在苯乙烯生产中使用基于对苯二胺的聚合调节剂

Evgeny A. Danilov, Ilmir I. Tabrisov, N. A. Likhacheva, O. B. Prozorova
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摘要

目前,工业苯乙烯生产中使用两种试剂来防止整顿过程中的热聚合:真正的抑制剂和聚合延缓剂。在生产过程中,真正的抑制剂会与自由基发生反应,打断反应链,从而决定聚合物的分子量。聚合调节剂可降低流动性最强的自由基的浓度并缩短其寿命,从而为活性最强的自由烷基自由基提供一个氢质子。作为聚合调节剂,二硝基丁基苯酚是最有效的,根据人体接触程度,它属于第一类危险。俄罗斯的二硝基丁基苯酚主要供应国是中华人民共和国。本文考虑了用国内品牌 Inflow7007(对苯二胺的衍生物)替代活性苯乙烯聚合抑制剂的可能性。根据这组特征,新的聚合调节剂属于第三类危险物质中的中度危险物质。在工作的第一阶段,对四种聚合抑制剂进行了实验室对比研究。接下来,在现有的苯乙烯生产厂进行了一次工业实验,在此期间,逐步过渡到实验室研究选定的国产抑制剂。过渡是分阶段进行的,用 Inflow 7007 品牌的抑制剂逐步取代二硝基丁基苯酚。在整个工业试验运行期间,对苯乙烯原料分离塔立方体液体中的聚合物含量进行了监测。研究结果表明,所建议的抑制系统具有很高的效率。根据中试期间的分析控制结果,可以降低立方液体中的平均聚合物含量。除了提高苯乙烯生产中的聚合抑制效率外,使用拟议的聚合调节剂还能解决进口替代问题,提高工人安全,降低环境风险。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
THE USE OF A POLYMERIZATION MODERATOR BASED ON PARA-PHENYLENEDIAMINES IN THE PRODUCTION OF STYRENE
Currently, two types of reagents are used in industrial styrene production to prevent thermal polymerization during the rectification process: true inhibitors and polymerization retarders. Consumed in the process, the true inhibitor reacts with free radicals and breaks the reaction chain, determining the molecular weight of the polymer. The polymerization moderator reduces the concentration of the most mobile radicals and their lifetime, giving a hydrogen proton to the most reactive free alkyl radical. As a polymerization moderator, dinitrobutylphenol is the most effective, which, according to the degree of exposure to the body, belongs to the first class of danger. The main supplier of dinitrobutylphenol to Russia is the People's Republic of China. The paper considers the possibility of replacing the active styrene polymerization inhibitor with the domestic brand Inflow7007, which is a derivative of para-phenylenediamine. According to the set of characteristics, the new polymerization moderator belongs to moderately dangerous substances of the third hazard class.At the first stage of the work, comparative laboratory studies of four polymerization inhibitors were carried out. The dependence of the inhibitory ability on the concentration of the polymerization moderator, the kinetics of the process was studied, and a comparative analysis of domestic and imported analogues of inhibitory reagents was carried out.Next, an experimental industrial run was conducted at an existing styrene production plant, during which a gradual transition to a domestic inhibitor selected as a result of laboratory research was carried out. The transition was carried out in stages with the gradual replacement of dinitrobutylphenol with an inhibitor of the Inflow 7007 brand. Throughout the entire industrial pilot run, the polymer content in the cubic liquid of the raw styrene separation column was monitored. The conducted studies have shown the high efficiency of the proposed inhibitory system. According to the results of analytical control during the period of pilot tests, it was possible to reduce the average polymer content in the cubic liquid. In addition to increasing the effectiveness of polymerization inhibition in styrene production, the use of the proposed polymerization moderator will solve the problem of import substitution, increase worker safety, and reduce environmental risks.
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