期刊论文详细信息
Biotechnology for Biofuels
Combining phospholipases and a liquid lipase for one-step biodiesel production using crude oils
Silvia Cesarini2  Rune Falkenberg Haller3  Pilar Diaz1  Per Munk Nielsen2 
[1] Department of Microbiology, University of Barcelona, Avenida Diagonal 643, Barcelona 08028, Spain
[2] Department of Bioenergy Opportunities, Novozymes A/S, Krogshoejvej 36, Bagsvaerd 2880, Denmark
[3] Department of Analytical Development, Novozymes A/S, Hallas Alle 1, Kalundborg 4400, Denmark
关键词: Phospholipases;    Crude oils;    Liquid lipase;    Enzymatic biodiesel;   
Others  :  793459
DOI  :  10.1186/1754-6834-7-29
 received in 2013-10-23, accepted in 2014-02-10,  发布年份 2014
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【 摘 要 】

Background

Enzymatic biodiesel is becoming an increasingly popular topic in bioenergy literature because of its potential to overcome the problems posed by chemical processes. However, the high cost of the enzymatic process still remains the main drawback for its industrial application, mostly because of the high price of refined oils. Unfortunately, low cost substrates, such as crude soybean oil, often release a product that hardly accomplishes the final required biodiesel specifications and need an additional pretreatment for gums removal. In order to reduce costs and to make the enzymatic process more efficient, we developed an innovative system for enzymatic biodiesel production involving a combination of a lipase and two phospholipases. This allows performing the enzymatic degumming and transesterification in a single step, using crude soybean oil as feedstock, and converting part of the phospholipids into biodiesel. Since the two processes have never been studied together, an accurate analysis of the different reaction components and conditions was carried out.

Results

Crude soybean oil, used as low cost feedstock, is characterized by a high content of phospholipids (900 ppm of phosphorus). However, after the combined activity of different phospholipases and liquid lipase Callera Trans L, a complete transformation into fatty acid methyl esters (FAMEs >95%) and a good reduction of phosphorus (P <5 ppm) was achieved. The combination of enzymes allowed avoidance of the acid treatment required for gums removal, the consequent caustic neutralization, and the high temperature commonly used in degumming systems, making the overall process more eco-friendly and with higher yield. Once the conditions were established, the process was also tested with different vegetable oils with variable phosphorus contents.

Conclusions

Use of liquid lipase Callera Trans L in biodiesel production can provide numerous and sustainable benefits. Besides reducing the costs derived from enzyme immobilization, the lipase can be used in combination with other enzymes such as phospholipases for gums removal, thus allowing the use of much cheaper, non-refined oils. The possibility to perform degumming and transesterification in a single tank involves a great efficiency increase in the new era of enzymatic biodiesel production at industrial scale.

