Abstract: A method for producing biofuel by a transesterification reaction of an alcohol and a triglyceride such as an oil or fat is carried out at supercritical conditions in a reactor using a stoichiometric excess of alcohol. The reaction products of biofuel and gaseous mixture of glycerin and alcohol are re-cycled through a series of heat exchangers which transfer heat to respective pre-heaters to sequentially raise the temperature and pressure of the reaction mixture prior to delivery to the reactor. Any excess alcohol after separating and recovering gaseous glycerin therefrom is recycled and mixed with “fresh” alcohol. Preferably, the process is a non-catalytic continuous process.

Abstract: A method for producing biofuel by a transesterification reaction of an alcohol and a triglyceride such as an oil or fat is carried out at supercritical conditions in a reactor using a stoichiometric excess of alcohol. The reaction products of biofuel and gaseous mixture of glycerine and alcohol are re-cycled through a series of pre-heaters to sequentially raise the temperature and pressure of the reaction mixture prior to delivery to the reactor. Any excess alcohol after separating and recovering gaseous glycerin therefrom is recycled and mixed with “fresh” alcohol. Preferably, the process is a non-catalytic continuous process.