微型反应器
放热反应
萘
硝化作用
产量(工程)
连续反应器
间歇式反应器
停留时间(流体动力学)
化学
热失控
反应量热计
化学工程
热力学
材料科学
有机化学
量热法
催化作用
复合材料
功率(物理)
物理
岩土工程
电池(电)
工程类
作者
Feng Xu,Zhiquan Chen,Lei Ni,Gang Fu,Jian Liu,Juncheng Jiang
标识
DOI:10.1021/acs.oprd.3c00282
摘要
In this work, the continuous flow nitration of naphthalene to 1-nitronaphthalene was systematically studied from the microreactor to mesoscale flow reactor and the safety issues during the reaction process were investigated. The effect of the molar ratio of nitric acid to naphthalene, residence time, reaction temperature, and sulfuric acid strength on the reaction process was comprehensively investigated in the microreactor. Under optimal conditions, the reaction yield could reach 94.96%. Due to the rapid exothermic characteristics of nitration, a quick heat transfer assessment was proposed to obtain the temperature profile during optimal conditions. It was found that the maximum overtemperature during the reaction was only 3.78 °C, which was consistent with the high yield under the optimal conditions. Then a scale-up of the microreactor to production was realized by a dimension-enlarging strategy. In the mesoscale flow reactor, the influence of volumetric flow rates was investigated. The annual output of the flow reactor could reach 2643 kg·a–1 while the highest overtemperature inside the reactor channel well exceeded 17.1 °C. In addition, a conventional semibatch experiment was carried out in the batch calorimeter RC1e to explore the reaction's exothermic characteristics. Finally, the performances of the two reactors were compared, showing that the continuous flow reactor had more advantages than the batch reactor in economic benefit and inherent safety.
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