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Validation of the Kinetics of the Hydrogen Peroxide Propene Oxide Process in a Dynamic Continuous Stirred Tank Reactor
Industrial & Engineering Chemistry Research ( IF 3.8 ) Pub Date : 2018-11-20 , DOI: 10.1021/acs.iecr.8b03233
V. Russo 1 , E. Santacesaria 2 , R. Tesser 1 , R. Turco 1 , R. Vitiello 1 , M. Di Serio 1, 3
Affiliation  

A continuous hydrogen peroxide propene oxide (HPPO) lab-scale pilot plant was designed and tested for the production of propene oxide via HPPO process. The plant was equipped with a continuous stirred tank reactor, able to work under nitrogen pressure with liquid propene. Attention was paid to the feed system and the plant control, the lab-scale pilot plant being completely automated. Hydraulic tests were performed to check the performance of the plant; a fluid-dynamic characterization was conducted to evaluate the residence time distribution. Propene oxide synthesis experiments were performed to evaluate both hydrogen peroxide conversion and propene oxide selectivity. The collected data were interpreted with a recently published kinetics, validating the developed model, obtaining satisfactory results, also in simulating the start-up transient state of the reactor. The model can be considered of high utility in designing and optimizing HPPO process, to achieve high reactant conversions and propene oxide yields.

中文翻译:

动态连续搅拌釜反应器中过氧化氢环氧丙烷过程动力学的验证

设计并测试了连续式过氧化氢环氧丙烷(HPPO)实验室规模的中试装置,用于通过HPPO工艺生产环氧丙烷。该工厂装备有连续搅拌釜反应器,该反应器能够在氮气压力下与液态丙烯一起工作。注意进料系统和工厂控制,实验室规模的中试工厂是完全自动化的。进行了水压测试以检查设备的性能。进行了流体动力学表征以评估停留时间分布。进行环氧丙烷合成实验以评估过氧化氢转化率和环氧丙烷选择性。使用最近发布的动力学解释收集的数据,验证开发的模型,获得令人满意的结果,在模拟反应堆的启动瞬态时也是如此。该模型可被认为在设计和优化HPPO工艺方面具有很高的实用性,可实现高的反应物转化率和环氧丙烷收率。
更新日期:2018-11-21
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