Industrial Methanol from Syngas: Kinetic Study and Process Simulation

被引：31

作者：

De Maria, Raquel ^{[1
]}

Diaz, Ismael ^{[1
]}

Rodriguez, Manuel ^{[1
]}

Saiz, Adrian ^{[1
]}

机构：

[1] Tech Univ Madrid, Sch Ind Engn, Chem Technol Lab, Madrid 28006, Spain

来源：

INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING | 2013年 / 11卷

关键词：

methanol; reactor model; process simulation;

D O I：

10.1515/ijcre-2013-0061

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

In this study, a detailed rigorous kinetic model is proposed for the industrial production of methanol taking into account changes in total mole flowrate. The kinetic model proposed is compared with the one proposed in literature (Rezaie et al., Chem Eng Process Process Intensification 2005; 44: 911-21), showing significant differences in terms of compositions and total mole flow. A complete simulation of the methanol production process is developed with a commercial software. The rigorous reactor model is integrated in the simulation using the CAPE OPEN standard. Flowsheet simulation is carried out, and results show small differences with those found in previous studies (Luyben, Ind Eng Chem Res 2010; 49: 6150-63).

引用

页码：469 / 477

页数：9

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