Kinetics
of biomass and polyhydroxyalkanoates synthesis using sugar industry waste as
carbon substrate by Alcaligenes sp. NCIM 5085
R.
Kanzariya1,4, A. Gautam2,4, S. Parikh3,4 and
S. Gautam2,4*
1Department of
Chemical Engineering, Government Engineering College, Bhuj-370 001, India
2Department of
Chemical Engineering, Shroff SR Rotary Institute of Chemical Technology,
Ankleshwar-393 135, India
3Department of
Chemical Engineering, Department of Technical Education, Gandhinagar-382 424,
India
4Department of
Chemical Engineering, Gujarat Technological University, Gandhinagar-382 424,
India
*Corresponding
Author Email :
shinaiitd@gmail.com *ORCiD:
https://orcid.org/0000-0002-6909-6253
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Abstract
Aim:
o optimize the operating parameters and further determine the kinetics of
biomass and polyhydroxyalkanoate synthesis using sugar industry waste as a
carbon substrate by Alcaligenes sp. NCIM 5085.
Methodology: Molasses, clarified and pretreated with sulphuric
acid, was taken in a batch reactor for fermentation to generate biomass and
further for polyhydroxyalkanoate synthesis where Alcaligenes sp. NCIM
5085 was used as a culture. A number of parameters were observed during
fermentation experiments to optimize the biomass and PHA namely: initial
substrate concentration, incubation period, C/N ratio, inoculum concentration
and pH. Fermented solution was filtered to account the yield of biomass from
the solution at each time interval decided for each experiment and
polyhydroxyalkanoate was extracted from the biomass by chloroform and
methanol extraction. Growth kinetics of biomass was modeled by Monod and
Logistic models whereas Luedeking-Piret model was used for polyhydroxyalkanoate
production rates.
Results:
From the fermentation experiments, it was found that for 40 g l-1
of molasses at neutral pH, 4.48 g l-1 of biomass was synthesized
when fermentation was observed for 48 hr. One percent of cell dry weight of
biomass was extracted as polyhydroxyalkanoate. Logistic model for growth
kinetics and Luedeking-Piret model for polyhydroxyalkanoate production rate
were found in agreement with the experiments where regression coefficient was
maximum with minimum error.
Interpretation: The PHA growth
kinetics and PHA production kinetics done in this work can be utilized to
design a bioreactor for PHA production at industrial scale.
Key words: Alcaligenes sp., Biomass, Cane molasses,
Growth kinetics, Polyhydroxyalkanoates
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the acceptability of the conclusions enforced or derived, rest completely
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