Distillation for in situ recovery of volatile fermentation products

In situ product removal (ISPR) is required for microbial production of hydrophobic chemicals.Vacuum distillation coupled to a bioreactor is effective for ISPR of volatile products.Process intensification allows low costs for ISPR and product purification.Even products with a boiling point of 170°C c...

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Veröffentlicht in:Trends in biotechnology (Regular ed.) 2025-01
Hauptverfasser: Straathof, Adrie J.J., Janković, Tamara, Kiss, Anton A.
Format: Artikel
Sprache:eng
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Zusammenfassung:In situ product removal (ISPR) is required for microbial production of hydrophobic chemicals.Vacuum distillation coupled to a bioreactor is effective for ISPR of volatile products.Process intensification allows low costs for ISPR and product purification.Even products with a boiling point of 170°C can be vacuum distilled from aqueous broth (if they are sufficiently hydrophobic). Many fermentation products inhibit their own microbial production, which complicates industrial-scale fermentation development for these products. When a product is volatile, this inhibition can be circumvented by removing product during fermentation through evaporation in a loop around the bioreactor. Microbes can survive this loop if its temperature is reduced using vacuum. Then, regrowing of microbes is not required. From a separation efficiency viewpoint, the evaporation loop should not use a single equilibrium stage, but a multistage vacuum distillation column. Such in situ product removal (ISPR) by vacuum distillation has hardly been recognized as an option, however. Costs for this product removal with subsequent purification are modest, even when product titers are low. A prerequisite is the use of advanced energy integration and heat pumping methods. Many fermentation products inhibit their own microbial production, which complicates industrial-scale fermentation development for these products. When a product is volatile, this inhibition can be circumvented by removing product during fermentation through evaporation in a loop around the bioreactor. Microbes can survive this loop if its temperature is reduced using vacuum. Then, regrowing of microbes is not required. From a separation efficiency viewpoint, the evaporation loop should not use a single equilibrium stage, but a multistage vacuum distillation column. Such in situ product removal (ISPR) by vacuum distillation has hardly been recognized as an option, however. Costs for this product removal with subsequent purification are modest, even when product titers are low. A prerequisite is the use of advanced energy integration and heat pumping methods.
ISSN:0167-7799
1879-3096
1879-3096
DOI:10.1016/j.tibtech.2024.12.009