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STUDY ON THE COKING REACTION KINETIC MODEL FOR GAS OIL CATALYTIC CRACKING

机译:天然气催化裂化的焦化反应动力学模型研究

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By reaction experiments and parameter estimations, three kinds of coking kinetic models for gas oil catalytic cracking were established. The best statistical fit of experiment data was obtained by the coking model for zero-order dependencies. This work points out that the catalyst activity of coking reaction was reduced linearly with coke amount deposited on the catalyst, for which the distribution of coke on catalyst was uniform. In the end, we give a conclusion that the initial coking rate and the activity reducing rate of coking reaction to coke content of catalyst of Gudao gas oil are the greatest, and that the initial coking rate and reducing rate of the catalyst of Daqing gas oil are the least.
机译:通过反应实验和参数估算,建立了三种瓦斯催化裂化的焦化动力学模型。通过焦化模型获得零级依赖性的最佳实验数据统计拟合。这项工作指出,焦炭反应的催化剂活性随沉积在催化剂上的焦炭量线性降低,为此焦炭在催化剂上的分布是均匀的。最后得出结论:孤岛粗柴油的初始焦化率和焦化反应活性降低率对焦炭含量的影响最大,大庆粗柴油的初始焦化率和催化剂还原率降低。最少。

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