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Ingeniería y competitividad

versión impresa ISSN 0123-3033

Resumen

ROJAS, Olga J. et al. Biodiesel production from palm oil in a fixed-bed-reactor with calcium methoxide catalyst. Ing. compet. [online]. 2014, vol.16, n.1, pp.109-118. ISSN 0123-3033.

In this research, the behavior of calcium methoxide as catalyst for the production of biodiesel from palm oil in a continuous system was studied. Initially, operating conditions such as CaO activation temperature (25°C), reaction temperature (60°C) and molar ratio methanol-oil (10)were established for a batch reactor. Then, the schematic diagram of the experimental setup and its implementation were described for a packed-bed laboratory scale reactor with continuous flow; for this system, yields of methyl esters of 20% with a residence time of 60 min were obtained. The use of co-solvent such as tert-Bbutanol and ethyl acetate in the continuous reaction system was also investigated, aiming to eliminate mass transfer artifacts between the phases and eventually increasing yields to methyl esters. The use of ethyl acetate as co-solvent increased methyl esters yields up to 31 %

Palabras clave : Activated calcium oxide; biodiesel; cosolvent; transesterification.

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