Numerical investigation of the back-mixing and non-uniform characteristics in the three-dimensional full-loop circulating fluidized bed combustor with six parallel cyclones
- 1. School of Chemical and Biomedical Engineering, Nanyang Technological University, Singapore 637459 (Singapore)
- 2. State Key Laboratory of Clean Energy Utilization, Energy Department, Zhejiang University, Hangzhou 310027 (China)
- 3. State Key Laboratory of Complex Nonferrous Metal Resources Clean Utilization, Kunming University of Science and Technology, Kunming 650093, Yunnan (China)
- 4. Singapore Membrane Technology Center, Nanyang Environment and Water Research Institute, Nanyang Technological University, Singapore 637141 (Singapore)
Description
Highlights: • CFD-DEM for high-fidelity simulation of the 3D full-loop CFB with six cyclones. • Particle-scale data on solid dispersion, force, mass distribution and back-mixing. • Solid dispersion behavior significantly different among the three directions. • Solid loading in the middle cyclone twice that of the two adjacent ones. • 50% and 48% of the total mass distributed respectively in the riser and standpipes. -- Abstract: The design and operation of circulating fluidized bed (CFB), which offers excellent heat and mass transfer, remain challenging because of the lack of a comprehensive understanding. CFD-DEM is used here for the high-fidelity simulation of the three-dimensional full-loop CFB with six parallel cyclones. Detailed information on the particle-scale information (i.e., solid dispersion, particle rotational speed, fluid and collision forces, mass distribution, and backing-mixing intensity) throughout the CFB are presented for the first time. Interesting results include: (i) the solid dispersion behavior is significantly different among the three directions; (ii) the solid loading in the middle cyclone on one side of the riser is twice that of the two adjacent ones, and this non-uniform distribution underscores the need for full-loop simulation for the CFB with multiple cyclones; (iii) the solid dispersion coefficients in all three directions, fluid force, collision force and particle rotational speed are similar among the six cyclones and correspondingly the standpipes; and (iv) approximately 50% and 48% of the total material are distributed respectively in the riser and standpipes. The results obtained provide valuable insights regarding the mass loading, particle-scale characteristics and non-uniform distribution of the solid phase throughout the entire CFB.
Availability note (English)
Available from http://dx.doi.org/10.1016/j.applthermaleng.2019.03.032Additional details
Identifiers
- DOI
- 10.1016/j.applthermaleng.2019.03.032;
- PII
- S1359431118336391;
Publishing Information
- Journal Title
- Applied Thermal Engineering
- Journal Volume
- 153
- Journal Page Range
- p. 524-535
- ISSN
- 1359-4311
- CODEN
- ATENFT
INIS
- Country of Publication
- United Kingdom
- Country of Input or Organization
- International Atomic Energy Agency (IAEA)
- INIS RN
- 54124932
- Subject category
- S42: ENGINEERING;
- Descriptors DEI
- CIRCULATING SYSTEMS; COMPUTERIZED SIMULATION; FLUIDIZED BEDS; FLUIDIZED-BED COMBUSTORS; HEAT; MASS DISTRIBUTION; MASS TRANSFER; SOLIDS; THREE-DIMENSIONAL CALCULATIONS; TWO-PHASE FLOW
- Descriptors DEC
- COMBUSTORS; DISTRIBUTION; ENERGY; FLUID FLOW; SIMULATION; SPATIAL DISTRIBUTION
Optional Information
- Copyright
- Copyright (c) 2019 Elsevier Ltd. All rights reserved.