Abstract
Biodiesel production has gained considerable importance over the last few decades due to the increase in fossil fuel prices as well as toxic emissions of oxygen and nitrogen. The production of biodiesel via catalytic transesterification produces crude glycerol as a co-product along with biodiesel, amounting to 10% of the total biodiesel produced. Glycerol has a low value in its impure form, and the purification of glycerol requires sophisticated technologies and is an expensive process. The conversion of crude glycerol into value-added chemicals such as solketal is the best way to improve the sustainability of biodiesel synthesis using the transesterification reaction. Therefore, the conversion of crude glycerol into the solketal was investigated in a batch reactor simulation model developed by the Aspen Plus V11.0. The non-random two liquid theory (NRTL) method was used as a thermodynamic property package to study the effect of four input ketalization parameters. The model was validated with the findings of previous experimental studies of solketal synthesis using sulfuric acid as a catalyst. The influence of the following operating parameters was investigated: reaction time of 10,000 to 60,000 s, reaction temperature of 303 to 323 K, acetone to glycerol molar ratio of 2:1 to 10:1, and catalyst concentration of 0.005 to 0.03 wt %. The optimum solketal yield of 81.36% was obtained at the optimized conditions of 313 K, 9:1, 0.03 wt %, and 40,000 s. The effect of each input parameter on the ketalization process and interaction between input and output parameters was investigated by using the response surface methodology (RSM) optimizer. The relationship between independent and response variables developed by RSM fit most of the simulation data, which showed the accuracy of the model. A second-order differential equation fit the simulation data well and showed an R2 value of 0.99. According to the findings of RSM, the influence of catalyst amount, acetone to glycerol molar ratio, and reaction time were more significant on solketal yield. The effect of temperature on the performance of the reaction was not found to be significant because of the exothermic nature of the process. The findings of this study showed that biodiesel-derived glycerol can be effectively utilized to produce solketal, which can be used for a wider range of applications such as a fuel additive. However, further work is required to enhance the solketal yield by developing new heterogeneous catalysts so that the industrial implementation of its production can be made possible.
Highlights
The energy demand of the world is extensively increasing due to its exponential economic and population growth
The solketal yield in the present study utilizing the homogeneous catalyst gave higher solketal yield (81.38%) as compared to the studies of ketalization processes conducted by Vannucci et al and Li et al the findings of the present study showed the great potential of crude glycerol to be used for solketal synthesis
The optimum input and output parameters suggested by ANOVA and 3D plots are acetone to glycerol molar ratio of 8, the reaction time of 10,000 s, reaction temperature of 308 K, and catalyst concentration of 0.03 wt % and gave an optimum yield of 82.108%
Summary
The energy demand of the world is extensively increasing due to its exponential economic and population growth. Their handling and restoration is easier as compared to conventional petroleum diesel. Biodiesel is one of the cheapest energy sources that can fully replace the use of fossil fuels due to its excellent combustion and flow properties [5]. It has good lubrication properties and causes less carbon dioxide (CO2 ) emissions in comparison with conventional diesel [6,7]. The produced glycerol from the transesterification is highly impure It contains methanol and unreacted fatty acids as major impurities apart from the traces of calcium, magnesium, phosphorus, and sulfur [10]
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