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Research Article

Intensification of interesterification of sustainable feedstock as mahua oil for biodiesel production

, &
Pages 1514-1523 | Received 12 Jul 2022, Accepted 11 Dec 2022, Published online: 25 Dec 2022
 

ABSTRACT

In the current work, the ultrasonic horn induced cavitation was used as an intensification approach for the production of fatty acid methyl esters (FAME), i.e. biodiesel and triacetin as a by-product from the reaction of mahua oil selected as sustainable feedstock and methyl acetate (MA). The effects of process variables like reaction temperature, mahua oil to methyl acetate molar ratio, reaction time, catalyst loading, duty cycle, and power on yield of FAME have been studied and the results elucidated best conditions for maximum fatty acid methyl ester yield of 96% as time of 50 min, temperature of 50 C, molar ratio of 1:8, duty cycle of 40%, ultrasonic power of 70 W and catalyst loading of 1 wt%. For conventional approach based on only stirring, the yield was 61% under otherwise similar conditions. Kinetic study was performed to estimate the order of reaction and the activation energy. It was shown that the kinetics was well fitted to first-order reaction and activation energy was observed as 25.9 kJ/mol. The study revealed the effective application of ultrasonic horn in intensification of biodiesel production using interesterification reaction resulting in considerably higher yield of FAME.

List of abbreviations

FAME=

Fatty acid methyl esters

MA=

Methyl acetate

min=

minute

h=

hour

ASTM=

American Society of Testing Material

HPLC=

High performance liquid chromatography

LR=

Laboratory reagent

GCMS=

Gas chromatography coupled with mass spectrophotometer

W=

Watt

MO=

Mahua oil

MADG=

Mono-acetin diglyceride,

DAMG=

Di-acetin monoglyceride

TA=

Triacetin

List of symbols

r=

rate of reaction

k=

rate constant

x=

conversion

CAO=

initial concentration of reactant

CA=

concentration of reactant at time t

Ea=

activation energy

Acknowledgment

One of the authors SG would like to acknowledge the support of the UGC Networking Resource Centre in Chemical Engineering for enabling the Ph.D. degree work

Disclosure statement

No potential conflict of interest was reported by the authors.

Additional information

Funding

The work was supported by the University Grants Commission [Networking Resource Center in Chemical Engineering].

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