Poly(3-Hydroxybutyrate) Production in Repeated fed-Batch with Cell Recycle Using a Medium with low Carbon Source Concentration
详细信息    查看全文
  • 作者:Jaciane Lutz Ienczak ; Mélodi Schmidt…
  • 关键词:Cell recycle ; Cross flow filtration ; Low carbon source concentration ; Poly(3 ; hydroxybutyrate) ; Repeated fed ; batch.
  • 刊名:Applied Biochemistry and Biotechnology
  • 出版年:2016
  • 出版时间:January 2016
  • 年:2016
  • 卷:178
  • 期:2
  • 页码:408-417
  • 全文大小:387 KB
  • 参考文献:1.Anderson, A. J., & Dawes, E. A. (1990). Occurrence, metabolism, metabolic role, end industrial uses of bacterial polyhydroxyalkanoates. Microbiol Reviews, 54(4), 450–472.
    2.Riesenberg, D., & Guthke, R. (1999). High-cell-density cultivation of microorganisms. Applied Microbiology and Biotechnology, 51, 422–430.CrossRef
    3.Ienczak, J. L., Quines, L. K., Melo, A. A., Brandellero, M., Mendes, C. R., Schmidell, W., & Aragão, G. M. F. (2011). High cell density strategy for poly(3-hydroxybutyrate) production by Cupriavidus necator. Brazilian Journal of Chemical Engineering, 28, 585–596.
    4.Marangoni, C., Furigo Jr., A., & Aragão, G. M. F. (2002). Production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) by Ralstonia eutropha in whey and inverted sugar with propionic acid feeding. Process Biochemistry, 38, 137–141.CrossRef
    5.Aragão, G. M. F., Schmidell, W., Ienczak, J. L., Schmidt, F. C., Dalcanton, F., Fiorese, M. L., Rodrigues, R., Deucher, R., & Marangoni, C. (2009). Preparation of polyhydroxyalkanoates from a citric residue. International Application Published Under the Patent Cooperation Treaty (PCT), WO2009/149529 A1.
    6.Delgenes, J. P., Escare, M. C., Laplace, J. M., Moletta, R., & Navarro, J. M. (1998). Biological production of industrial chemicals, i.e. xylitol and ethanol, from lignocelluloses by controlled mixed culture systems. Ind. Crop Prod., 7, 101–111.CrossRef
    7.Santos, S. C., Rosa, P. R. F., Sakamoto, I. K., Varesche, M. B. A., & Silva, E. L. (2014). Hydrogen production from diluted and raw sugarcane vinasse under thermophilic anaerobic conditions. Interntional Journal of Hydrogen Energy, 39, 9599–9610.CrossRef
    8.Khanna, S., & Srivastava, A. K. (2005). Repeated fed-batch cultivation of Ralstonia eutropha for poly(β-hydroxybutyrate) production. Biotechnology Letters, 27, 1401–1403.CrossRef
    9.Ibrahim, M. H. A., & Steinbüchel, A. (2010). High-cell-density cyclic fed-batch fermentation of a poly(3-hydroxybutyrate)-accumulating thermophile, Chelatococcus sp. Strain MW10. Applied and Enviromental Microbiology, 76, 7890–7895.CrossRef
    10.Ahn, W. S., Park, S. J., & Lee, S. Y. (2001). Production of poly(3-hydroxybutyrate) from whey by cell recycle fed-batch culture of recombinant Escherichia coli. Biotechnolgy Letters., 23, 235–240.CrossRef
    11.Pinto, M. A., & Immanuel, C. D. (2005). Modelling and bifurcation studies os a two-stage continuous bioreactor for the production of poly-ß-hydroxybutyrate (PHB). Aiche Annual Meeting.
    12.Lambrechts, T., Papantoniou, I., Sonnaert, M., Schrooten, J., & Aerts, J. M. (2014). Model-based cell number quantification using online single-oxygen sensor data for tissue engineering perfusion bioreactors. Biotechnology and Bioengineering, 111, 1982–1992.CrossRef
    13.Brandl, H., Gross, R. A., Lenz, R. W., & Fuller, R. C. (1998). Pseudomonas oleovorans as a source of poly(β-hydroxyalkanoates) for potential applications as biodegradable polyesters. Applied and Enviromental Microbiology, 54, 1977–1982.
