Double diffusive natural convection driven by simultaneous temperature and concentration gradients is governed by the Rayleigh number Ra, which represents the balance between buoyancy and viscous forces. The Rayleigh number determines the transition from conduction-dominated to convection-dominated heat and mass transfer. While most existing studies rely on two-dimensional simplifications, this paper presents a three-dimensional numerical investigation of the effect of the Rayleigh number Ra on steady, laminar double-diffusive natural convection in a rectangular enclosure with an aspect ratio Ar of 0.5. The governing equations are solved using the finite volume method with the SIMPLE algorithm on a staggered grid. Parametric simulations are performed for Ra = 104, 5×104, 105, and 106, with fixed Prandtl number Pr = 7.0, Lewis number Le = 2.5, and buoyancy ratio N = 10. The results reveal that increasing the Ra from 104 to 105 leads to a clear transition from conduction-dominated to convection-dominated heat and mass transfer. At Ra = 104, profiles are smooth, and gradients are weak; at Ra = 105, sharp boundary layers and strong circulation appear. Concentration profiles become sharper and more localized with increasing Ra. At high Ra, solutal stratification occurs, and solute remains confined near the source, indicating enhanced solutal buoyancy effects. Temperature profiles evolve from nearly parallel isotherms (conduction) to wavy, distorted patterns with thermal plumes (convection). Vertical heat transfer increases significantly with Ra. Velocity fields become stronger and more organized as Ra increases. At Ra = 105, well-defined primary and secondary circulation cells produce intense upwelling and downwelling, with velocities an order of magnitude higher than at low Ra. The 3-dimensional nature of the flow reveals anisotropy: the primary circulation plane (z-y) shows the strongest response, but secondary planes (x-y, x-z) also exhibit significant changes with Ra. These results provide valuable benchmarks for engineering applications where controlling the strength of buoyancy-driven convection is crucial, such as in solar collectors, building ventilation, and drying systems. The finite volume method proves to be an effective tool for such 3-dimensional parametric studies.
| Published in | International Journal of Fluid Mechanics & Thermal Sciences (Volume 12, Issue 3) |
| DOI | 10.11648/j.ijfmts.20261203.11 |
| Page(s) | 51-61 |
| Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
| Copyright |
Copyright © The Author(s), 2026. Published by Science Publishing Group |
Rayleigh Number, Double-Diffusive Convection, Finite Volume Method, 3D Flow, Heat and Mass Transfer
| [1] | Veronis, G. (1965). On finite amplitude instability in thermohaline convection. Journal of Marine Research, 23, 1-17. |
| [2] | Turner, J. S. (1965). The coupled turbulent transports of salt and heat across a sharp density interface. International Journal of Heat and Mass Transfer, 8(5), 759-767. |
| [3] | Ho, C. J., & Chang, J. Y. (1994). A study of natural convection heat transfer in a vertical rectangular enclosure with two-dimensional discrete heating: Effect of aspect ratio. International Journal of Heat and Mass Transfer, 37(6), 917-925. |
| [4] | Mamou, M., Vasseur, P., & Bilgen, E. (1996). Analytical and numerical study of double diffusive convection in a vertical enclosure. Heat and Mass Transfer, 32(1-2), 115-125. |
| [5] | Mohamad, A. A., & Bennacer, R. (2002). Double-diffusion natural convection in an enclosure filled with a saturated porous medium. Numerical Heat Transfer, Part A: Applications, 41(5), 453-470. |
| [6] | Costa, V. A. F. (2004). Double-diffusive natural convection in parallelogrammic enclosures. International Journal of Heat and Mass Transfer, 47(14-16), 2913-2926. |
| [7] | Bilgen, E., & Yedder, R. B. (2007). Natural convection in enclosure with heating and cooling by sinusoidal temperature profiles on one side. International Journal of Heat and Mass Transfer, 50(1-2), 139-150. |
| [8] |
Abu-Nada, E., Masoud, Z., Oztop, H. F., & Campo, A. (2010). Effect of nanofluid variable properties on natural convection in enclosures. International Journal of Thermal Sciences, 49(3), 479-491.
