Numerical investigation of thermal and fluid analysis of the effect of flight altitude and porous metal foam on the oil cooler of training airplane

Document Type : Original Article

Authors

1 Department of aerosapce.Aerospace faculty.shahid sattari aeronautical university.Tehran.Iran

2 Department of aerospace. Aerospace faculty. shahid Sattari aeronautical University. Tehran. Iran

3 school of mechanical engineering,iran university of science and technology.Tehran,Iran

10.22034/joae.2023.348694.1105

Abstract

using porous metal foams is one of the conventional methods to increase heat transfer in industrial systems, including heat exchangers. Porous media increase heat transfer and lead to an increase in pressure drop.. In this paper, the three-dimensional effects of flight altitude (1000m<H<5000m) and porous metal foam with Darcy number(0.1<Da<0.0001) in a training airplane oil cooler were investigated. The porosity coefficient was assumed to be 0.9 for all cases with porous foam.The Darcy-Brinkman-Fortheim equation was used to simulate a 20 W50 oil flow in a porous medium. The thermophysical properties of the oil including density, viscosity and thermal conductivity were extracted using laboratory data in terms of operating temperature. Hot oil with boundary condition enters the oil cooler. The boundary condition of the output oil is . The cooling wall is the boundary condition of non-slip and the heat transfer coefficient of air movement is proportional to the height. The governing equations are discrete based on the finite volume method using commercial computational fluid dynamics FLUENT. With increasing flight altitude, in pure oil mode, heat transfer, pressure drop and performance evaluation criteria increase by 0.65%, 0.45% and 0.49%, respectively. Porous metal foam with Darcy number having leads to increase of Nusselt number , increase of pressure drop and has the highest performance evaluation criterion PEC=31.75. Porous metal foam with Darcy number has the highest pressure drop and the highest heat transfer increase . According to the obtained results, Darcy's number is the most optimal performance evaluation parameter.

