Bioreactor design for synthesis gas fermentations
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The ratio and partial pressures of CO, H2, and CO2 influence the product yield, production rate, and selectivity of a gas fermentation.
“Next to gas availability determined by reactor kLa, the ratio and partial pressures of CO, H2, and CO2 also influence the product yield, production rate, and selectivity of a gas fermentation (Genthner and Bryant, 1982; Vega et al., 1988; Klasson et al., 1991; Gaddy and Chen, 1998; Hurst and Lewis, 2010; Kantzow et al., 2015).”
From Gas Fermentation—A Flexible Platform for Commercial Scale Production of Low-Carbon-Fuels and Chemicals from Waste and Renewable Feedstocks (2016) · cites this paper as Klasson et al., 1991
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- Authors
- Klasson, K. T., Ackerson, M. D., Clausen, E. C., & Gaddy, J. L.
- Affiliations
- University of Arkansas at Fayetteville (US)
- ORCID
- Klasson, K.T.
- Venue
- Fuel
- Publisher
- Elsevier BV
- Published
- 1991-05
- Volume
- 70
- Issue
- 5
- Pages
- 605-614
- ISSN
- 0016-2361 (ISSN-L)
- OpenAlex
- W2049496022
- Cited by
- 68
- References
- 31
- Citations by year
- 2025: 1 · 2024: 1 · 2023: 1 · 2022: 2 · 2021: 3 · 2020: 5 · 2019: 4 · 2018: 5 · 2017: 6 · 2016: 6 · 2015: 3 · 2014: 5 · 2013: 4 · 2012: 2
- FWCI
- 0.43
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- Fuel (publishedVersion)
- Topics
- Physical Sciences › Engineering › Biomedical Engineering › Fluid Dynamics and Mixing
- Physical Sciences › Engineering › Building and Construction › Anaerobic Digestion and Biogas Production
- Physical Sciences › Engineering › Biomedical Engineering › Biofuel production and bioconversion
- Keywords
- bioreactor design, ethanol production, methane production, gas-liquid mass transfer, continuous stirred tank reactor, immobilized cell reactors, mass transfer coefficient, gas solubility, retention time
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