A method for time and spatially resolved measurement of convective heat transfer coefficient (h) in complex flows

Abstract A miniaturized plane probe ( 5 × 5 × 1.1 mm 3 ) was developed to measure on-line local and unsteady convective heat transfer coefficients ( h ) in complex flows. The proposed method is in particular dedicated to assess h at the surface of porous media subjected to mass transport that interacts with the surrounding flow such as those that occur between a partially saturated porous medium and hot fluid phase (superheated steam, oil, etc.). The active h -probe consisted of a combination of a film heater sandwiched between two heat flux sensors, and h was obtained on each side from temperature and flux outputs of flux sensors in response to a periodic input of heating (maximum increase in probe surface temperature 2.5 ∘ C ). In controlled hydrodynamic conditions, it was found that 3 cycles of 1 Hz measurements ensured h relative errors ranged between −3% and −0.5% with 98% confidence for h values ranged between 200 and 500 W m - 2 K - 1 .

[1]  M. Kaviany Principles of heat transfer in porous media , 1991 .

[2]  Giovanni Maria Carlomagno,et al.  Wall heat transfer in static and rotating 180° turn channels by quantitative infrared thermography , 1998 .

[3]  Anne-Lucie Raoult-Wack,et al.  Characterization of heat and mass transfer during deep-fat frying and its effect on cassava chip quality , 2002 .

[4]  Patrick Perré,et al.  Advances in transport phenomena during convective drying with superheated steam and moist air , 1993 .

[5]  Akira Nakayama,et al.  A numerical study of interfacial convective heat transfer coefficient in two-energy equation model for convection in porous media , 2001 .

[6]  Chin Tsau Hsu,et al.  A closure model for transient heat conduction in porous media , 1999 .

[7]  S. Ramaswamy,et al.  HIGH INTENSITY DRYING , 1999 .

[8]  H. S. Ramaswamy,et al.  Analysis of critical control points in deviant thermal processes using artificial neural networks , 2003 .

[9]  Jorge Welti-Chanes,et al.  Transport Phenomena in Food Processing , 2002 .

[10]  Alain Cloutier,et al.  Experimental determination of the convective heat and mass transfer coefficients for wood drying , 2000, Wood Science and Technology.

[11]  Fernanda A. R. Oliveira,et al.  Analysis of the heat transfer coefficient during potato frying , 1999 .

[12]  G. Trystram,et al.  Continuous measurement of convective heat flux during deep-frying: validation and application to inverse modeling , 2003 .

[13]  A. Degiovanni,et al.  Simulation par volumes finis des transferts couplés en milieux poreux anisotropes : séchage du bois à basse et à haute température , 1990 .

[14]  O. Alifanov Inverse heat transfer problems , 1994 .

[15]  B. Farkas,et al.  A METHOD FOR DETERMINING THE CONVECTIVE HEAT TRANSFER COEFFICIENT DURING IMMERSION FRYING , 1999 .

[16]  A. Datta,et al.  Moisture, Oil and Energy Transport During Deep-Fat Frying of Food Materials , 1999 .

[17]  S. Whitaker,et al.  One- and Two-Equation Models for Transient Diffusion Processes in Two-Phase Systems , 1993 .

[18]  Ting Wang,et al.  A transient liquid crystal method using a 3-D inverse transient conduction scheme , 2002 .