Fathiganjehlou A, Peters E A J F, Buist K A, Kuipers J A M
Multiphase Reactors Group, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, Postbus, 5600 MB Eindhoven, The Netherlands.
Ind Eng Chem Res. 2024 Oct 3;63(41):17662-17678. doi: 10.1021/acs.iecr.4c01727. eCollection 2024 Oct 16.
In this work, a 3D pore network model (PNM) is introduced for modeling reaction-diffusion phenomena, with and without coupled heat transfer, in a spherical porous catalyst particle. The particle geometry is generated by packing thousands of microspheres inside a large sphere to represent the 3D geometry, porosity, and tortuosity of a spherical catalyst particle. A pore-network representation is extracted from this geometry, and a PNM for diffusion-reaction and heat conduction is constructed. This newly proposed particle-scale PNM allows for the application of realistic 3D nonuniform boundary conditions on the particle's surface, which is commonly encountered in slender packed-bed reactors. Concentration profiles inside the particle, and effectiveness of the reactions, is analyzed.
在这项工作中,引入了一种三维孔隙网络模型(PNM),用于模拟球形多孔催化剂颗粒中有无耦合传热情况下的反应扩散现象。通过在大球体内填充数千个微球来生成颗粒几何形状,以表示球形催化剂颗粒的三维几何形状、孔隙率和曲折度。从该几何形状中提取孔隙网络表示,并构建用于扩散反应和热传导的PNM。这种新提出的颗粒尺度PNM允许在颗粒表面应用实际的三维非均匀边界条件,这在细长填充床反应器中很常见。分析了颗粒内部的浓度分布以及反应的有效性。