Acetone-butanol-ethanol (ABE) fermentation in an immobilized cell trickle bed reactor
- 5 June 1989
- journal article
- research article
- Published by Wiley in Biotechnology & Bioengineering
- Vol. 34 (1) , 18-29
- https://doi.org/10.1002/bit.260340104
Abstract
Acetone–butanol–ethanol (ABE) fermentation was successfully carried out in an immobilized cell trickle bed reactor. The reactor was composed of two serial columns packed with Clostridium acetobutylicum ATCC 824 entrapped on the surface of natural sponge segments at a cell loading in the range of 2.03–5.56 g dry cells/g sponge. The average cell loading was 3.58 g dry cells/g sponge. Batch experiments indicated that a critical pH above 4.2 is necessary for the initiation of cell growth. One of the media used during continuous experiments consisted of a salt mixture alone and the other a nutrient medium containing a salt mixture with yeast extract and peptone. Effluent pH was controlled by supplying various fractions of the two different types of media. A nutrient medium fraction above 0.6 was crucial for successful fermentation in a trickle bed reactor. The nutrient medium fraction is the ratio of the volume of the nutrient medium to the total volume of nutrient plus salt medium. Supplying nutrient medium to both columns continuously was an effective way to meet both pH and nutrient requirement. A 257-mL reactor could ferment 45 g/L glucose from an initial concentration of 60 g/L glucose at a rate of 70 mL/h. Butanol, acetone, and ethanol concentrations were 8.82, 5.22, and 1.45 g/L, respectively, with a butanol and total solvent yield of 19.4 and 34.1 wt %. Solvent productivity in an immobilized cell trickle bed reactor was 4.2 g/L h, which was 10 times higher than that obtained in a batch fermentation using free cells and 2.76 times higher than that of an immobilized CSTR. If the nutrient medium fraction was below 0.6 and the pH was below 4.2, the system degenerated. Oxygen also contributed to the system degeneration. Upon degeneration, glucose consumption and solvent yield decreased to 30.9 g/L and 23.0 wt %, respectively. The yield of total liquid product (40.0 wt %) and butanol selectivity (60.0 wt %) remained almost constant. Once the cells were degenerated, they could not be recovered.This publication has 25 references indexed in Scilit:
- Mathematical model of a batch acetone–butanol fermentationBiotechnology & Bioengineering, 1986
- Optimal conditions for long-term stability of acetone-butanol production by continuous cultures ofClostridium acetobutylicumBiotechnology Letters, 1985
- Studies on the stability of solvent production by Clostridium acetobutylicum in continuous cultureJournal of Applied Bacteriology, 1985
- Control of cell adhesion and activity during continuous production of acetone and butanol with adsorbed cellsEnzyme and Microbial Technology, 1985
- Influence of pH and undissociated butyric acid on the production of acetone and butanol in batch cultures of Clostridium acetobutylicumApplied Microbiology and Biotechnology, 1984
- Control of immobilized, non-growing cells for continuous production of metabolitesApplied Microbiology and Biotechnology, 1983
- Continuous isopropanol-butanol-ethanol fermentation by immobilized Clostridium beijerinckii cells in a packed bed fermenterEnzyme and Microbial Technology, 1983
- Effect of pH and butyrate concentration on the production of acetone and butanol by Clostridium acetobutylicum grown in continuous cultureApplied Microbiology and Biotechnology, 1982
- Continuous production of n-butanol and isopropanol by immobilized, growingClostridium butylicum cellsBiotechnology Letters, 1980
- Oxygen and the Growth and Metabolism of Clostridium acetobutylicumJournal of General Microbiology, 1971