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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 />

1326<br />

requirement can be manipulated by the<br />

conventional or statistical methods (3). The<br />

conventional method involves changing one<br />

independent variable at a time, while keeping<br />

other variables at a fixed level. Statistical<br />

methods, on the other h<strong>and</strong>, (a) shortlist<br />

significant variables, (b) help in underst<strong>and</strong>ing<br />

the interactions among the variables at different<br />

levels, <strong>and</strong> (c) reduce the total number <strong>of</strong><br />

experiments resulting in saving time <strong>and</strong><br />

resources. Hence these methods are more rapid<br />

<strong>and</strong> reliable (4).<br />

There are very few reports on production<br />

<strong>of</strong> cephamycin C from Nocardia lactamdurans<br />

using submerged fermentation (SmF) (5,6). To<br />

the best <strong>of</strong> our knowledge, no report on<br />

optimization <strong>of</strong> the fermentation media<br />

composition <strong>and</strong> conditions for cephamycin C<br />

production are available, which prompted us to<br />

undertake this study. This paper reports a detailed<br />

study on the optimization <strong>of</strong> cephamycin C<br />

production from Nocardia lactamdurans NRRL<br />

3802 using SmF, initially by the conventional<br />

one factor at-a-time method <strong>and</strong> subsequently by<br />

statistical methods such as Taguchi L 16<br />

-<br />

orthogonal array design <strong>and</strong> central composite<br />

rotatable design. Furthermore, the effects <strong>of</strong><br />

precursors <strong>and</strong> inducer on the production <strong>of</strong><br />

cephamycin C were also undertaken.<br />

Materials <strong>and</strong> Methods<br />

Materials: Nutrient broth, yeast extract, malt<br />

extract, peptone, L-glutamic acid, sucrose,<br />

fructose, lactose, maltose, galactose, myoinositol<br />

<strong>and</strong> 1,3-diaminopropane were purchased<br />

from Himedia Limited, Mumbai, India. Glucose,<br />

glycerol, starch, ammonium chloride, calcium<br />

carbonate, potassium dihydrogen<br />

orthophosphate, dipotassium hydrogen<br />

orthophosphate, sodium chloride, magnesium<br />

sulphate, ferrous sulphate, manganese sulphate,<br />

zinc sulphate, sodium thiosulphate,<br />

orthophosphoric acid, methanol, L-cysteine, L-<br />

valine, DL-methionine, L-lysine hydrochloride,<br />

heptanesulphonic acid sodium salt for HPLC <strong>and</strong><br />

HPLC grade acetonitrile were purchased from<br />

s.d. Fine-Chem Limited, Mumbai, India.<br />

Soybean oil, sesame oil, coconut oil, groundnut<br />

oil <strong>and</strong> mustard oil were procured from local<br />

market <strong>of</strong> Matunga, Mumbai, India. All solvents<br />

used were <strong>of</strong> AR grade unless mentioned.<br />

St<strong>and</strong>ard cephamycin C (authentic sample) was<br />

a gift sample through kind courtesy <strong>of</strong> Merck<br />

Research Laboratories, Rahway, NJ, USA.<br />

A cephamycin C producing strain,<br />

Nocardia lactamdurans NRRL 3802, was a gift<br />

sample from Northern Regional Research<br />

Laboratory, Peoria, Illinois, USA.<br />

Preparation <strong>of</strong> seed inoculums: The strain was<br />

maintained as glycerol stock by adding 1 ml <strong>of</strong><br />

culture solution, prepared by growing 1 ml (1 x<br />

10 9 CFU/ml) <strong>of</strong> the organism in 50 ml NYG<br />

medium [(g/l) nutrient broth 8, yeast extract 2,<br />

glucose 10, MgCl 2<br />

4, pH 6.8) for 48 h (7)], to<br />

preautoclaved 1.5 ml microcentrifuge tube<br />

containing 0.5 ml <strong>of</strong> 50% glycerol solution <strong>and</strong><br />

stored at -20°C. For seed inoculum, the glycerol<br />

stock (1 x 10 9 CFU/ml) prepared earlier was<br />

inoculated into 50 ml <strong>of</strong> sterilized NYG media<br />

<strong>and</strong> kept on orbital shaker at 180 rpm for 48 h.<br />

Fermentative production <strong>of</strong> cephamycin C: The<br />

production medium for cephamycin C contained<br />

(g/l) glucose, 10.0; L-glutamic acid, 4.25; NH 4<br />

Cl,<br />

1.0; CaCO 3<br />

, 0.25; K 2<br />

HPO 4<br />

, 2.0; myo-inositol,<br />

0.2; MgSO 4<br />

.7H 2<br />

O, 0.5; NaCl, 0.5; FeSO 4<br />

.7H 2<br />

O,<br />

0.025; MnSO 4<br />

.H 2<br />

O, 0.005; ZnSO 4<br />

.7H 2<br />

O, 0.01;<br />

para-amino benzoic acid (PABA), 0.0001 <strong>and</strong><br />

Na 2<br />

S 2<br />

O 3<br />

.5H 2<br />

O, 0.36. The pH <strong>of</strong> the production<br />

medium was adjusted to 6.8 ± 0.05 (5). 50 ml <strong>of</strong><br />

production medium was taken in 250 ml<br />

Erlenmeyer flask <strong>and</strong> sterilized by autoclaving<br />

at 121°C for 20 min. After cooling, the media<br />

was inoculated with 1 ml <strong>of</strong> 48 h old seed culture<br />

Lalit D. Kagliwal et al

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