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Transesterification reaction of sunflower oil and ethanol for biodiesel synthesis in microchannel reactor: Experimental and simulation studies

机译:向日葵油与乙醇的酯交换反应在微通道反应器中合成生物柴油的实验和模拟研究

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The transesterification of vegetable oils with alcohols is the most widely used method in biodiesel synthesis, generally taking place in batch processes. However, this production is currently being explored in microdevices, due to its short residence times and high conversions. This paper presents an experimental and numerical study of biodiesel synthesis in a microdevice from sunflower oil and ethanol using sodium hydroxide as catalyst. The influence of three operating variables were studied (temperature, ethanol/oil ratio and catalyst concentration). This paper also compares the reaction performance of a batch reactor with a microdevice reactor. The highest percentages of biodiesel found for the batch process and for the microdevice were 94.1% and 95.8%, respectively. These results proved the efficiency of microdevice in the biodiesel synthesis over conventional reactors. The superior results predicted for oil conversion, production yield and esters selectivity in numerical simulations were 99.90%, 2.10 and 0.42, respectively. The transesterification process simulation and intensification can be performed numerically evaluating reaction yield and selectivity parameters. (C) 2016 Elsevier B.V. All rights reserved.
机译:植物油与醇的酯交换反应是生物柴油合成中使用最广泛的方法,通常在间歇过程中进行。然而,由于其短的停留时间和高的转化率,目前正在微型设备中探索这种生产。本文提供了一种实验装置和数值研究方法,以氢氧化钠为催化剂,在葵花籽油和乙醇中的微型装置中合成生物柴油。研究了三个操作变量(温度,乙醇/油比和催化剂浓度)的影响。本文还比较了间歇式反应器与微型装置反应器的反应性能。在批处理过程和微型设备中发现的最高生物柴油百分比分别为94.1%和95.8%。这些结果证明了微型装置在常规反应器中生物柴油合成中的效率。在数值模拟中,预测的卓越转化率分别为99.90%,2.10和0.42,分别是油转化率,产率和酯选择性。酯交换反应过程的模拟和强化可以通过数字方式评估反应收率和选择性参数。 (C)2016 Elsevier B.V.保留所有权利。

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