Mm. Hoq et al., CELLULASE-FREE XYLANASE BY THERMOMYCES-LANUGINOSUS RT9 - EFFECT OF AGITATION, AERATION, AND MEDIUM COMPONENTS ON PRODUCTION, Journal of biotechnology, 37(1), 1994, pp. 49-58
Several carbohydrates were examined for their ability to induce xylana
se in Thermomyces lanuginosus RT9 at 50 degrees C in shake flask cultu
res. It was found that xylan or xylan containing substrates, such as c
orn cobs, induced maximum and comparable level of xylanase free of cel
lulase, while the easily metabolisable sugars (glucose, xylose, and su
crose) appeared to repress xylanase synthesis. Low level of constituti
ve enzyme was produced as evident from the culture medium without carb
on source addition. Initial culture pH significantly influenced both g
rowth and xylanase production, exhibiting a maximum at 6.5 on xylan. T
he effects of agitation and aeration rates were investigated in a bior
eactor. Both influenced significantly the growth, cultivation time and
enzymes (xylanase and beta-xylosidase) production. The highest level
of xylanase productivity (41630 U l(-1) h(-1)) was achieved at an agit
ation of 200 rpm and 1.0 vvm aeration rate. At these conditions, the s
pecific xylanase activity in the shake flask could be reproduced. Vari
ation of nitrogen components demonstrated that a combination of yeast
extract and (NH4)(2)HPO4 supported the best biomass growth, extracellu
lar protein and xylanase production. At a C/N ratio of about 6.0 using
yeast extract and (NH4)(2)HPO4 containing medium (yeast extract mediu
m), a 3-fold higher xylanase production compared with the peptone medi
um was achieved in shake flask. However, in bioreactor system, the imp
roved specific xylanase activity could not be reproduced due to theolo
gical problem under higher biomass formation with accompanying viscosi
ty and consequent oxygen transfer efficiency. Hence, the peptone mediu
m with xylan (2.0%) is more appropriate to achieve high productivity o
f xylanase in bioreactor system.