【 授权许可】

   
2014 Cesarini et al.; licensee BioMed Central Ltd.

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【 参考文献 】
  • [1]Dizge N, Aydiner C, Imer DY, Bayramoglu M, Tanriseven A, Keskinlera B: Biodiesel production from sunflower, soybean, and waste cooking oils by transesterification using lipase immobilized onto a novel microporous polymer. Bioresour Technol 2009, 100(6):1983-1991.
  • [2]Fjerbaek L, Christensen KV, Norddahl B: A review of the current state of biodiesel production using enzymatic transesterification. Biotechnol Bioeng 2009, 102(5):1298-1315.
  • [3]Ghaly AE, Dave D, Brooks MS, Budge S: Production of biodiesel by enzymatic transesterification: review. Am J Biochem Biotechnol 2010, 6(2):54-76.
  • [4]Kaieda M, Samukawa T, Matsumoto T, Ban K, Kondo A, Shimada Y, Noda H, Nomoto F, Ohtsuka K, Izumoto E, Fukuda H: Biodiesel fuel production from plant oil catalyzed by Rhizopus oryzae lipase in a water-containing system without an organic solvent. J Biosci Bioeng 1999, 88(6):627-631.
  • [5]Kawakami K, Oda Y, Takahashi R: Application of a Burkholderia cepacia lipase-immobilized silica monolith to batch and continuous biodiesel production with a stoichiometric mixture of methanol and crude Jatropha oil. Biotechnol Biofuels 2011, 4(1):42. BioMed Central Full Text
  • [6]Watanabe Y, Shimada Y, Sugihara A, Tominaga Y: Conversion of degummed soybean oil to biodiesel fuel with immobilized Candida antarctica lipase. J Mol Catal B Enzym 2002, 17(3–5):151-155.
  • [7]Robles-Medina A, González-Moreno PA, Esteban-Cerdán L, Molina-Grima E: Biocatalysis: towards ever greener biodiesel production. Biotechnol Adv 2009, 27(4):398.
  • [8]Xu Y, Nordblad M, Nielsen PM, Brask J, Woodley JM: In situ visualization and effect of glycerol in lipase-catalyzed ethanolysis of rapeseed oil. J Molec Catal B 2011, 72(3–4):213-219.
  • [9]Chen X, Du W, Liu D, Ding F: Lipase-mediated methanolysis of soybean oils for biodiesel production. J Chem Technol Biotechnol 2008, 83(1):71-76.
  • [10]Lv D, Du W, Zhang G, Liu D: Mechanism study on NS81006-mediated methanolysis of triglyceride in oil/water biphasic system for biodiesel production. Process Biochem 2010, 45(4):446-450.
  • [11]Cesarini S, Diaz P, Nielsen PM: Exploring a new, soluble lipase for FAMEs production in water-containing systems using crude soybean oil as a feedstock. Process Biochem 2013, 48(3):484-487.
  • [12]Tufvesson P, Lima-Ramos J, Nordblad M, Woodley JM: Guidelines and cost analysis for catalyst production in biocatalytic processes. Org Process Res Dev 2010, 15(1):266-274.
  • [13]Nielsen PM, Brask J, Fjerbaek L: Enzymatic biodiesel production: technical and economical considerations. Eur J Lipid Sci Technol 2008, 110(8):692-700.
  • [14]Nielsen PM: Proceedings of the 104th AOCS Annual Meeting and Expo: April 28-May 1. Montréal, QC; 2013.
  • [15]Hama S, Kondo A: Enzymatic biodiesel production: an overview of potential feedstocks and process development. Bioresour Technol 2013, 135:386-395.
  • [16]Haas M, McAloon A, Yee W, Foglia T: A process model to estimate biodiesel production costs. Bioresour Technol 2006, 97(4):671-678.
  • [17]Encinar JM, Sanchez N, Martinez G, Garcia L: Study of biodiesel production from animal fats with high free fatty acid content. Bioresour Technol 2011, 102(23):10907-10914.
  • [18]Cowan D, Nielsen PM: Enzymatic Degumming Of Edible Oils And Fats. In Bleaching and Purifying Fats and Oils: Theory and Practice. Edited by Patterson HBW. Urbana, IL: AOCS Press; 2009:216-235.
  • [19]Aalrust E, Beyer W, Ottofrickenstein H, Penk G, Plainer H, Reiner R: Enzymatic Treatment of Edible Oils. US Patent: 5,264,367; 1993.
  • [20]Dijstra A: Proceedings of the World Conference on Oilseed Technology and Utilization. Champaign, IL: American Oil Chemists’ Society; 1993.
  • [21]van Nieuwenhuyzen W, Tomás MC: Update on vegetable lecithin and phospholipid technologies. Eur J Lipid Sci Technol 2008, 110(5):472-486.
  • [22]Clausen K: Enzymatic oil-degumming by a novel microbial phospholipase. Eur J Lipid Sci Technol 2001, 103(6):333-340.
  • [23]Holm HC, Nielsen PM, Christensen MW: Production of Fatty Acid Alkyl Esters. US Patent: US 2008/0199924 A1; 2008.
  • [24]Dayton CLG, Galhardo F: Enzymatic Degumming Utilizing a Mixture of PLA and PLC Phospholipases. US Patent: US 2008/0182322 A1; 2008.
  • [25]Pinisetty D, Moldovan D, Devireddy R: The effect of methanol on lipid bilayers: an atomistic investigation. Ann Biomed Eng 2006, 34(9):1442-1451.
  • [26]Daicheng L, Fucui M: Soybean Phospholipids. In Recent Trends for Enhancing the Diversity and Quality of Soybean Products, Volume 22. Edited by Krezhova D. Rijeka: InTech; 2011.
  • [27]Hitchman T: Purifine® PLC: industrial application in oil degumming and refining. Oil Mill Gazetteer 2009, 115:2-4.
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