Authors: Timo Dymala a, Ernst-Ulrich Hartge a, Tao Song b, Laihong Shen c, and Stefan Heinrich a
a Hamburg University of Technology, Institute of Solids Process Engineering and Particle Technology, Denickestrasse 15, 21073 Hamburg, Germany
b School of Energy and Mechanical Engineering, Nanjing Normal University, Nanjing 210023, China
c Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China
Source: This paper was published in the 13th International Conference on Fluidized Bed Technology in 2021.
Abstract: Aim of the project “Multi-scale analysis and optimization of chemical looping gasification of biomass” of the Hamburg University of Technology (TUHH) with the Southeast University (SEU) is the detailed modeling and subsequent optimization of a Chemical Looping Gasification (CLG) process. For this purpose, the process is simulated using the multiphase particle-in-cell (MP-PIC) method, which allows a detailed simulation of even large-scale units with affordable computational efforts. This paper deals with the implementation and validation of the reaction model for the gasification reactions.
CPFD and staff have distribution rights for some publications. Contact us with any questions.