Skip to main content

Advertisement

Log in

A two-dimensional mass transfer model for an annular bioreactor using immobilized photosynthetic bacteria for hydrogen production

  • Original Research Paper
  • Published:
Biotechnology Letters Aims and scope Submit manuscript

Abstract

A two-dimensional model for substrate transfer and biodegradation in a novel, annular fiber-illuminating bioreactor (AFIBR) is proposed in which photosynthetic bacteria are immobilized on the surface of a side-glowing optical fiber to form a stable biofilm. When excited by light, the desired intensity and uniform light distribution can be obtained within the biofilm zone in bioreactor and then realize continuous hydrogen production. Substrate transfer and biodegradation within the biofilm zone, as well as substrate diffusion and convection within bulk fluid regions are considered simultaneously in this model. The validity of the model is verified experimentally. Based on the model analysis, influences of flow rate and light intensity on the substrate consumption rate and substrate degradation efficiency were investigated. The simulation results show that the optimum operational conditions for the substrate degradation within the AFIBR are: flow rate 100 ml h−1 and light intensity 14.6 μmol photons m−2 s−1.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Fig. 1
Fig. 2
Fig. 3
Fig. 4
Fig. 5
Fig. 6
Fig. 7
Fig. 8

Similar content being viewed by others

References

  • Bai MD, Cao YC, Lin YH, Lu WC, Lee HT (2009) Immobilized biofilm used as seeding source in batch biohydrogen fermentation. Renew Energy 34:1969–1972

    Article  CAS  Google Scholar 

  • Haluk B, Abdurrahman T (1998) The effects of biofilm characteristics on the external mass transfer coefficient in a differential fluidized bed biofilm reactor. Biochem Eng J 1:53–61

    Article  Google Scholar 

  • Kaviany M (1995) Principles of heat transfer in porous media. Springer, New York

    Book  Google Scholar 

  • Kumar N, Das D (2001) Continuous hydrogen production by immobilized Enterobacter cloacae IIT-BT 08 using lignocellulosic materials as solid matrices. Enzyme Microb Technol 29:280–287

    Article  CAS  Google Scholar 

  • Levin DB, Pitt L, Love M (2004) Biohydrogen production: prospects and limitations to practical application. Int J Hydrogen Energy 29:173–185

    Article  CAS  Google Scholar 

  • Liao Q, Wang YZ, Zhu X, Tian X, Ba SL, Zhang P, Zhang C (2008) Effect of initial substrate concentration on kinetics of hydrogen production by photosynthetic bacteria in batch culture. China Biotechnol 27:51–56

    Google Scholar 

  • Mizuno O, Dinsdale R, Hawkes FR, Hawkes DL, Noike T (2000) Enhancement of hydrogen production from glucose by nitrogen gas spraying. Bioresour Technol 73:59–65

    Article  CAS  Google Scholar 

  • Mowla D, Ahmadi M (2007) Theoretical and experimental investigation of biodegradation of hydrocarbon polluted water in a three phase fluidized-bed bioreactor with PVC biofilm support. Biochem Eng J 36:147–156

    Article  CAS  Google Scholar 

  • Patankar SV, Baliga BR (1981) Numerical heat transfer and fluid flow. Hemisphere, Washington

    Google Scholar 

  • Shi XY, Yu HQ (2006) Continuous production of hydrogen from mixed volatile fatty acids with Rhodopseudomonas capsulate. Int J Hydrogen Energy 31:1641–1647

    Article  CAS  Google Scholar 

  • Tian X, Liao Q, Liu W, Wang YZ, Zhu X, Li J, Wang H (2009) Photo-hydrogen production rate of a PVA-boric acid gel granule containing immobilized photosynthetic bacteria cells. Int J Hydrogen Energy 34:4708–4717

    Article  CAS  Google Scholar 

  • Vinod AV, Reddy GV (2006) Mass transfer correlation for phenol biodegradation in a fluidized bed bioreactor. J Hazard Mater 136:727–734

    Article  CAS  Google Scholar 

  • Wang YZ, Liao Q, Zhu X, Tian X, Zhang C (2010) Characteristics of hydrogen production and substrate consumption of Rhodopseudomonas palustris CQK 01 in an immobilized-cell photobioreactor. Bioresour Technol 101:4034–4041

    Article  PubMed  CAS  Google Scholar 

  • Wang YZ, Liao Q, Zhu X, Li J, Lee DJ (2011) Effect of culture conditions on kinetics of hydrogen production by photosynthetic bacteria in batch culture. Int J Hydrogen Energy 36:14004–14013

    Article  CAS  Google Scholar 

  • Zhang C, Zhu X, Liao Q, Wang YZ, Li J, Ding YD, Wang H (2010) Performance of a groove-type photobioreactor for hydrogen production by immobilized photosynthetic bacteria. Int J Hydrogen Energy 35:5284–5292

    Article  CAS  Google Scholar 

Download references

Acknowledgments

The authors gratefully acknowledge financial support from the National Natural Science Foundation of China (No. 50976029), National High Technology Research and Development Program (863 Program) (No. 2012AA051502), China Postdoctoral Science Foundation (No. 2012M521395), Science and Technology Research Project of Education Department in Henan Province (No. 13B470119) and Doctoral Foundation of NCWU (No. 201028).

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Quan-Guo Zhang.

Rights and permissions

Reprints and permissions

About this article

Cite this article

Zhang, C., Wang, AJ. & Zhang, QG. A two-dimensional mass transfer model for an annular bioreactor using immobilized photosynthetic bacteria for hydrogen production. Biotechnol Lett 35, 1579–1587 (2013). https://doi.org/10.1007/s10529-013-1250-2

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s10529-013-1250-2

Keywords

Navigation