    14.Taguchi, H., & Humphrey, A. (1966). Dynamic measurement of the volumetric oxygen transfer coefficient in fermentation systems. Journal of Fermentation Technology, 44, 881–889.
    15.Pirt, S. J. (1975). Principles of microbe and cell cultivations. Oxford: Blackwell.
    16.Ryu, H. W., Hahn, S. K., Chang, Y. K., & Chang, H. N. (1997). Production of poly(3-hydroxybutyrate) by high cell density fed-batch culture of Alcaligenes eutrophus with phosphate limitation. Biotechnology and Bioengineering, 55(1), 25–32.CrossRef
    17.Khanna, S., & Srivastava, A. K. (2008). Continuous production of poly-β-hydroxybutyrate by high-cell-density cultivation of Wautersia eutropha. Journal of Chemical Technology & Biotechnology, 83, 799–805.CrossRef
    18.Shang, L., Jiang, M., & Chang, H. N. (2003). Poly(3-hydroxybutyrate) synthesis in fed-batch culture of Ralstonia eutropha with phosphate limitation under different glucose concentrations. Biotechnology Letters, 25, 1415–1419.CrossRef
    19.Davis, R., Duane, G., Kenny, S. T., Cerrone, F., Guzik, M. W., Babu, R. P., Casey, E., & O’Connor, K. E. (2015). High cell density cultivation of Pseudomonas putida KT2440 using glucose without the need for oxygen enriched air supply. Biotechnology and Bioengineering, 112, 725–733.CrossRef
    20.Atlié, A., Koller, M., Scherzer, D., Kutschera, C., Grillo-Fernandes, E., Horvat, P., Chiellini, E., & Braunegg, G. (2011). Continuous production of poly([R]-3-hydroxybutyrate) by Cupriavidus necator in a multistage bioreactor cascade. Applied and Enviromental Microbiology, 91, 295–304.
    21.Cesário, M. T., Rapose, R. S., Almeida, M. C. M. D., Keulen, F. V., Ferreira, B. S., & Fonseca, M. M. R. (2014). Enhanced bioproduction of poly-3-hydroxybutyrate from wheat straw lignocellulosic hydrolysates. New Biotechnology, 31, 104–113.CrossRef
  • 作者单位:Jaciane Lutz Ienczak (1)
    Mélodi Schmidt (2)
    Luci Kelin Quines (2)
    Kellen Zanfonato (2)
    José Geraldo da Cruz Pradella (1)
    Willibaldo Schmidell (2)
    Glaucia Maria Falcao de Aragao (2)

    1. Laboratório Nacional de Ciência e Tecnologia do Bioetanol (CTBE), Centro Nacional de Pesquisa em Energia e Materiais (CNPEM), PO box 6192, Campinas, SP, CEP 13083-970, Brazil
    2. Department of Chemical Engineering and Food Engineering, Federal University of Santa Catarina, UFSC, PO Box 476, Florianópolis, SC, CEP 88040-900, Brazil
  • 刊物类别:Chemistry and Materials Science
  • 刊物主题:Chemistry
    Biotechnology
    Biochemistry
  • 出版者:Humana Press Inc.
  • ISSN:1559-0291
文摘
Among approaches applied to obtain high productivity and low production costs in bioprocesses are high cell density and the use of low cost substrates. Usually low cost substrates, as waste/agroindustrial residues, have low carbon concentration, which leads to a difficulty in operating bioprocesses. Real time control of process for intracellular products is also difficult. The present study proposes a strategy of repeated fed-batch with cell recycle to attain high cell density of Cupriavidus necator and high poly(3-hydroxybutyrate) (P(3HB)) productivity, using a substrate with low carbon source concentration (90 g l−1). Also, the use of the oxygen uptake rate data was pointed out as an on line solution for process control, once P(3HB) is an intracellular product. The results showed that total biomass (X), residual biomass (Xr) and P(3HB) values at the end of the culture were 61.6 g l−1, 19.3 g l−1 and 42.4 g l−1 respectively, equivalent to 68.8 % of P(3HB) in the cells, and P(3HB) productivity of 1.0 g l−1 h−1. Therefore, the strategy proposed was efficient to achieve high productivity and high polymer content from a medium with low carbon source concentration. Keywords Cell recycle Cross flow filtration Low carbon source concentration Poly(3-hydroxybutyrate) Repeated fed-batch.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700