Syngas fermentation to biofuel: Evaluation of carbon monoxide mass transfer and analytical modeling using a composite hollow fiber (CHF) membrane bioreactor - PowerPoint PPT Presentation

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Syngas fermentation to biofuel: Evaluation of carbon monoxide mass transfer and analytical modeling using a composite hollow fiber (CHF) membrane bioreactor

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Title: Syngas fermentation to biofuel: Evaluation of carbon monoxide mass transfer and analytical modeling using a composite hollow fiber (CHF) membrane bioreactor


1
Syngas fermentation to biofuel Evaluation of
carbon monoxide mass transferand analytical
modeling using a composite hollow fiber (CHF)
membrane bioreactor
2
Syngas
  • Synthesis gas
  • Produced from the gasification of carbon-rich
    feedstock
  • Composed primarily of carbon monoxide and
    hydrogen
  • Can be converted to biofuels

3
Problems
  • Syngas exists in a gaseous phase
  • Microorganisms are in an aqueous phase

4
Mass Transfer Implications
  • Mass transfers occurs at several points
  • transfer of gas to gas-liquid interface
  • transfer of gas to liquid
  • transfer of gas to liquid around microorganism
  • diffusion of gas into microorganism
  • Solubility of CO and H2 are low
  • Gasliquid mass transfer is a rate-limiting step
    in syngas fermentation

5
Previous Bioreactor Designs
  • In order to increase mass transfer
  • Increase pressure
  • Increase gas-liquid surface area
  • Increase agitation
  • Alternative designs

6
This study
  • Determine the mass transfer efficiencies of
    carbon monoxide in composite hollow fiber (CHF)
    membrane bioreactor

7
Setup
  • CHF membrane bioreactor (3 liters)
  • Tap water (25C)
  • Pure carbon monoxide

8
CHF Membrane Module
  • Pressurized gas is forced through one side
  • Gas can pass through a nonporus layer
  • Liquid cannot

9
Experiment
  • Measure volumetric mass transfer coefficient at
    varying
  • Water recirculation rates (five)
  • Inlet carbon monoxide pressures (six)

10
Carbon Monoxide Determination
  • Myoglobin (Mb)-protein bioassay

11
Results
12
Compared with other Bioreactors
13
Resistance Analysis
14
Model
  • Used data to create a modeling equation using
    fluid dynamics

15
Discussion
  • Demonstrated the effectiveness of CHF membrane
    reactor

16
Problems
  • Did not compare bioreactors consistently
  • Did not test with syngas
  • Did not test the affect on microorganism

17
References
  • Cussler, E. L. (2009). Diffusion, mass transfer
    in fluid systems. (3rd ed. ed.). Cambridge
    Cambridge Univ Pr.
  • Munasinghe, P. C., Khanal, S. K. (2010).
    Biomass-derived syngas fermentation into
    biofuels Opportunities and challenges.
    Bioresource technology, 101(13), 5013-5022.
  • Munasinghe, P. C., Khanal, S. K. (2012). Syngas
    fermentation to biofuel Evaluation of carbon
    monoxide mass transfer and analytical modeling
    using a composite hollow fiber (CHF) membrane
    bioreactor. Bioresource Technology, 112, 130-136
  • Riggs, S. S., Heindel, T. J. (2008). Measuring
    Carbon Monoxide GasLiquid Mass Transfer in a
    Stirred Tank Reactor for Syngas Fermentation.
    Biotechnology progress, 22(3), 903-906.
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