Hydrodynamic-thermal boundary layer development and mass transfer characteristics of a circular cylinder in confined flow

Autor: A. Alper Ozalp, Ibrahim Dincer
Přispěvatelé: Uludağ Üniversitesi/Mühendislik Fakültesi/Makine Mühendisliği Bölümü., Özalp, Abdurrahman Alper, ABI-6888-2020
Rok vydání: 2010
Předmět:
Low-reynolds number
Heat exchangers
Literature data compilation
Circular cylinders
Forced-convection
Cylinder (engine)
law.invention
Engineering
Stagnation points
law
Heat transfer
Moisture diffusivity
Mass transfer
Mixed convection
Convection heat-transfer
Horizontal annulus
Front face
General Engineering
Condensed Matter Physics
Stagnation point
Fluid-flow
Thermal activity
Alternating direction implicit method
Boundary layer
Heat transfer value
Thermodynamics
Boundary layers
Thermal field
Mass transfer coefficient
Materials science
Engineering
mechanical
Square cylinder
Thermal diffusivity
Separation
Thermal boundary layer
Fluid dynamics
Blockage
Numerical-simulation
Moisture distribution
Moisture
Vortex systems
Flow and heat transfer
Wall shear
Vortex
Square Cylinder
Nusselt Number
Mixed Convection
Hydrodynamics
Zdroj: International Journal of Thermal Sciences. 49:1799-1812
ISSN: 1290-0729
DOI: 10.1016/j.ijthermalsci.2010.04.016
Popis: The effects of blockage on the hydrodynamic, thermal and mass transfer characteristics of a circular cylinder (CC) and their association with each other are investigated numerically, by considering the influence of blockage (beta=0.333-0.800) on the flow and heat transfer mechanisms in conjunction with moisture diffusivity (D=1 x 10(-8)-1 x 10(-5) m(2)/s) to show how much mass transfer behavior and phenomena are affected. As some comprehensive ANSYS-CFX runs are performed in the hydrodynamic and thermal fields around the CC, the moisture distributions within the CC are evaluated by Alternating Direction implicit method. It is determined that blockage causes thinner hydrodynamic and thermal boundary layers, rises the frictional and thermal activities, and shifts the separation locations (theta(s)) downstream to theta(s)=50.20 degrees, 41.98 degrees and 37.30 degrees for beta=0.333, 0.571 and 0.800. In the complete blockage scenario set, stagnation point heat transfer values are evaluated to be above those of the back-face, signifying the superior heat transfer enhancing capability of the stagnation point momentum activity when compared with the impact of downstream vortex system. The influence of moisture diffusivity on the overall drying times is determined to advance with stronger blockage. As the back face mass transfer coefficients (h(m-bf)) rise with a high beta, the contrary is valid for front face values (h(m-ff)), with the interpreting ratios of (h) over bar (m-bf)/(h) over bar (m)=0.51 and 0.57 and (h) over bar (m-ff)/(h) over bar (m)=1.49 and 1.43 for beta=0.333 and 0.800.
Databáze: OpenAIRE
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