https://doi.org/10.1016/j.ijthermalsci.2010.07.006 International Journal of Thermal Sciences, 49(3), 479-491. |
| [9] | Kuznetsov, G. V., & Sheremet, M. A. (2011). Natural convection in an enclosure with double diffusive conjugate natural convection. International Journal of Heat and Mass Transfer, 54(1-3), 456-465. |
| [10] | Anderson, D., Tannehill, J. C., Pletcher, R. H., Munipalli, R., & Shankar, V. (2020). Computational Fluid Mechanics and Heat Transfer. CRC Press. |
| [11] | Belazizia, A., Benissaad, S., & Abboudi, S. (2012). Double-diffusion natural convection of binary fluid in a square enclosure with top active vertical wall. Advances in Theoretical and Applied Mechanics, 5(3), 119-131. |
| [12] | Elsherbiny, S. M., & Ragab, E. H. (2013). Laminar natural convection in inclined rectangular cavities with a localized heat source. Alexandria Engineering Journal, 52(3), 249-257. |
| [13] | Ridha, B., & Mounir, B. (2014). Effect of buoyancy ratio on double-diffusive mixed convection in a double-lid driven rectangular cavity. Heat Transfer Engineering, 35(5), 456-467. |
| [14] | Falahat, A. (2014). Effect of aspect ratio on laminar natural convection in a partially heated enclosure. Universal J. Mech. Eng, 2(1), 28-33. |
| [15] | Aly, A. M., & Raizah, Z. A. (2016). Double-diffusive natural convection in an enclosure filled with nanofluid using ISPH method. Alexandria Engineering Journal, 55(4), 3037-3052. |
| [16] | Aghighi, M., Ammar, A., & Masoumi, H. (2022). Double-diffusive natural convection of Casson fluids in an enclosure. International Journal of Mechanical Sciences, 236, 107754. |
APA Style
Musili, P. N., Okongo, M., Murwayi, A. L. M. (2026). Effect of Rayleigh Number on Double-Diffusive Natural Convection Flow in a Rectangular Enclosure. International Journal of Fluid Mechanics & Thermal Sciences, 12(3), 51-61. https://doi.org/10.11648/j.ijfmts.20261203.11
ACS Style
Musili, P. N.; Okongo, M.; Murwayi, A. L. M. Effect of Rayleigh Number on Double-Diffusive Natural Convection Flow in a Rectangular Enclosure. Int. J. Fluid Mech. Therm. Sci. 2026, 12(3), 51-61. doi: 10.11648/j.ijfmts.20261203.11
@article{10.11648/j.ijfmts.20261203.11,
author = {Peninnah Ngina Musili and Mark Okongo and Alice Lunani Mulama Murwayi},
title = {Effect of Rayleigh Number on Double-Diffusive Natural Convection Flow in a Rectangular Enclosure},
journal = {International Journal of Fluid Mechanics & Thermal Sciences},
volume = {12},
number = {3},
pages = {51-61},
doi = {10.11648/j.ijfmts.20261203.11},
url = {https://doi.org/10.11648/j.ijfmts.20261203.11},
eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ijfmts.20261203.11},
abstract = { Double diffusive natural convection driven by simultaneous temperature and concentration gradients is governed by the Rayleigh number Ra, which represents the balance between buoyancy and viscous forces. The Rayleigh number determines the transition from conduction-dominated to convection-dominated heat and mass transfer. While most existing studies rely on two-dimensional simplifications, this paper presents a three-dimensional numerical investigation of the effect of the Rayleigh number Ra on steady, laminar double-diffusive natural convection in a rectangular enclosure with an aspect ratio Ar of 0.5. The governing equations are solved using the finite volume method with the SIMPLE algorithm on a staggered grid. Parametric simulations are performed for Ra = 104, 5×104, 105, and 106, with fixed Prandtl number Pr = 7.0, Lewis number Le = 2.5, and buoyancy ratio N = 10. The results reveal that increasing the Ra from 104 to 105 leads to a clear transition from conduction-dominated to convection-dominated heat and mass transfer. At Ra = 104, profiles are smooth, and gradients are weak; at Ra = 105, sharp boundary layers and strong circulation appear. Concentration profiles become sharper and more localized with increasing Ra. At high Ra, solutal stratification occurs, and solute remains