CATALYTIC CRACKING OF METHYLCYCLOHEXANE OVER SILICA ALUMINA CATALYST IN GAS FLUIDIZED BED
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概要
- 論文の詳細を見る
This paper presents a simulation model to predict the reaction performance of a fluidized bed from the operating conditions. The simulation model was derived from the observation of bubble behavior, and was developed in a form which can elucidate the conversion and selectivity with catalyst fouling. The model was applied to methylcyclohexane cracking data, and unknown parameters in the model were estimated by a non-linear regression technique. It was confirmed that the model is applicable to the performance of a fiuidized bed reactor.
- 公益社団法人 化学工学会の論文
著者
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Tone Setsuji
Department Of Chemical Engineering Faculty Of Engineering Science Osaka University
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OTAKE TSUTAO
Department of Chemical Engineering, Faculty of Engineering Science, Osaka University
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SEKO HIROYASU
Department of Chemical Engineering, Faculty of Engineering Science, Osaka University
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MARUYAMA HISAO
Department of Chemical Engineering, Faculty of Engineering Science, Osaka University
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