Abstract

Ultrasonic spraying was used in a three-phase reactor to produce small droplets of triolein mixed with CaO as a solid catalyst at temperatures above the boiling point of methanol for enhancement of the transesterification of triolein. Droplets fell in the methanol countercurrent flow and were collected at the bottom of the reactor, followed by circulation to the ultrasonic spray system. The experimental parameters included triolein flow rates of 2.5–9.0 mL/min, reaction temperatures of 70–100 °C, and catalyst contents of 1.0–7.0 wt%. The methanol feed rate was set to be constant. The results suggested that the enhancement was successful after using the three-phase reactor by generating a high contact surface area for the droplets, which was a key factor for determining the performance. Comparing the results with conventional transesterification in the liquid phase using the same CaO at 60 °C, the three-phase reactor produced a methyl ester yield 2–5% higher during the 60 min trial period. However, the yield became lower after 60 min because the mass transfer of methanol to the droplets was limited. The transesterification kinetics were estimated based on the experimental data—assuming a first-order reaction—and the results indicated a range of the rate constant, an apparent activation energy, and a pre-exponential factor of 1.21–3.70 × 10−2 min−1, 36.1 kJ mol−1, and 64.9 min−1, respectively, suggesting that the three-phase reactor was effective for fast transesterification at the initial stage.

Highlights

  • Published: 19 January 2021Modern society is currently consuming a great deal of energy

  • Biodiesel is produced by the transesterification of vegetable oil, algal oil, or animal fat [1] by using a homogenous catalyst such as sodium hydroxide

  • It was observed that a flow rate 2 showsgave the effect of theyield, triolein flow rate on those the methyl ester yield

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Summary

Introduction

Published: 19 January 2021Modern society is currently consuming a great deal of energy. Biodiesel has the potential to be one of the clean, sustainable energy sources for human civilization, and it has proven to be an attractive substitute because of its renewability and combustion performance being nearly similar to conventional diesel oil. The disadvantage of the homogenous process is that the catalyst remains with the product after the reaction. Wastewater from the washing cannot be directly released into the environment. This problem could be solved by changing the homogenous catalysts to heterogeneous catalysts. Alkaline earth metal oxide is considered a candidate because the strength of the basic site is related to the electronegativity of the conjugated metal cation. The basic strength of the data from CO2 -TPD

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