Comparative studies were performed to develop a fermentation process for th
e production of rifamycin-B using Amycolatopsis mediterranei VA18. Wheat br
an as substrate in solid state fermentation (SSF), and peanut meal and soyb
ean with glucose were used as substrate for submerged fermentation (SmF). V
arious process parameters including moisture and pH of the substrate, inocu
lum size, temperature and period of incubation were optimised for rifamycin
-B production. For SmF, the optimal conditions were 10% (v/v) inoculum, pH
7.2, incubation temperature 30 degreesC with a fermentation period of 6 day
s. When SmF was carried out in fermenter with controlled aeration (1.5 vvm)
and dissolved oxygen level (80%), rifamycin production increased to about
1.5-fold greater than the flasks. SSF was, in general, superior to SmF cond
ucted in flasks or fermenter. Optimal conditions for SSF were 7.2 substrate
pH, 30% (v/v) inoculum size and incubation at 32 degreesC for 9 days. As t
he content of substrate moisture increased in SSF, rifamycin production als
o increased and highest yields were obtained when fermentation was carried
out using 90% moisture which led practically to semi-solid-to-slurry condit
ions of fermentation. With 70% substrate moisture (SSF conditions), rifamyc
in production was about 15 g/kg which was about 31 g/kg with 80% moisture.
Maximum production (rifamycin-B, 39 g/kg substrate) was obtained with 90% s
ubstrate moisture, which was almost 16-fold higher than that obtained in th
e fermenter (SmF). Ethyl acetate appeared as the most suitable organic solv
ent for the extraction of the antibiotic from the fermented material. (C) 2
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