TY - JOUR
T1 - Natural convection heat transfer in PCM suspensions in a square enclosure with bottom heating and top cooling
AU - Ho, C. J.
AU - Jang, C.
AU - Lai, Chi-ming
N1 - Funding Information:
Support from the Ministry of Sciences and Technologies (MOST) of ROC in Taiwan through Grant NSC89-2212-E006-160 is gratefully acknowledged.
Publisher Copyright:
© 2021 Elsevier Ltd
PY - 2021/10/1
Y1 - 2021/10/1
N2 - Research on the use of phase change material (PCM) suspensions to improve the natural convection efficiency of thermal systems is booming; however, there are few studies on the transient behavior of PCM suspensions. In this study, numerical simulations were used to investigate transient and steady-state natural convection in a square enclosure containing a PCM suspension. The implicit finite-difference method was adopted. The left and right walls of the enclosure were adiabatic sections, the bottom was an isothermal heating, and the top was an isothermal cooling. The following parameters were considered: PCM = n-octadecane (C18H38), enclosure aspect ratio = 1, buoyancy ratio for mass-to-heat transfer = 1, Rayleigh number (RaT) = 103–104, Stefan number (Ste) = 0.005–0.05, subcooling factor (Sb) = 0–10, and initial mass fraction (cm,i) = 0–20%. The results show that all the parameters (RaT, Ste, Sb, and cm,i) affect the flow pattern, and convection oscillations occur at Sb = 0.5–1. The heat transfer rate increases with RaT. Both cm,i and Sb affect the heat transfer rate but in a case-specific manner, and no well-defined correlations are observed.
AB - Research on the use of phase change material (PCM) suspensions to improve the natural convection efficiency of thermal systems is booming; however, there are few studies on the transient behavior of PCM suspensions. In this study, numerical simulations were used to investigate transient and steady-state natural convection in a square enclosure containing a PCM suspension. The implicit finite-difference method was adopted. The left and right walls of the enclosure were adiabatic sections, the bottom was an isothermal heating, and the top was an isothermal cooling. The following parameters were considered: PCM = n-octadecane (C18H38), enclosure aspect ratio = 1, buoyancy ratio for mass-to-heat transfer = 1, Rayleigh number (RaT) = 103–104, Stefan number (Ste) = 0.005–0.05, subcooling factor (Sb) = 0–10, and initial mass fraction (cm,i) = 0–20%. The results show that all the parameters (RaT, Ste, Sb, and cm,i) affect the flow pattern, and convection oscillations occur at Sb = 0.5–1. The heat transfer rate increases with RaT. Both cm,i and Sb affect the heat transfer rate but in a case-specific manner, and no well-defined correlations are observed.
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U2 - 10.1016/j.tsep.2021.101037
DO - 10.1016/j.tsep.2021.101037
M3 - Article
AN - SCOPUS:85122662659
SN - 2451-9049
VL - 25
JO - Thermal Science and Engineering Progress
JF - Thermal Science and Engineering Progress
M1 - 101037
ER -