Kinetic study on esterification of palmitic acid catalyzed by glycine-based crosslinked protein coated microcrystalline lipase

被引:12
作者
Raita, Marisa [1 ]
Kiatkittipong, Worapon [3 ]
Laosiripojana, Navadol [1 ]
Champreda, Verawat [2 ]
机构
[1] King Mongkuts Univ Technol Thonburi, JGSEE, Bangkok 10140, Thailand
[2] Natl Ctr Genet Engn & Biotechnol, Enzyme Technol Lab, Khlong Luang 12120, Pathum Thani, Thailand
[3] Silpakorn Univ, Dept Chem Engn, Fac Engn & Ind Technol, Nakhon Pathom 73000, Thailand
关键词
Biodiesel; Esterification; Kinetics; Lipase; Palmitic acid; TERT-BUTANOL SYSTEM; BIODIESEL PRODUCTION; IMMOBILIZED LIPASE; BURKHOLDERIA-CEPACIA; OIL; TRANSESTERIFICATION; OPTIMIZATION; ETHANOLYSIS;
D O I
10.1016/j.cej.2015.01.016
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Enzymatic esterification of fatty acid-rich feedstocks represents an efficient and eco-friendly catalytic process for production of biodiesel. In this study, the reaction kinetics on esterification of palmitic acid with methanol using the heterogeneous glycine-based crosslinked protein coated microcrystalline lipase (CL-PCMC-LIP/Gly) was studied. The maximum FAME yield of over 95% based on a molar basis was achieved at 15% (w/w) enzyme dosage with a 4:1 [MeOH]/IFFA] molar ratio after incubation at 50 degrees C for 1 h in the presence of tert-butanol as a co-solvent. According to the rate equation based on the Ping Pong Bi Bi mechanism model with methanol inhibition, the maximum velocity of the reaction was 4.8 x 10(-3) M/min while the Michaelis-Menten's constants for palmitic acid (Km,pA) and methanol (K-m,K-MeOH) were 2.2 M and 1.4 M, respectively with the inhibition constant of methanol (14(i,MeoH)) of 32.6 M. The turnover number (k(cat)) of CL-PCMC-LIP/Gly was 2.7 min(-1) under the optimized experimental condition. The reaction kinetics result provides an important basis for further up-scaling study of the enzymatic esterification process for biodiesel synthesis. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:19 / 23
页数:5
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