Experimental study of a rapid rate biofuel production in a cyclone type reactor

Abstract

A cyclone-type transesterification system at a pilot scale setup is developed to minimize production costs. This device works on the concept of a cyclone separator in which the straight vegetable oil was injected tangentially to create a vortex. Then a solution of methoxide was poured slowly. An electric heater was provided externally for the perfect reaction of SVOs with methoxide solution. Biodiesel is gaining prominence as substitute of fossil-fuel to minimize the diminution of fossil fuels. It is a safe storable, non-toxic renewable energy source with characteristics comparable to petro-diesel. In the present biodiesel production system, the denser particles were forced towards the chamber wall and light particles in the central position of the reactor. Hence, due to the gravity effect, denser particles fell below in the collection chamber and recirculated, and the biodiesel is obtained after the reactor's completion in a specific time. The developed system is an effective and efficient technique to reduce reaction time and production cost with enhanced production capacity in a small reactor.