Cl2+CO气催化合成金红石的氯化动力学

Sungkook Hong, So-Yeong Lee, H. Sohn
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引用次数: 0

摘要

在流化床中研究了二氧化氯和一氧化碳混合气选择性氯化钛矿制备合成金红石的氯化动力学。考察了反应温度、反应时间、Cl2 / CO分压(Cl³CO)对TiCl4转化率的影响。在高Cl³CO条件下,TiCl4的转化率较低。对比高CO分压的化学计量转化率和实验结果,认为CO分压比Cl2分压更有效。考虑到颗粒的多孔结构,确定合成金红石氯化反应的控速步骤为化学反应,计算出活化能为53.77 kJ/mol。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Chlorination Kinetics of Synthetic Rutile with Cl2+CO Gas
The chlorination kinetics of synthetic rutile prepared by selective chlorination of ilmenite with Cl2 and CO gas mixture were studied in a fluidized bed. The effects of reaction temperature, reaction time, and the ratio of Cl2 and CO partial pressure (ClCO ) on the conversion rate of TiCl4 were investigated. The conversion rate of TiCl4 was low under the high ClCO conditions. Moreover, it was considered that the partial pressure of CO gas was more effective than that of Cl2 gas when comparing the stoichiometric conversion rate and experimental results of high CO partial pressure. Considering the porous structure of particles, the rate controlling step of the chlorination of synthetic rutile was determined to be chemical reaction and the activation energy was calculated as 53.77 kJ/mol.
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