화학공학소재연구정보센터
International Journal of Heat and Mass Transfer, Vol.46, No.23, 4427-4438, 2003
Natural convection heat transfer of microemulsion phase-change-material slurry in rectangular cavities heated from below and cooled from above
An experimental study has been conducted in dealing with natural convection heat transfer characteristics of microemulsion slurry in rectangular enclosures. The microemulsion slurry used in the present experiment was composed of water, surfactant, and fine particles of phase-change-material (PCM). The PCM mass concentration of the microemulsion slurry was varied from a maximum 30 mass% to a diluted minimum 5 mass%, and the experiments have been done separately in three subdivided temperature ranges of the dispersed PCM particles in a solid phase, two phases (coexistence of solid and liquid) and a liquid phase. The results showed that the Nusselt number increased slightly with the PCM mass concentration for the slurry in solid phase. In the phase change temperature range, the Nusselt number increased with an increase in PCM mass concentration of the slurry at low Rayleigh numbers, while it decreased with increasing PCM mass concentration of the slurry at high Rayleigh numbers. There was not much difference in natural heat transfer characteristics of the PCM slurry with low PCM concentrations(<10 mass%), however, the difference was getting greater with increasing the PCM concentration, especially for the enclosure at a lower aspect ratio (width/height of the rectangular enclosure). The enclosure height was varied from 5.5 to 24.6 mm under a fixed width and depth of 120 mm. Hence, the experiments were performed for a wide range of modified Rayleigh number from 3x10(2) to 1.0x10(7). The correlation generalized for the PCM slurry in a single phase was derived in the form of Nu=0.22(1-C(1)C(m)e(-C 2 AR))Ra1/(3n+1), where C-1 and C-2 were the optimum fitting constants obtained by the least square method. While the PCM was in a phase changing region, the correlation could be expressed as Nu=0.22(1-C(1)C(m)e(-C 2 AR))Ra1/(3n+1) Ste(-0.25), where the Ste was the modified Stefan number. (C) 2003 Elsevier Ltd. All rights reserved.