摘要
The cyclohexanone peroxide reaction process, one of the eighteen hazardous chemical processes identified in China, is performed in indirectly cooled semibatch reactors. The peroxide reaction is added to a mixture of hydrogen peroxide and nitric acid, which form heterogeneous liquid-liquid systems. A simple and general procedure for building boundary and temperature diagrams of peroxide process is given here to account for the overall kinetic expressions. Such a procedure has been validated by comparison with experimental data. Thermally safer operating parameters were obtained at laboratory scale, and the scaled-up procedure was performed to give the minimum dosing time in an industrial plant, which is in favor of maximizing industrial reactor productivity. The results are of great significance for governing the peroxide reaction process apart from the thermal runaway region. It also greatly aids in determining optimization on operating parameters in industrial plants.
| 源语言 | 英语 |
|---|---|
| 页(从-至) | 6-14 |
| 页数 | 9 |
| 期刊 | Thermochimica Acta |
| 卷 | 618 |
| DOI | |
| 出版状态 | 已出版 - 20 10月 2015 |
联合国可持续发展目标
此成果有助于实现下列可持续发展目标:
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可持续发展目标 3 良好健康与福祉
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可持续发展目标 12 负责任消费和生产
指纹
探究 'Safer operating conditions and optimal scaling-up process for cyclohexanone peroxide reaction' 的科研主题。它们共同构成独一无二的指纹。引用此
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