The synthesis of fatty acid ethyl esters (FAEE) from Jatropha curcas L. oil was studied in a batch reactor and a continuous centrifugal contactor separator (CCCS) using sodium ethoxide as the catalyst. The effect of relevant process variables like rotational speed, temperature, catalyst concentration, and molar ratio of ethanol to oil was investigated. Maximum yield of FAEE was 98 mol% for both the batch (70°C, 600 rpm, 0.8% w/w of sodium ethoxide) and CCCS reactor configuration (60°C, 2100 rpm, 1% w/w of sodium ethoxide, oil feed 28 mL/min). The volumetric production rate of FAEE in the CCCS at optimum conditions was 112 kgFAEE/m3liquid · min.Practical applications: The Jatropha curcas L. shrub produces a non‐edible oil in yields up to 1.5 ton/(ha. y), which is known to be suitable for biodiesel synthesis. We here report an experimental study on the synthesis of jatropha biodiesel using ethanol instead of methanol as the alcohol source. Ethanol is accessible from biomass by fermentation and as such a green alternative for methanol. In addition, it is more readily available in developing countries than methanol. Biodiesel synthesis was performed in a CSSS, a continuous device that integrates reaction and separation. The device has potential to be applied in small scale mobile biodiesel technology due to its compact size, robustness, flexibility in operation, and high volumetric productivities.
The synthesis of fatty acid methyl esters (FAME) from sunflower oil and methanol was studied in a continuous centrifugal contactor separator (CCCS) using sodium methoxide as the catalyst. The effect of relevant process variables like oil and methanol flow rate, rotational speed and catalyst concentration was investigated and modelled using non-linear regression. Good agreement between experiments and model were obtained. At optimised conditions (oil flow rate of 31 mL/min, rotational speed of 34 Hz, catalyst concentration of 1.2%w/w and a methanol flow rate of 10 mL/min), the FAME yield was 94 mol% at a productivity of 2470 kg FAME /m 3 reactor .h. Proof of principle for the synthesis and subsequent refining of FAME in a cascade of two CCCS devices was also obtained. Relevant properties of the refined FAME obtained using this technology were determined and were shown to meet the ASTM specifications.Practical application: Synthesis and refining of sunflower biodiesel was successfully performed in a cascade of two CSSS devices. Besides for large scale biodiesel production, this technology has particularly potential to be applied in small mobile biodiesel units due to the compact size, robustness, flexibility in operation, and high volumetric productivity of the CCCS devices.
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