-2013
Publisher
KOREAN SOC BIOTECHNOLOGY & BIOENGINEERING
Keywords
biodiesel; continuous process; lipase; response surface methodology; optimization
Citation
BIOTECHNOLOGY AND BIOPROCESS ENGINEERING, v.18, no.4, pp.703 - 708
Indexed
SCIE
SCOPUS
KCI
Journal Title
BIOTECHNOLOGY AND BIOPROCESS ENGINEERING
Volume
18
Number
4
Start Page
703
End Page
708
URI
https://scholar.korea.ac.kr/handle/2021.sw.korea/102930
DOI
10.1007/s12257-012-0805-8
ISSN
1226-8372
Abstract
In this study, non-edible Jatropha oil and postcooking waste soybean oil were utilized for enzymatic biodiesel production. The process was optimized by using a statistical method. In addition, a novel continuous process using co-immobilized Rhizopus oryzae and Candida rugosa lipases was developed. The optimum conditions for the batch process were determined to be a reaction temperature of 45oC, an agitation speed of 250 rpm, 10 wt% of water, and 20% of immobilized lipases. A conversion of about 98% at 4 h could be achieved for biodiesel production using Jatropha oil, while a conversion of about 97% at 4 h was achieved from waste soybean oil. A packed bed reactor charged with co-immobilized lipases was employed for continuous biodiesel production from Jatropha and waste soybean oil. The reactor consisted of a jacketed glass column (ID 25 mm x 130 mm), in which a temperature of 45A degrees C was maintained by water circulation. A maximum conversion of about 80% in 24 h at a flow rate of 0.8 mL/ min was achieved with the continuous process, whereas in the two-stage continuous process, a conversion of about 90% in 72 h was attained at a flow rate of 0.1 mL/min.
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