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

被引:19
|
作者
Lee, Ja Hyun [1 ]
Kim, Sung Bong [1 ]
Yoo, Hah Young [1 ]
Suh, Young Joon [1 ]
Kang, Gyung Bo [2 ]
Jang, Woo In [2 ]
Kang, Jongwon [2 ]
Park, Chulhwan [3 ]
Kim, Seung Wook [1 ]
机构
[1] Korea Univ, Dept Chem & Biol Engn, Seoul 136701, South Korea
[2] Honam Petrochem Corp, Daedeok Res Inst, Taejon 305726, South Korea
[3] Kwangwoon Univ, Dept Chem Engn, Seoul 139701, South Korea
关键词
biodiesel; continuous process; lipase; response surface methodology; optimization; PACKED-BED REACTOR; FREE FATTY-ACIDS; RHIZOPUS-ORYZAE; CANDIDA-RUGOSA; OPTIMIZATION; PRETREATMENT; CONVERSION; MIXTURE; LIPASE;
D O I
10.1007/s12257-012-0805-8
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
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.
引用
收藏
页码:703 / 708
页数:6
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