Process intensification in biodiesel production using unconventional reactors

Ajeet Kumar Prajapati

doi:10.1016/j.fuel.2024.133263

2025-01-01

PRE

Ajeet Kumar Prajapati

Syed Saim Ali

Khursheed B. Ansari *

Moina Athar

Mohammed K. Al Mesfer

DOI：10.1016/j.fuel.2024.133263

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This review discussed unconventional reactors for biodiesel production including static and chaotic mixers, hydrodynamic cavitation reactor, oscillatory flow reactor (OFR), rotating/spinning-tube reactor, reactive distillation, plasma-, spiral-, membrane-, ultrasonic-, microwave-, and microchannel reactors. Mixers and OFR eased biodiesel production with improved mixing, reduced methanol consumption, and faster reaction time. Cavitation and ultrasound reactor intensified oil/catalyst surface area, mass transfer, and transesterification reaction. Rotary/spinning tube reactors enabled shear stress on oil/alcohol films, providing a high surface area/ volume ratio and high interactions between the reactants. Plasma reactor avoided catalyst use and enabled biodiesel production 20 - 25 folds faster than the conventional reactor. Reactive distillation with membrane reactors avoided the separation issue. Spiral reactor facilitated enhanced heat transfer between the reacting mixtures with net energy ratio and energy efficiency of 0.92 and 0.98, respectively. Microwave reactors enabled local heating of reactants and resulted in uniform heating of the reaction mixture. Microreactors enabled short diffusion distance, improved surface area/volume ratio, and enhanced heat and mass transfers than conventional reactors. Thus, the unconventional reactors appeared promising to intensify biodiesel production, however, significant efforts are needed to reach their applications in commercial biodiesel production.

Keyword:

Biodiesel

Unconventional reactors

Intensification

Improved mixing

Heat and mass transfer

Future perspectives