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Flow & Transfer

Effect of boundary conditions on particle?fluid convection heat transfer

  • Li SUN Nan ZHANG Xinhua LIU Yiping FAN
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  • 1. State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China 2. State Key Laboratory of Heavy Oil, China University of Petroleum (Beijing), Beijing 102249, China

Received date: 2019-01-22

  Revised date: 2019-03-31

  Online published: 2019-12-22

Abstract

The effect of boundary conditions including the constant temperature and the uniform heat flux as well as the fluid?solid coupling boundary conditions on particle–fluid convection heat transfer were investigated by numerical simulation in this work. It was found that the time- and surface-averaged Nusselt numbers obtained by the fluid–solid coupling and the constant temperature boundary conditions matched well with the empirical formula, while the simulation result of the uniform heat flux boundary condition was larger than those of the other two boundary conditions. The distribution of the time- and surface-averaged local Nusselt number indicated that when the flow was in the steady symmetric regime, the Nusselt number decreased from the front stagnation point to the rear stagnation point. While the flow was in the unsteady vortex regime, the time- and surface-averaged local Nusselt number firstly decreased from its maximum at the front stagnation point to a minimum value near the separation point, and then gradually increased to the rear stagnation point.

Cite this article

Li SUN Nan ZHANG Xinhua LIU Yiping FAN . Effect of boundary conditions on particle?fluid convection heat transfer[J]. The Chinese Journal of Process Engineering, 2019 , 19(6) : 1075 -1084 . DOI: 10.12034/j.issn.1009-606X.219118

