Numerical simulation of two-phase flow characteristics in spray drying towerNumerical simulation of two-phase flow characteristics in spray drying tower
热能科学研究|更新时间:2025-09-28
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Numerical simulation of two-phase flow characteristics in spray drying towerNumerical simulation of two-phase flow characteristics in spray drying tower
Numerical simulation of two-phase flow characteristics in spray drying towerNumerical simulation of two-phase flow characteristics in spray drying tower
热力发电2012年41卷第11期 页码:17-21
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纸质出版:2012
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Numerical simulation of two-phase flow characteristics in spray drying towerNumerical simulation of two-phase flow characteristics in spray drying tower[J]. 热力发电, 2012,41(11):17-21.
Numerical simulation of two-phase flow characteristics in spray drying towerNumerical simulation of two-phase flow characteristics in spray drying tower[J]. Thermal power generation, 2012, 41(11): 17-21.
Numerical simulation of two-phase flow characteristics in spray drying towerNumerical simulation of two-phase flow characteristics in spray drying tower[J]. 热力发电, 2012,41(11):17-21.DOI:
Numerical simulation of two-phase flow characteristics in spray drying towerNumerical simulation of two-phase flow characteristics in spray drying tower[J]. Thermal power generation, 2012, 41(11): 17-21.DOI:
Numerical simulation of two-phase flow characteristics in spray drying towerNumerical simulation of two-phase flow characteristics in spray drying tower
摘要
To optimize the two-phase flow characteristics of flue gas and slurry droplets in spray drying tower
an equalizing plate was installed inside the tower.The Fluent software package
turbulence model and the stochastic model of droplet track were adopted in numerical simulation.Results showed that
the average speed of flue gas along the tower axis was the greatest;the temperature variation in the vicinity of spray nozzle was the largest;when the inlet flue gas speed v was 4 m / s
the temperature gradient variation inside the tower was the maximum
and the slurry droplets full filled the tower;with an increase in the diameter of hole area on equalizing plate
the resistance in tower was gradually decreased
and the viscosity to the wall of slurry droplets first increased and then reduced.