CFD Modeling Of Particle Rotation for Segregation in Bubbling Gas-Fluidized Beds
عنوان مقاله: CFD Modeling Of Particle Rotation for Segregation in Bubbling Gas-Fluidized Beds
شناسه ملی مقاله: ICHEC06_207
منتشر شده در ششمین کنگره بین المللی مهندسی شیمی در سال 1388
شناسه ملی مقاله: ICHEC06_207
منتشر شده در ششمین کنگره بین المللی مهندسی شیمی در سال 1388
مشخصات نویسندگان مقاله:
Behnaz Firouzbakht - Sharif University of Technology, Dept. of Chemical and Petroleum Engineering, Azadi Ave.,
Seyed Hossein Ahmadi Afshar - Islamic Azad University Tehran South Branch, Graduate School of Engineering, Faculty of Chemical Engineering, Tehran, Iran
Asghar Molaei Dehkordi - Sharif University of Technology, Dept. of Chemical and Petroleum Engineering, Azadi Ave.,
خلاصه مقاله:
Behnaz Firouzbakht - Sharif University of Technology, Dept. of Chemical and Petroleum Engineering, Azadi Ave.,
Seyed Hossein Ahmadi Afshar - Islamic Azad University Tehran South Branch, Graduate School of Engineering, Faculty of Chemical Engineering, Tehran, Iran
Asghar Molaei Dehkordi - Sharif University of Technology, Dept. of Chemical and Petroleum Engineering, Azadi Ave.,
A two-dimensional multi-fluid Eulerian CFD model has been improved by incorporating particle rotation using kinetic theory for rapid granular flow of slightly frictional spheres. Simulation with and without particle rotation were performed to study segregation phenomena in a bidispersed bubbling gas-fluidized bed. In this model an effective restitution coefficient was introduced. It was found that model with particle rotation better predicts the bubble dynamics and bed behavior.
کلمات کلیدی: multi-fluid flow, fluidization, hydrodynamic, kinetic theory, granular flow
صفحه اختصاصی مقاله و دریافت فایل کامل: https://civilica.com/doc/77482/