Keywords

Main Subjects


  • [1]  K. Vafai, S. J. Kim, ‘‘Forced Convection in a Channel Filled With a Porous Medium: An Exact Solution’’, ASME, vol. 111, no. 4, pp. 1103–1106, Nov. 1989.
  • [2]  K. Hooman,  A. A. Ranjbar-Kani, ‘‘Forced convection in a fluid-saturated porous-medium tube with isoflux wall, Int. Commun.’’ Heat Mass Transf., vol. 30, no. 7, pp. 1015–1026, Oct. 2003.
  • [3]  A. A. Ranjbar-Kani, K. Hooman, ‘‘Viscous Dissipation Effects onThermally Developing Forced Convectionin A Porous Medium Circular Duct with Isothermal Wall, Int. Commun.’’ Heat Mass Transf., vol. 31, no. 6, pp. 897–907, Aug. 2004.
  • [4]  P.-X. Jiang,  X.-C. Lu, ‘‘Numerical simulation of fluid flow and convection heat transfer in sintered porous plate channels’’, Int. J. Heat Mass Transf., vol. 49, no. 9, pp. 1685–1695, May 2006.
  • [5]  D. Poulikakos,  M. Kazmierczak, ‘‘Forced Convection in a Duct Partially Filled With a Porous Material’’, ASME, vol. 109, no. 3, pp. 653–662, Aug. 1987.
  • [6]  B. I. Pavel,  A. A. Mohamad, ‘‘An experimental and numerical study on heat transfer enhancement for gas heat exchangers fitted with porous media’’, Int. J. Heat Mass Transf., vol. 47, no. 23, pp. 4939–4952, Nov. 2004.
  • [7]  M. Mahdavi, M. Saffar-Avval, S. Tiari, Z. Mansoori, “Entropy generation and heat transfer numerical analysis in pipes partially filled with porous medium”, Int. J. Heat Mass Transf., vol. 79, pp. 496–506, Dec. 2014.
  • [8]        B. Wang et al., “Numerical configuration design and investigation of heat transfer enhancement in pipes filled with gradient porous materials,” Energy Convers. Manag., vol. 105, pp. 206–215, Nov. 2015.
  • [9]        B. Wang, Y. Hong, L. Wang, X. Fang, P. Wang, and Z. Xu, “Development and numerical investigation of novel gradient-porous heat sinks,” Energy Convers. Manag., vol. 106, pp. 1370–1378, Dec. 2015.
  • [10]      M. Dehghan, M. S. Valipour, and S. Saedodin, “Temperature-dependent conductivity in forced convection of heat exchangers filled with porous media: A perturbation solution,” Energy Convers. Manag., vol. 91, pp. 259–266, Feb. 2015.
  • [11]      A. Amiri and K. Vafai, “Analysis of dispersion effects and non-thermal equilibrium, non-Darcian, variable porosity incompressible flow through porous media,” Int. J. Heat Mass Transf., vol. 37, no. 6, pp. 939–954, Apr. 1994.
  • [12]      P.-X. Jiang and Z.-P. Ren, “Numerical investigation of forced convection heat transfer in porous media using a thermal non-equilibrium model,” Int. J. Heat Fluid Flow, vol. 22, no. 1, pp. 102–110, Feb. 2001.
  • [13]      A. Amiri, K. Vafai, and T. M. Kuzay, “EFFECTS OF BOUNDARY CONDITIONS ON NON-DARCIAN HEAT TRANSFER THROUGH POROUS MEDIA AND EXPERIMENTAL COMPARISONS,” Numer. Heat Transf. Part Appl., vol. 27, no. 6, pp. 651–664, Jun. 1995.
  • [14]  H. R. Talesh Bahrami, E. Aminian, and H.
    Saffari, “Energy Transfer Enhancement Inside an Annulus Using Gradient Porous Ribs and Nanofluids”, J. Energy Resour. Technol, vol. 142, no. 12, Dec. 2020, doi: 10.1115/1.4047312.
  • [15]  Y. Mahmoudi, N. Karimi, ‘‘Numerical investigation of heat transfer enhancement in a pipe partially filled with a porous material under local thermal non-equilibrium condition’’, Int. J. Heat Mass Transf., vol. 68, pp. 161–173, Jan. 2014.
  • [16]  Z. F. Huang, A. Nakayama, K. Yang, C. Yang, W. Liu, ‘‘Enhancing heat transfer in the core flow by using porous medium insert in a tube’’, Int. J. Heat Mass Transf., vol. 53, no. 5, pp. 1164–1174, Feb. 2010.
  • [17]E. Aminian, H. Moghadasi, H. Saffari, and A. M. Gheitaghy, “Investigation of Forced Convection Enhancement and Entropy Generation of Nanofluid Flow through a Corrugated Minichannel Filled with a Porous Media,” Entropy, vol. 22, no. 9, Art. no. 9, Sep. 2020, doi: 10.3390/e22091008.
  • [18]E. Aminian, H. Moghadasi, and H. Saffari, “Magnetic field effects on forced convection flow of a hybrid nanofluid in a cylinder filled with porous media: a numerical study,” J Therm Anal Calorim, vol. 141, no. 5, pp. 2019–2031, Sep. 2020, doi: 10.1007/s10973-020-09257-y.
  • [19]M. Siavashi, H. R. Talesh Bahrami, E. Aminian, and H. Saffari, “Numerical analysis on forced convection enhancement in an annulus using porous ribs and nanoparticle addition to base fluid,” J. Cent. South Univ., vol. 26, no. 5, pp. 1089–1098, 2019.
  • [20]      M. Siavashi, H. R. Talesh Bahrami, and E. Aminian, “Optimization of heat transfer enhancement and pumping power of a heat exchanger tube using nanofluid with gradient and multi-layered porous foams”, Appl. Therm. Eng., vol. 138, pp. 465–474, Jun. 2018, doi: 10.1016/j.applthermaleng.2018.04.066.
  •