Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
6588076 | Chemical Engineering Journal | 2013 | 8 Pages |
Abstract
The Euler-Euler modeling approach was employed to simulate the coal combustion in a circulating fluidized bed combustor. The unsteady processes of gas-solid two phase flow, heat transfer, mass transfer and chemical reactions were considered. By numerical simulation, distributions of pressure, solid volume fraction, temperature and gas concentrations (O2, CO2, H2O, CO, NO and SO2) were studied in O2/CO2 combustion mode (mixture of O2 and CO2 from gas bottles as oxidant) and O2/RFG combustion mode (mixture of O2 and recycled flue gas as oxidant) with O2 concentration range of 21-40%. Calculations were made for two cases, maintaining the same coal feed rate and maintaining the same oxidant volume flow rate. Simulated temperature distribution, pressure distribution and outlet gas concentrations were validated by the experimental data in 30% O2/70% CO2 atmosphere.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Wu Zhou, Changsui Zhao, Lunbo Duan, Xiaoping Chen, Daoyin Liu,