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full issue - Association of Biotechnology and Pharmacy

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Current Trends in <strong>Biotechnology</strong> <strong>and</strong> <strong>Pharmacy</strong><br />

Vol. 5 (3) 1325 -1337 July 2011, ISSN 0973-8916 (Print), 2230-7303 (Online)<br />

1327<br />

<strong>and</strong> incubated in an orbital incubator shaker at<br />

28 ± 2ÚC for 88 h. All experiments were carried<br />

out in triplicates.<br />

Optimization <strong>of</strong> fermentation medium using<br />

one factor at-a-time method<br />

Using the production medium selected for<br />

the optimization study, the following parameters<br />

were optimized<br />

Effect <strong>of</strong> various carbon sources: The effect <strong>of</strong><br />

various carbon sources on production <strong>of</strong><br />

cephamycin C was studied by substituting<br />

glucose in the production media with other<br />

carbon sources such as fructose, galactose,<br />

glycerol, lactose, maltose, sucrose, starch.<br />

Several oils such as soybean oil, groundnut oil,<br />

mustard oil, coconut oil <strong>and</strong> sesame oil were also<br />

evaluated for their effect on cephamycin C<br />

production. Each carbon source was used at 10<br />

g/l. Reducing sugars were autoclaved separately<br />

<strong>and</strong> added before inoculation. The carbon source<br />

which supported maximum production <strong>of</strong><br />

cephamycin C was used for further studies.<br />

Effect <strong>of</strong> inorganic <strong>and</strong> organic nitrogen<br />

sources: Here ammonium chloride was<br />

substituted with other nitrogen sources such as<br />

yeast extract, peptone, malt extract, ammonium<br />

nitrate, urea, ammonium sulphate, (NH 4<br />

) 2<br />

HPO 4<br />

<strong>and</strong> (NH 4<br />

)H 2<br />

PO 4<br />

to check their suitability for<br />

cephamycin C production. Each nitrogen source<br />

was used at 1 g/l. The nitrogen source which<br />

supported maximum production <strong>of</strong> cephamycin<br />

C was used for further studies.<br />

Production pr<strong>of</strong>ile <strong>of</strong> cephamycin C <strong>and</strong> growth<br />

curve <strong>of</strong> N. lactamdurans NRRL 3802: To<br />

obtain production pr<strong>of</strong>ile for cephamycin C <strong>and</strong><br />

growth curve <strong>of</strong> N. lactamdurans NRRL 3802,<br />

three flasks were taken out each day for a period<br />

<strong>of</strong> 5 days <strong>and</strong> processed to determine cephamycin<br />

C content <strong>and</strong> dry cell weight. All other<br />

conditions were maintained as previously<br />

described. The incubation period that gave<br />

maximum production <strong>of</strong> cephamycin C was<br />

chosen for subsequent experiments.<br />

Effect <strong>of</strong> initial pH: In order to investigate the<br />

effect <strong>of</strong> initial pH <strong>of</strong> the medium on cephamycin<br />

C production, N. lactamdurans was cultivated<br />

at different initial pH <strong>of</strong> medium (pH 5.0 - 8.0).<br />

The pH was adjusted using 1N hydrochloric acid<br />

or 1N sodium hydroxide. The fermentation was<br />

carried out at 28 ± 2°C for 72 h. The optimum<br />

pH was used for further studies.<br />

Effect <strong>of</strong> inoculum size: To study the effect <strong>of</strong><br />

inoculum size on cephamycin C production, by<br />

N. lactamdurans, the production media was<br />

inoculated with 1 ml <strong>of</strong> 10 9 ,10 8 ,10 7 <strong>and</strong> 10 6 CFU/<br />

ml in 50 ml <strong>of</strong> autoclaved medium <strong>and</strong> studied<br />

for production <strong>of</strong> cephamycin C.<br />

Effect <strong>of</strong> various minerals: Here each<br />

component from the production medium was<br />

removed one at-a-time (except glycerol, yeast<br />

extract <strong>and</strong> L-glutamic acid) to check its effect<br />

on cephamycin C production.<br />

Optimization <strong>of</strong> fermentation medium using<br />

statistical methods<br />

Optimization using the L 16<br />

-orthogonal array:<br />

Taguchi design was used to determine the most<br />

significant factors which affect the production<br />

<strong>of</strong> cephamycin C. The design for the L 16<br />

-<br />

orthogonal array with 8 factors at two levels to<br />

give a total <strong>of</strong> 16 experiments was developed<br />

<strong>and</strong> analyzed using “MINITAB 13.32” s<strong>of</strong>tware.<br />

The factors selected were glycerol, yeast extract,<br />

L-glutamic acid, K 2<br />

HPO 4<br />

, NaCl, MgSO 4<br />

, FeSO 4<br />

<strong>and</strong> Na 2<br />

S 2<br />

O 3.<br />

Table 1 depicted L 16<br />

-orthogonal<br />

array design, which was used in the present study.<br />

All experiments were performed in triplicates.<br />

Optimization <strong>of</strong> concentrations <strong>of</strong> the selected<br />

medium components by RSM: To examine the<br />

Sequential optimization <strong>of</strong> cephamycin C

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