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African Journal of Biotechnology

     
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  Afr. J. Biotechnol.

  Vol. 7 No. 18

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  Search Pubmed for articles by:

  Mahammadi M
  Pazouki M

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Scientific Research and Essays
 

African Journal of Biotechnology Vol. 7 (18), pp. 3332–3338, 17 September 2008

ISSN 1684-5315  © 2008 Academic Journals  

 

 

Full Length Research Paper

 

Production of organic acids in an immobilized cell reactor using Propionibacterium acidi-propionici

 

M. Mohammadi1, G.D. Najafpour1*, M. Asadi2, M. Rahimnejad1, S. Najafpour3 M. Pazouki4

 

1Faculty of Chemical Engineering, Noushirvani University of Technology, Babol, Iran.

2Faculty of Civil Engineering, Noushirvani University of Technology, Babol, Iran.

3Ecological Academy of Caspian Sea P.O.Box 961, Sari, Iran.

4Environment Group, Department of Energy, Materials and Energy Research Center, Karaj, Iran.

 

*Corresponding author. E-mail: najafpour@nit.ac.ir, najafpour8@yahoo.com. Fax: 0098-111-3234204.

 

Accepted 1 August, 2008

 
   Abstract
 

Immobilized cell reactor (ICR) was developed as a novel bioreactor to convert hydrolyzed sugars to organic acids. Sugar fermentation by Propionibacterium acid-propionici entraped by calcium alginate was carried out in continuous mode to produce propionic and acetic acids. In continuous fermentation, more than 90 percent of glucose conversion and 60 percent conversion of xylose were obtained at a retention time of 28 h.  The present research has demonstrated that the microorganism preferred glucose as carbon source over other carbon sources. The highest sugar concentration (120 g/L) in the ICR column was successfully converted to propionic acid. The achieved results in ICR with high substrate concentration are promising for scale up operation.

 

Key words: Enzyme, whole cell, immobilized cell reactor, bioreactor, entrapment.

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