Mononitration of N-(4-Methoxyphenyl)acetamide in continuous-flow: Kinetics study and process optimization

IF 3.9 3区 工程技术 Q3 ENERGY & FUELS Chemical Engineering and Processing - Process Intensification Pub Date : 2025-02-01 Epub Date: 2024-12-16 DOI:10.1016/j.cep.2024.110136
Zhiqun Yu , Lishan Geng , Zhaoyang Mu , Jiadi Zhou , Bingbing Chen , Yuyu Yang
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Abstract

Mononitration products of N-(4-Methoxyphenyl)acetamide (NMA) are intermediates of various mature products. However, for the nitration of NMA, N-(4-methoxy-2-nitrophenyl)acetamide (2-NMA) and N-(4-methoxy-3-nitrophenyl) acetamide (3-NMA) will be produced at the same time, making it difficult to control the selectivity of single nitration product, and no kinetics study has ever been reported before. To comprehend the high regioselectivity nitration of NMA more deeply, a microfluidic system was developed to evaluate the reaction kinetics of NMA nitration. At first, two different systems for nitration were identified. Then, the kinetics parameters for these two systems were determined. Next, a series of validation experiments were designed to show the accuracy of the kinetic model. In the end, to obtain a controlled selectivity, the effects of reaction temperature, initial concentration and molar ratio were investigated through the model simulation. Under the conditions optimized by the kinetic model, the selectivity for both 2-NMA and 3-NMA could achieve above 99.5 %, but due to the changes in the properties of the reaction solution, it was extremely difficult to achieve in practice. Ultimately, within the feasibility range of the kinetic model, 98.4 % selectivity of 2-NMA and 96.1 % selectivity of 3-NMA were obtained in the microreactor, respectively.

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N-(4-甲氧基苯基)乙酰胺连续流单硝化动力学研究及工艺优化
N-(4-甲氧基苯基)乙酰胺(NMA)的单硝化产物是各种成熟产物的中间体。但在NMA的硝化过程中,会同时生成N-(4-甲氧基-2-硝基苯基)乙酰胺(2-NMA)和N-(4-甲氧基-3-硝基苯基)乙酰胺(3-NMA),难以控制单个硝化产物的选择性,动力学研究也未见报道。为了更深入地了解NMA的高区域选择性硝化,开发了一种微流控系统来评估NMA硝化反应动力学。首先,确定了两种不同的硝化系统。然后,确定了两种体系的动力学参数。接下来,设计了一系列的验证实验来验证动力学模型的准确性。最后,通过模型模拟考察了反应温度、初始浓度和摩尔比对反应选择性的影响。在动力学模型优化的条件下,2-NMA和3-NMA的选择性均可达到99.5%以上,但由于反应溶液性质的变化,在实际应用中很难达到。最终,在动力学模型的可行范围内,微反应器中2-NMA的选择性分别达到98.4%和96.1%。
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来源期刊
CiteScore
7.80
自引率
9.30%
发文量
408
审稿时长
49 days
期刊介绍: Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.
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