Modeling of a Methanol Synthesis Reactor for Storage of Renewable Energy and Conversion of CO2 - Comparison of Two Kinetic Models

被引:33
|
作者
Meyer, Johannes J. [1 ]
Tan, Pepe [1 ]
Apfelbacher, Andreas [1 ]
Daschner, Robert [1 ]
Hornung, Andreas [1 ,2 ,3 ,4 ]
机构
[1] Inst Branch Sulzbach Rosenberg, Fraunhofer UMSICHT, Maxhutte 1, D-92237 Sulzbach Rosenberg, Germany
[2] Univ Birmingham, Sch Chem Engn, Birmingham B15 2TT, W Midlands, England
[3] Univ Bologna, Sch Sci, Bologna, Italy
[4] Univ Erlangen Nurnberg, D-91054 Erlangen, Germany
关键词
Fixed-bed reactor; Kinetic model; Methanol synthesis; Reactor modeling; Simulation; DESIGN; CU/ZNO/AL2O3; LIMITATIONS; SIMULATION;
D O I
10.1002/ceat.201500084
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The storage of renewable energy over a long time period, via methanol synthesis, will become very important to reach a greenhouse gas-free energy supply. A steady-state methanol synthesis flowsheet, containing a 2D pseudo-homogeneous reactor, flash, and recycle, is modeled in MATLAB. With the kinetic models of Graaf and Bussche & Froment, two frequently used kinetic models for conventional methanol synthesis are compared and evaluated for applicability regarding methanol synthesis from CO2/H-2. The results are presented for different cases of synthesis gas compositions. Both kinetic models produce similar results when the system is limited by thermodynamic equilibrium. However, differences in reaction rates are observable from the reactor axial molar component profiles of the reaction products.
引用
收藏
页码:233 / 245
页数:13
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