作者: P. Valle , A. Velez , P. Hegel , G. Mabe , E.A. Brignole
DOI: 10.1016/J.SUPFLU.2010.03.009
关键词:
摘要: In the present work, transesterification of non-edible oil with methanol and ethanol is studied. The reactor phase transitions are directly observed in a double windowed cylindrical conversion to fatty esters measured. optimization process conditions was carried out based on statistical design experiments where key variables were studied over different ranges obtain reliable model for efficiency reaction as function time, temperature, pressure alcohol molar ratio. From direct observations modeling behavior, better understanding supercritical obtained well confirmation equilibrium predictions GCA-EOS model.