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d(GC) - Association of Biotechnology and Pharmacy

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

Vol. 6 (2) 241-254 April 2012, ISSN 0973-8916 (Print), 2230-7303 (Online)<br />

simultaneously use <strong>of</strong> three amino acids as<br />

precursors increases the production cost. Due<br />

to this reason GSH production by fermentation<br />

has been extensively studied, in which sugars<br />

as substrates can be used on industrial scale to<br />

nullify the production cost <strong>and</strong> to increase the<br />

GSH concentration in the medium (13). GSH<br />

production can be increased by either increasing<br />

the biomass or by changing amino acids.<br />

Saccharomyces cerevisiae <strong>and</strong> C<strong>and</strong>ida utilis are<br />

currently utilised to produce glutathione on an<br />

industrial scale (13).<br />

The conventional one factor at-a-time<br />

optimization method optimizes only one<br />

parameter at a time in which other parameters<br />

are kept constant. The statistical procedure<br />

makes available an alternative methodology to<br />

optimize a particular process by considering<br />

mutual interactions among the variables <strong>and</strong><br />

gives an estimate <strong>of</strong> the combined effect <strong>of</strong><br />

variables selected for study on the final result.<br />

Response surface methodology (RSM)<br />

employed in this study is based on the<br />

fundamental principles <strong>of</strong> statistics,<br />

r<strong>and</strong>omization, replication <strong>and</strong> duplication, which<br />

simplifies the optimization by studying the mutual<br />

interactions among the variables over a range <strong>of</strong><br />

values in a statistically valid manner. It is also<br />

known as full factorial central composite design<br />

(CCD). Previously, RSM was successfully<br />

employed for the production <strong>of</strong> GSH by<br />

Saccharomyces cerevisiae (14). Industrially,<br />

GSH is produced on a large scale by yeast<br />

fermentation (15). Although final purification step<br />

must satisfy extremely high purity for<br />

pharmaceutical purposes, the crude cell extract<br />

includes a lot <strong>of</strong> impurities which limit the<br />

efficiency <strong>of</strong> GSH recovery by crystallization (16).<br />

There are only a few studies reported on<br />

industrial separation <strong>of</strong> GSH.<br />

In the present study, S. cerevisiae was<br />

screened for GSH production. Media optimization<br />

was done by one factor at-a-time <strong>and</strong> a statistical<br />

method i.e. RSM. The effect <strong>of</strong> addition <strong>of</strong> amino<br />

Parbatsingh Rajpurohit et al<br />

242<br />

acids on GSH production was also studied. The<br />

present work also includes the development <strong>of</strong><br />

an effective procedure for isolation <strong>and</strong><br />

purification <strong>of</strong> GSH from fermentation broth. The<br />

effect <strong>of</strong> ATPS on partitioning behavior <strong>of</strong> GSH<br />

<strong>and</strong> contaminating proteins was also studied.<br />

ATPS parameters were studied with respect to<br />

PEG molecular weight, PEG concentration <strong>and</strong><br />

salt concentration to concentrate GSH in one<br />

phase <strong>and</strong> unwanted proteins in other phase.<br />

Further the effective purification process was<br />

done successively with respect to operating<br />

parameters such as selection <strong>of</strong> an ion exchange<br />

resin <strong>and</strong> elution system.<br />

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

Materials: Media components such as glucose,<br />

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

starch, yeast extract, peptone, beef extract, malt<br />

extract, casein peptone <strong>and</strong> agar were purchased<br />

from Hi-Media Lab. Ltd, Mumbai, India.<br />

Magnesium sulphate, Potassium dihydrogen<br />

phosphate, Sodium chloride, Zinc chloride,<br />

Calcium chloride, Ammonium chloride,<br />

Ammonium sulphate <strong>and</strong> ethanol AR grade were<br />

purchased from S. D. Fine Chemicals Ltd,<br />

Mumbai, India. Glycine, hydrochloric acid, acetic<br />

acid, sodium acetate, Amberlite IR 120H,<br />

Amberlite XAD 16, PEG 1500, PEG 4000, PEG<br />

6000 were purchased from S. D. Fine Chem. Ltd.,<br />

Mumbai, India. Indion CAM <strong>and</strong> Indion 830 were<br />

purchased from Ion exchange (India) Ltd.,<br />

Mumbai.<br />

Maintenance <strong>of</strong> cultures <strong>and</strong> Inoculum<br />

development: The strains <strong>of</strong> S. cerevisiae NCIM<br />

3454 was procured from NCIM (National<br />

Collection <strong>of</strong> Industrial Microorganisms) Pune,<br />

India <strong>and</strong> maintained on MGYP agar medium<br />

(malt extract, 0.3 %; glucose, 1.0 %; yeast<br />

extract, 0.5 %; peptone, 0.5 %). All slants were<br />

grown for 24 h aerobically at 30 °C. For inoculum,<br />

saline solution (5 mL) was added to the fully<br />

grown slant <strong>and</strong> 1 mL cell suspension was<br />

transferred to 25 mL <strong>of</strong> the seed medium (MGYP

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