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Received November 10, 2011
Accepted August 14, 2012
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Lipase from Penicillium camembertii KCCM 11268: Optimization of solid state fermentation and application to biodiesel production
Waraporn Malilas1 2
Seong Woo Kang1
Sung Bong Kim1
Hah Young Yoo1
Warawut Chulalaksananukul2
Seung Wook Kim1†
1Department of Chemical and Biological Engineering, Korea University, 1, Anam-dong, Sungbuk-gu, Seoul 136-701, Korea 2Department of Botany, Faculty of Science, Chulalongkorn University, Bangkok, Thailand
kimsw@korea.ac.kr
Korean Journal of Chemical Engineering, February 2013, 30(2), 405-412(8), 10.1007/s11814-012-0132-y
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Abstract
Lipase was produced by Penicillium camembertii KCCM 11268 under solid state fermentation (SSF), and the production process was optimized by using statistical experimental designs. The initial moisture content, cultivation time, inoculum size and concentration of basal medium were considered as the factors of optimum conditions for SSF. P. camembertii KCCM 11268 was cultivated in SSF using wheat bran as the substrate for lipase production. Under the optimized condition, lipase activity was reached around 7.8 U/ml after eight days fermentation. To partially purify the lipase, ammonium sulfate (80% saturation) was added to the crude lipase solution and concentrated using a diafiltration (VIVAFLOW 50). The concentrated lipase solution from P. camembertii KCCM 11268 (PCL) was immobilized on silica gel by cross-linking method. Also, PCL was mixed with a commercial lipase solution from Candida rugosa (CRL), and this mixture was co-immobilized on silica gel. The immobilized and co-immobilized lipase activities were 1150.1 and 7924.8 U/g matrix, respectively. Palm oil and methanol were used as substrates and 1mmol of methanol was added every 1.5 h and 2 times during biodiesel production. The reaction was carried out at temperatures of 30, 40, 50, 60 and 70 ℃. The maximum biodiesel conversion by co-immobilized lipase was 99% after 5 h at 50 ℃.
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References
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Oda M, Kaieda M, Mana S, Yamaji H, Kondo A, Izumoto E, Fukuda H, Biochem. Eng. J., 45-51, 23 (2005)
Lee JH, Kim SB, Park C, Tae B, Han SO, Kim SW, Biochem. Biotehcnol., 365-371, 161 (2010)
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Shieh CJ, Liao HF, Lee CC, Bioresour. Technol., 103-106, 88 (2003)
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Neilsen PM, Brask J, Fjerbaek L, Biotechnol. Bioeng., 692-700, 110 (2008)
Lee DH, Kim JM, Shin HY, Kim SW, Biotechnol. Bioprocess Eng., 522-525, 11 (2006)
Hsu AF, Jones K, Fogolia TA, Marmer WM, Biotechnol.Appl. Biochem., 181-186, 36 (2002)
Shweta S, Shweta S, Gupta MN, Energy Fuels., 154-159, 18 (2004)
Lee JH, Kim SB, Park C, Kim SW, Bioresour. Technol., s66-s70, 101 (2010)
Lee JH, Kim SB, Kang SW, Song YS, Park C, Kim SW, Bioresour. Technol., 2105-2108, 102 (2011)
Cordova J, Nemmaoui M, Ismaili-Alaoui M, Morin A, Roussos S, Raimbault M, Benjilali B, J. Mol. Catal. B Enzymatic., 5, 75 (1998)
Lee JH, Lee DH, Lim JS, Um BH, Park C, Kim SW, J. Microbiol. Biotechnol., 18, 1927 (2008)
Kim SB, Lee JH, Oh KK, Lee SJ, Lee JY, Kim JS, Kim SW, Biotechnol. Biopro. Eng., 16, 725 (2011)
Sunitha K, Lee JK, Oh TK, Bioproc. Eng., 21, 477 (1999)
Um BH, Bae SH, Korean J. Chem. Eng., 28(5), 1172 (2011)
Li J, Liu L, Wu J, Sun J, Du G, Chen J, Tao W, Korean J. Chem. Eng., 27(4), 1233 (2010)
Amrane A, Prstel V, Prigent Y, J. Gen. Appl. Microbiol., 251-5, 49 (2003)
Torabi SF, Khajeh K, Ghasempur S, Ghaemi N, Siadat SOR, J. Biotechnol., 111-20, 131 (2007)
Gupta R, Rathi P, Bradoo S, Crit. Rev. Food Sci. Nutr., 635-44, 43 (2003)
Krishna HS, Karanth GN, Catal. Rev., 499-591, 44 (2002)
Lifka J, Ondruschka B, Chem. Eng. Technol., 1156-9, 27 (2004)