posted on 2008-07-14, 15:14authored byRichard J.L. Meanwell, Gilbert Shama
Streptomycin production from chitin by Streptomyces griseus was compared using
two different types of bioreactor. The first was equipped with a combined U-shaped
paddle and Rushton impeller. Also employed was a bioreactor of novel design in
which the chitin was contained in a wire mesh basket that was totally submerged in a
liquid salts medium. During operation the chitin was gently fluidised by air admitted
into the basket. Fermentation was continued in both bioreactors until maximum
antibiotic titres were achieved whereupon operation was interrupted to allow the
streptomycin adsorbed to the chitin substrate to be extracted into pH 3.0 buffer before
continuing fermentation of the same batch of chitin a second time. At a chitin
concentration of 10 % (w/v) the highest streptomycin yields (c. 5.5 mg/L) were
obtained using the stirred bioreactor, however growth occurred more rapidly in the
vertical basket bioreactor.
History
School
Aeronautical, Automotive, Chemical and Materials Engineering
Department
Chemical Engineering
Citation
MEANWELL, R.J.L. and SHAMA, G., 2006. Chitin in a dual role as substrate for Streptomyces griseus and as adsorbent for streptomycin produced during fermentation. Enzyme and microbial technology, 38(5), pp. 657-664