2005
DOI: 10.1080/10407780590948936
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Numerical Study of Transient and Steady-State Natural Convection and Surface Thermal Radiation in a Horizontal Square Open Cavity

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Cited by 62 publications
(16 citation statements)
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“…They observed that cavity receiver inclination angle significantly influences the convective Nusselt number and not the radiation Nusselt number. Hinojosa et al [16] used the Boussinesq approximation in the numerical study of natural convection and surface thermal radiation in an open cavity. Reddy and Sendhil Kumar [17] reported numerical results of natural convection and radiation heat transfer in a modified cavity receiver.…”
Section: Introductionmentioning
confidence: 99%
“…They observed that cavity receiver inclination angle significantly influences the convective Nusselt number and not the radiation Nusselt number. Hinojosa et al [16] used the Boussinesq approximation in the numerical study of natural convection and surface thermal radiation in an open cavity. Reddy and Sendhil Kumar [17] reported numerical results of natural convection and radiation heat transfer in a modified cavity receiver.…”
Section: Introductionmentioning
confidence: 99%
“…To further validate the present numerical code, natural convection in square open cavities has been numerically analyzed. One of the initial numerical studies on single component natural convection in an open enclosure was performed by Chan and Tien [11,12]; Angirasa et al [13]; Hinojosa et al [16]. For this comparison, solutions presented in Table 1 are obtained for Ra = 10 3 -10 7 , Pr = 1.0 in a square cavity where the vertical wall facing to the opening is maintained at uniform and higher temperature, while the horizontal walls are adiabatic.…”
Section: Numerical Technique and Code Validationmentioning
confidence: 98%
“…The solution of elliptic partial differential equations of natural convection flow in open cavities is found to be highly sensitive to the boundary conditions at the entry and exit [11][12][13][14][15][16][17]. In the present work, the derivative of tangential velocity is set at zero and the longitudinal velocity is obtained by the mass balance at the boundary cells [12].…”
Section: Boundary Conditionsmentioning
confidence: 99%
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“…Foregoing equations are emerging the dimensionless parameters: (9) where, Le represents the ratio between the thermal and compositional diffusivities. For liquid solutions, thermal diffusivity is considerably higher than mass diffusivity, and this is one of the causes of many remarkable patterns of these flows, like convective cells separated by sharp interfaces [13,14].…”
Section: Governing Equationsmentioning
confidence: 99%