d(GC) - Association of Biotechnology and Pharmacy
d(GC) - Association of Biotechnology and Pharmacy
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