Study on membrane reactors for biodiesel production by phase behaviors of canola oil methanolysis in batch reactors.
In comparison with the general stirring batch reactor, the membrane reactor has been reported to have higher molar ratios of methanol to oil but ultralow catalyst concentration in the biodiesel production. In this research, the methanolysis of canola oil is conducted in a stirring batch reactor in the presence of NaOH as a catalyst. Based on the investigation of the effects of operating conditions, including methanol to oil molar ration, catalyst concentrations and temperatures, the time course of the reaction path for the reactant composition in the ternary phase diagram of oil-FAME-MeOH offers an effective way to understand the operation of membrane reactors in the biodiesel production. The results show that increasing the residence time of the whole reactant system within the two-phase zone is good for the separation operation through the membranes.
Cheng
Li-Hua
LH
Department of Environmental Engineering, Zhejiang University, Hangzhou 310027, PR China.
Yen
Shih-Yang
SY
Su
Li-Sheng
LS
Chen
Junghui
J
D056804:Biofuels; D002384:Catalysis; D004951:Esterification; D005229:Fatty Acids, Monounsaturated / Q000737:chemistry*; D007700:Kinetics; D008567:Membranes, Artificial; D008697:Methane / Q000737:chemistry*; D000074262:Rapeseed Oil; D013696:Temperature
D056804:Biofuels; D005229:Fatty Acids, Monounsaturated; D008567:Membranes, Artificial; D000074262:Rapeseed Oil; D008697:Methane