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Acetone Butanol Production - Acetone butanol production is a strictly anaerobic process due to the strictly anaerobic Clostridium acetobutylicum. The process was industrialized for production of acetone, used as solvent for cordite for explosive manufacture, during the World War 1. Later it was used to produce butanol, which has varied applications.

But at present, both acetone and butanol are obtained by chemical synthesis, and this fermentation is rarely used. C. acetobutylicum is a spore forming bacterium, whose strains differ in their ability to utilize various substrates, e.g., potato, molasses, com, etc.

The fermentation yields a number of products of which acetone, butanol and ethanol are the major ones. Generally, strains are developed to produce the highest possible ratio of butanol over acetone and ethanol. During fermentation, the starch is digested to yield glucose, which is then metabolized to yield butanol and acetone.

Corn meal medium is prepared by grinding degermed (de-embryonated) corn to fine powder; 8-10% of this com meal is heated to gelatinize the starch. The molasses medium contains; 6% sucrose to which are added ammonium sulphate, calcium carbonate, superphosphate and sometimes cornsteep liquor.

Com medium is used for fermentation by C. acetobutylicum, while molasses medium is fermented by C. saccharo acetobutylicum. The fermentation passes through three phases:

(i) rapid bacterial growth and production of acetic and butyric acids, and evolution of CO2 and H2 (initially, H2 is the major component of gas) for 13-17 hr after incubation,
(ii) rapid conversion of the acids into acetone and butanol leading to a fast decline in the acidity of the broth (this is called "acid break"), and
(iii) marked decrease in gas evolution, and acetone and butanol production.

The final broth contains about 2% acetone, ethanol and butanol, which represents about 30% conversion of the carbohydrates. Typically, com medium yields butanol, acetone and ethanol in the ratio 6, 3 and I, while for molasses medium these values are 6.5, 3 and 5.
Recovery of the products is by a distillation process usually by a "beer still" which operates in a continuous mode; this yields approximately 40% (w/w) total mixed solvents. Individual solvents are separated by fractional distillation.