References

[1] 刘威威, 高豪, 秦云龙, 等. 基于 CFX 的多腔回转炉中催化剂颗粒加热的数值模拟 [J]. 过程工程学报, 2013, 13(6): 908-914.
[2] 米翠丽, 樊孝华, 魏刚, 等. 热解温度对生物质和煤成焦特性的影响 [J]. 生物质化学工程, 2014, 48(6): 36-42.
[3] 刘国庆, 刘清才, 姚璐, 等. 干熄焦除尘灰与低灰煤混合燃烧特性及动力学 [J]. 过程工程学报, 2015, 15(2): 272-277.
[4] 王维, 卢旭晨, 李佑楚. 循环流化床燃烧器的一维拟流体数值模拟 [J]. 过程工程学报, 2004, 4(5): 385-390.
[5] 侯凤云, 吕清刚, 那永洁, 等. 湿污泥颗粒的流化床干燥实验及模型 [J]. 过程工程学报, 2007, 7(4): 646-651.
[6] Ranz W E, Marshall W R, Jr. Evaporation from Drops, Parts I [J]. Chemical Engineering Progress, 1952, 48(3): 141-146.
[7] Ranz W E, Marshall W R, Jr. Evaporation from Drops, Parts II [J]. Chemical Engineering Progress, 1952, 48(4): 173-180.
[8] Whitaker S. Forced convection heat transfer correlations for flow in pipes, past flat plates, single cylinders, single spheres, and for flow in packed beds and tube bundles [J]. AIChE Journal, 1972, 18(2): 361-371.
[9] Imai T, Murayama T, Ono Y. The estimation of convective heat transfer coefficients between a spherical particle and fluid at lower Reynolds number [J]. ISIJ International, 1995, 35(12): 1438-1443.
[10] Proudman I, Pearson J R A. Expansions at small Reynolds numbers for the flow past a sphere and a circular cylinder [J]. Journal of Fluid Mechanics, 1957, 2(3): 237-262.
[11] Acrivos A, Taylor T D. Heat and mass transfer from single spheres in stokes flow [J]. Physics of Fluids, 1962, 5(5): 387-394.
[12] Rimmer P L. Heat transfer from a sphere in a stream of small Reynolds number [J]. Journal of Fluid Mechanics, 1968, 32(1): 1-7.
[13] Choudhury P N, Drake D G. Unsteady heat transfer from a sphere in a low Reynolds number flow [J]. Quarterly Journal of Mechanics and Applied Mathematics, 1971, 24(1): 23-36.
[14] Dennis S C R, Walker J D A, Hudson J D. Heat transfer from a sphere at low Reynolds number [J]. Journal of Fluid Mechanics, 1973, 60(2): 273-283.
[15] Clift,J.R. Grace M.E. Weber, Bubbles, Drops and Particles [M]. Academic Press, New York, 1978.
[16] Kendoush A A. Low Prandtl number heat transfer to fluids flowing past an isothermal spherical particle [J]. International Journal of Heat and Fluid Flow, 1995, 16(4): 291-297.
[17] Feng Z G, Michaelides E E. Unsteady heat transfer from a sphere at small Peclet numbers [J]. Journal of Fluid Engineering, 1996, 118(1): 96-102.
[18] Mansoorzadeh S, Pain C C, Oliveira C R E D, et al. Finite element simulations of incompressible flow past a heated/cooled sphere [J]. International Journal for Numerical Methods in Fluids, 1998, 28(6): 903-915.
[19] Feng Z G, Michaelides E E. A numerical study on the transient heat transfer from a sphere at high Reynolds and Peclet numbers [J]. International Journal of Heat and Mass Transfer, 2000, 43(2): 219-229.
[20] Bagchi P, Ha M Y, Balachandar S. Direct numerical simulation of flow and heat transfer from a sphere in a uniform cross-flow [J]. Journal of Fluids Engineering, 2001, 123(2): 347-358.
[21] Balachandar S, Ha M Y. Unsteady heat transfer from a sphere in a uniform cross-flow [J]. Physics of Fluids, 2001, 13(12): 3714-3728.
[22] Alassar R S, Badr H M. Heat convection from a sphere placed in a fluctuating free stream [J]. AIChE Journal, 2007, 53(7): 1670-1677.
[23] Koizumi H, Umemura Y, Hadno S, et al. Heat transfer performance and the transition to chaos of mixed convection around an isothermally heated sphere placed in a uniform, downwardly directed flow [J]. International Journal of Heat and Mass Transfer, 2010, 53(13-14): 2602-2614.
[24] Krishnan S, Kaman A. Effect of blockage ratio on drag and heat transfer from a centrally located sphere in pipe flow [J]. Engineering Applications of Computational Fluid Mechanics, 2010, 4(3): 396-414.
[25] Song D, Gupta R K, Chhabra R P. Effect of blockage on heat transfer from a sphere in power-law fluids [J]. Industrial and Engineering Chemistry Research, 2010, 49(49): 3849-3861.
[26] Song D, Gupta R K, Chhabra R P. Heat transfer to a sphere in tube flow of power-law liquids [J]. International Journal of Heat and Mass Transfer, 2012, 55(7-8): 2110-2121.
[27] Richter A, Nikrityuk P A. Drag forces and heat transfer coefficients for spherical, cuboidal and ellipsoidal particles in cross flow at sub-critical Reynolds numbers [J]. International Journal of Heat and Mass Transfer, 2012, 55(4): 1343-1354.
[28] Gupta A K, Mishra G, Nirmalkar N, et al. Effect of confinement on heat transfer in aqueous nanofluids from a heated sphere [J]. Powder Technology, 2018, 325(1): 576-596.
[29] Hema Sundar Raju B, Nath D, Pati S. Effect of Prandtl number on thermo-fluidic transport characteristics for mixed convection past a sphere [J]. International Communications in Heat and Mass Transfer, 2018, 98(1): 191-199.
[30] Dhole S D, Chhabra R P, Eswaran V. A numerical study on the forced convection heat transfer from an isothermal and isoflux sphere in the steady symmetric flow regime [J]. International Journal of Heat and Mass Transfer, 2006, 49(5-6): 984-994.
[31] Imai T, Mrrayama T, Ono Y. The effect of structure of packed beds on the convective heat transfer coefficient between particle and liquid [J]. ISIJ International, 1994, 34(10): 777-783.
[32] 张楠. 基于EMMS的介尺度传质模型及其在循环流化床锅炉燃烧模拟中的应用.[D]. 2010.
[33] Wu M H, Wen C Y, Yen R H, et al. Experimental and numerical study of the separation angle for flow around a circular cylinder at low Reynolds number [J]. Journal of Fluid Mechanics, 2004, 515(1): 233-260.
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