Application of novel technology to the abe fermentation process

Traditional technology for ABE production and recovery does not allow an economic process. However, use of a fluidized-bed reactor using immobilized cells in a continuous fermentation process, coupled with product removal and concentration by a membrane process, is a viable option. The major factor affecting product price is the substrate cost. Membrane selectivity and flux have little effect.

[1]  W. J. Groot,et al.  Economic feasibility of the production of iso-propanol-butanol-ethanol fuels from whey permeate , 1985 .

[2]  N. Qureshi,et al.  Reactor design for the ABE fermentation using cells of Clostridium acetobutylicum immobilized by adsorption onto bonechar , 1988 .

[3]  Pak-Lam Yu,et al.  Fermentation technologies: industrial applications , 1990 .

[4]  Frank C. Vilbrandt Chemical Engineering Plant Design, 2Nd. Ed. , 1942 .

[5]  N. Qureshi,et al.  Integration of continuous production and recovery of solvents from whey permeate: use of immobilized cells of Clostridium acetobutylicum in a flutilized bed reactor coupled with gas stripping , 1990 .

[6]  Frank C. Vilbrandt,et al.  Chemical Engineering Plant Design , 1935, Nature.

[7]  N. Qureshi,et al.  Continuous solvent production from whey permeate using cells of Clostridium acetobutylicum immobilized by adsorption onto bonechar , 1987 .

[8]  William D. Baasel,et al.  Preliminary chemical engineering plant design , 1976 .

[9]  M. Matsumura,et al.  Separation of dilute aqueous butanol and acetone solutions by pervaporation through liquid membranes , 1987, Biotechnology and bioengineering.

[10]  I. Maddox,et al.  The acetone-butanol-ethanol fermentation: a current assessment , 1986 .

[11]  D. T. Jones,et al.  Acetone-butanol fermentation revisited. , 1986, Microbiological reviews.

[12]  L. Puigjaner,et al.  Study of butanol extraction through pervaporation in acetobutylic fermentation. , 1987, Biotechnology and bioengineering.

[13]  Gael D. Ulrich,et al.  A Guide to Chemical Engineering Process Design and Economics , 1984 .