Validation and application of a multiphase CFD model for hydrodynamics, temperature field and RTD simulation in a pilot-scale biomass pyrolysis vapor phase upgrading reactor
Autor: | Katherine R. Gaston, Xi Gao, Gavin M. Wiggins, James E. Parks, Kristin Smith, William A. Rogers, Tingwen Li |
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Rok vydání: | 2020 |
Předmět: |
business.industry
General Chemical Engineering Nuclear engineering Multiphase flow Mixing (process engineering) 02 engineering and technology General Chemistry Computational fluid dynamics Chemical reactor 010402 general chemistry 021001 nanoscience & nanotechnology Residence time distribution 01 natural sciences Industrial and Manufacturing Engineering 0104 chemical sciences Volumetric flow rate Environmental Chemistry Environmental science Fluidized bed combustion 0210 nano-technology Transport phenomena business |
Zdroj: | Chemical Engineering Journal. 388:124279 |
ISSN: | 1385-8947 |
DOI: | 10.1016/j.cej.2020.124279 |
Popis: | Accurate prediction of transport phenomena is critical for VPU reactor design, optimization, and scale-up. The current study focused on the validation and application of a multiphase CFD model within an open-source code MFiX for hydrodynamics, temperature field, and residence time distribution (RTD) simulation in a non-reacting circulating fluidized bed riser for biomass pyrolysis vapor phase upgrading (VPU). First, an Eulerian-Eulerian approach three-dimensional CFD model was employed to simulate the pilot-scale VPU riser on the supercomputer Joule. Excellent quantitative agreement between experimental and simulated results was achieved for pressure drops and temperature field in a range of operating conditions. Then the validated multiphase CFD model was applied to predict gas and solid residence time distributions (RTDs) since prediction and analysis of RTD is an important tool to study the complex multiphase flow behavior and mixing inside chemical reactors. The predictions show that solid mean residence time is 3.5 times the gas residence time; the solid RTD is more sensitive to the process gas flow rate than the solids circulation rate. |
Databáze: | OpenAIRE |
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