Abstract
Three ranges of increasing temperatures (35–43, 37–45, 39–47°C) were sequentially applied to a five-stage system continuously operated with cell recycling so that differences of 2°C (between one reactor to the next) and 8°C (between the first reactor at the highest temperature and the fifth at the lowest temperature) were kept among the reactors for each temperature range. The entire system was fed through the first reactor. The lowest values of biomass and viability were obtained for reactor R3 located in the middle of the system. The highest yield of biomass was obtained in the effluent when the system was operated at 35–43°C. This nonconventional system was set up to simulate the local fluctuations in temperature and nutrient concentrations that occur in different regions of the medium in an industrial bioreactor for fuel ethanol production mainly in tropical climates. Minimized cell death and continuous sugar utilization were observed at temperatures normally considered too high for Saccharomyces cerevisiae fermentations.
| Original language | English |
|---|---|
| Pages (from-to) | 140-144 |
| Journal | Journal of Industrial Microbiology and Biotechnology |
| Volume | 29 |
| Issue number | 3 |
| DOIs | |
| Publication status | Published - Sept 2002 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- Continuous process
- Fermentation
- Ethanol
- Thermotolerance
- Heat shock
- Saccharomyces
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