Abstract
In this paper, the transesterification reaction of waste cooking oil (WCO) with methanol using KOH as catalyst to produce biodiesel was performed in a micro reactor (1 mm ID) using a cross -flow inlet configuration. The effects of different variables such as, methanol-to-oil molar ratio, temperature, catalyst concentration, and residence time on biodiesel yield, as well as the associated flow patterns during the transesterification reaction were investigated and the relationship between flow characteristics and mass transfer performance of the system was examined. The work reveals important aspects and the links between the hydrodynamic behaviour and the mass transfer performance of the intensified reactors. It was found that high yield (>90%) of biodiesel can be achieved in one stage reaction using cross -flow micro-reactors for a wide range of conditions, i.e., methanol-to-oil molar ratio: 8-14, catalyst concentration: 1.4%-1.8% w/w, temperature: 55 degrees C-60 degrees C, and residence times: 55-75 s.