摘要
The transesterification activity of several solid base catalysts in biodiesel production was systematically studied and evaluated at room temperature. Commercialized calcined silicates showed stronger transesterification ability than other commonly-used oxides, and provided considerable biodiesel yields. Biodiesel yield of >96% was obtained for Na 2 SiO 3 catalyst (calcined at 400 °C) at 28 °C within 12 h with methanol/oil molar ratio of 12/1 and catalyst dosage of 5 wt%, and for CaSiO 3 catalyst (calcined at 550 °C) at 28 °C within 24 h with methanol/oil molar ratio of 27/1 and catalyst dosage of 23 wt%. The high activity of Na 2 SiO 3 came from low activation energy of 104.6 kJ/mol and considerable higher pre-exponential factor of 3.73 × 10 15 min −1 , which produced high turnover frequency of 0.234 min −1 at 28 °C. The introduction of CA-O-Si structure in CaSiO 3 resulted in high surface basicity of 0.70 mmol/g and high pre-exponential factor of 3.79 × 10 19 min −1 but high activation energy of 136.4 kJ/mol. The loss of catalyst activity was mainly due to the variation of surface silicate structure during transesterification.
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