Integrated Process Combining High-Temperature Fermentation and Extractive Ethanol Removal via CO2 Stripping

Fermentation at high temperatures may be a viable alternative for ethanol production, especially in tropical climate regions. This work describes the evaluation of ethanol production through extractive fermentation at high temperatures using thermotolerant Kluyveromyces marxianus. An experimental design was applied to assess the effect of temperature on the ethanol removal process by CO2 stripping. Subsequently, kinetic modeling of conventional batch ethanol fermentation at high temperatures was performed, and the hybrid Andrews−Levenspiel model was found to be suitable for describing the kinetics of this process. Experiments were conducted to evaluate ethanol production at high temperatures using thermotolerant yeast, specifically evaluating the effects of different specific CO2 flow rates (ϕ = 1.0, 1.5, and 2.0 vvm) on ethanol stripping. The results indicated that in all the extractive fermentations conducted with K. marxianus, there was faster substrate uptake and earlier substrate exhaustion compared to conventional fermentation. Significant ethanol removal by stripping was achieved using a CO2 flow rate of 1.0 vvm (EFHT1), and complete substrate consumption was observed by the end of 12 h of fermentation. This result highlights the positive effect of temperature on ethanol entrainment. In addition, integrating the CO2 stripping technique with high-temperature fermentation (T = 40 °C) improves process efficiency with a lower gas flow rate. This is advantageous, especially for industrial-scale applications, as it can reduce equipment costs associated with the CO2 feed.

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Publication Details

Journal
Fermentation
Published
2025-05-09
DOI
https://doi.org/10.3390/fermentation11050270
Citations
3
Primary Topic
Process Optimization and Integration
Type
article
Field-Weighted Citation Impact
3.64

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article

Integrated Process Combining High-Temperature Fermentation and Extractive Ethanol Removal via CO2 Stripping

Rosineide G. Silva, Antonio José Gonçalves Cruz, Nayana Simon de Vargas, Jaqueline Machado de Moraes et al.
3 citations
Fermentation
Process Optimization and Integration
3.64
article

Integrated Process Combining High-Temperature Fermentation and Extractive Ethanol Removal via CO2 Stripping

Rosineide G. Silva, Antonio José Gonçalves Cruz, Nayana Simon de Vargas, Jaqueline Machado de Moraes, Anderson Ferreira da Cunha, Alberto C. Badino, Jorge Luíz Silveira Sonego
article en
3 citations

Abstract

Fermentation at high temperatures may be a viable alternative for ethanol production, especially in tropical climate regions. This work describes the evaluation of ethanol production through extractive fermentation at high temperatures using thermotolerant Kluyveromyces marxianus. An experimental design was applied to assess the effect of temperature on the ethanol removal process by CO2 stripping. Subsequently, kinetic modeling of conventional batch ethanol fermentation at high temperatures was performed, and the hybrid Andrews−Levenspiel model was found to be suitable for describing the kinetics of this process. Experiments were conducted to evaluate ethanol production at high temperatures using thermotolerant yeast, specifically evaluating the effects of different specific CO2 flow rates (ϕ = 1.0, 1.5, and 2.0 vvm) on ethanol stripping. The results indicated that in all the extractive fermentations conducted with K. marxianus, there was faster substrate uptake and earlier substrate exhaustion compared to conventional fermentation. Significant ethanol removal by stripping was achieved using a CO2 flow rate of 1.0 vvm (EFHT1), and complete substrate consumption was observed by the end of 12 h of fermentation. This result highlights the positive effect of temperature on ethanol entrainment. In addition, integrating the CO2 stripping technique with high-temperature fermentation (T = 40 °C) improves process efficiency with a lower gas flow rate. This is advantageous, especially for industrial-scale applications, as it can reduce equipment costs associated with the CO2 feed.

FermentationVol. 11(5)
Universidade Federal de São Carlos (BR), Universidade Federal de Pernambuco (BR)
Fundação de Amparo à Pesquisa do Estado de São Paulo, Conselho Nacional de Desenvolvimento Científico e Tecnológico
Openalex Percentile: Top 7%
Process Optimization and Integration
3.64
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