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管式固定床反应器中振荡操作研究
Forced oscillation of tubular fixed bed reactor
【摘要】 在单管固定床反应器中,研究了V2O5颗粒催化剂上邻二甲苯催化氧化反应过程振荡操作的特性。在反应器熔盐温度为362—366℃,空速为2000—3500h-1范围内,以浓度、空速的方波形式,进行了周期操作特性的研究。结果表明,反应过程收率与振荡周期有关,在周期为40—100s时的振荡操作与同样条件的定态操作相比,可以提高反应过程收率3%,并能改善反应器操作特性。
【Abstract】 The periodical operation of o-xylene oxidation processes over V2O5 catalysts intubular fixed bed reactor was studied. Yield of phthalic anhydride was measured undersquare-wave forced oscillation operating parameters, such as reactant concentration andspace velocity. Obvious increase of phthalic anhydride yield was found compared withsteady state values, depending upon the oscillation frequency. Some preliminary inter-pretation of these results is provided.
【关键词】 化学反应工程;
固定床;
振荡;
邻二甲苯氧化;
催化氧化;
【Key words】 chemical reaction engineering; fixed bed; oscillation; o-xylene oxidation; catalytic oxidation;
【Key words】 chemical reaction engineering; fixed bed; oscillation; o-xylene oxidation; catalytic oxidation;
- 【文献出处】 华东化工学院学报 , 编辑部邮箱 ,1987年05期
- 【被引频次】1
- 【下载频次】50