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Chemical Equilibria in the Process of Etherification of Light FCC Gasoline with Methanol

机译:轻质FCC汽油与甲醇的醚化过程中的化学平衡

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The paper presents the thermodynamic analysis of the process of etherification of light FCC gasoline with methanol. In the model presented, it is assumed that the chemical equilibria are reached only for the reactions of methanol with C_4-C_7 olefins having the double bond on a tertiary carbon atom and the reactions of isomerization of olefins and ethers do not take place. Thermodynamic data which were not available from tables (the Gibbs free energies of formation of C_7 olefins and C_6—C_8 ethers) were calculated using two essentially different group contribution methods (the Benson method and the Yoneda method) to investigate the influence of the data obtained this way on the calculated equilibrium compositions. The nonideality of the liquid phase was described by the modified UNIFAC method and by the ASOG method. In both cases very similar equilibrium compositions were obtained. The parameters were specified for which the system begins to be in the simultaneous chemical and phase (vapor—liquid) equilibrium.
机译:本文介绍了轻质催化裂化汽油与甲醇醚化过程的热力学分析。在给出的模型中,假定仅对于甲醇与在叔碳原子上具有双键的C_4-C_7烯烃的反应达到化学平衡,并且不发生烯烃和醚的异构化反应。使用两种本质上不同的基团贡献方法(Benson方法和Yoneda方法)计算了表中未提供的热力学数据(C_7烯烃和C_6-C_8醚形成的吉布斯自由能),以研究所获得数据的影响这样就可以计算出平衡组成。通过改进的UNIFAC方法和ASOG方法描述了液相的非理想性。在两种情况下,都获得了非常相似的平衡组成。规定了系统开始同时处于化学和相(汽-液)平衡状态的参数。

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