confined near the source, indicating enhanced solutal buoyancy effects. Temperature profiles evolve from nearly parallel isotherms (conduction) to wavy, distorted patterns with thermal plumes (convection). Vertical heat transfer increases significantly with Ra. Velocity fields become stronger and more organized as Ra increases. At Ra = 105, well-defined primary and secondary circulation cells produce intense upwelling and downwelling, with velocities an order of magnitude higher than at low Ra. The 3-dimensional nature of the flow reveals anisotropy: the primary circulation plane (z-y) shows the strongest response, but secondary planes (x-y, x-z) also exhibit significant changes with Ra. These results provide valuable benchmarks for engineering applications where controlling the strength of buoyancy-driven convection is crucial, such as in solar collectors, building ventilation, and drying systems. The finite volume method proves to be an effective tool for such 3-dimensional parametric studies.},
year = {2026}
}
TY - JOUR T1 - Effect of Rayleigh Number on Double-Diffusive Natural Convection Flow in a Rectangular Enclosure AU - Peninnah Ngina Musili AU - Mark Okongo AU - Alice Lunani Mulama Murwayi Y1 - 2026/09/04 PY - 2026 N1 - https://doi.org/10.11648/j.ijfmts.20261203.11 DO - 10.11648/j.ijfmts.20261203.11 T2 - International Journal of Fluid Mechanics & Thermal Sciences JF - International Journal of Fluid Mechanics & Thermal Sciences JO - International Journal of Fluid Mechanics & Thermal Sciences SP - 51 EP - 61 PB - Science Publishing Group SN - 2469-8113 UR - https://doi.org/10.11648/j.ijfmts.20261203.11 AB - Double diffusive natural convection driven by simultaneous temperature and concentration gradients is governed by the Rayleigh number Ra, which represents the balance between buoyancy and viscous forces. The Rayleigh number determines the transition from conduction-dominated to convection-dominated heat and mass transfer. While most existing studies rely on two-dimensional simplifications, this paper presents a three-dimensional numerical investigation of the effect of the Rayleigh number Ra on steady, laminar double-diffusive natural convection in a rectangular enclosure with an aspect ratio Ar of 0.5. The governing equations are solved using the finite volume method with the SIMPLE algorithm on a staggered grid. Parametric simulations are performed for Ra = 104, 5×104, 105, and 106, with fixed Prandtl number Pr = 7.0, Lewis number Le = 2.5, and buoyancy ratio N = 10. The results reveal that increasing the Ra from 104 to 105 leads to a clear transition from conduction-dominated to convection-dominated heat and mass transfer. At Ra = 104, profiles are smooth, and gradients are weak; at Ra = 105, sharp boundary layers and strong circulation appear. Concentration profiles become sharper and more localized with increasing Ra. At high Ra, solutal stratification occurs, and solute remains confined near the source, indicating enhanced solutal buoyancy effects. Temperature profiles evolve from nearly parallel isotherms (conduction) to wavy, distorted patterns with thermal plumes (convection). Vertical heat transfer increases significantly with Ra. Velocity fields become stronger and more organized as Ra increases. At Ra = 105, well-defined primary and secondary circulation cells produce intense upwelling and downwelling, with velocities an order of magnitude higher than at low Ra. The 3-dimensional nature of the flow reveals anisotropy: the primary circulation plane (z-y) shows the strongest response, but secondary planes (x-y, x-z) also exhibit significant changes with Ra. These results provide valuable benchmarks for engineering applications where controlling the strength of buoyancy-driven convection is crucial, such as in solar collectors, building ventilation, and drying systems. The finite volume method proves to be an effective tool for such 3-dimensional parametric studies. VL - 12 IS - 3 ER -