固定床反应系统丙烯醛生产的优化

M. Lei, F. Lesage, M. A. Latifi, S. Tretjak
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引用次数: 1

摘要

建立了丙烯醛生产的二维固定床催化反应器模型。反应器和动力学模型已通过实验室规模和中试规模的测量确定。冷却液温度、进料速度、进口压力和温度等操作条件对丙烯醛收率和床层温度都有很大的影响。更具体地说,冷却液温度和加料速度是丙烯醛生产的两个最重要的参数。在一组不同进料速率下,优化了冷却剂温度和反应器入口温度,以在给定的反应器长度和入口压力下最大化丙烯醛的产率。确定了丙烯醛产量最高的最佳投料速率。研究了不同温度下冷却段数对丙烯醛产率的影响,结果表明对丙烯醛产率没有明显的提高。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Optimization of acrolein production in a fixed-bed reactor system
A two-dimensional fixed-bed catalytic reactor model for acrolein production has been developped. The reactor and kinetic models have been identified by using both laboratory-scale and pilot-scale measurements. Many operating conditions such as coolant temperature, feeding rate, inlet pressure and temperature have great influence on the yield of acrolein and also on the bed temperature which are two very important parameters. More specifically, the coolant temperature and feeding rate are the two most important parameters for the acrolein production. With a set of different feed rates, the coolant temperature and the reactor inlet temperature were optimized to maximise the yield of acrolein for a given reactor length and inlet pressure. There was an optimal feeding rate for the maximum yield of acrolein. The study of the influence of number of the cooling sections with different temperatures shows that there was no significant improvement in the yield of acrolein.
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