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Experimental study on heat transfer and hydrodynamics of a concentric double-pipe pulsed fluidized bed using microencapsulated phase change material and sand
被引:3
作者:
Assari, Mohammad Reza
[1
,3
]
Setareh, Milad
[1
]
Tabrizi, Hassan Basirat
[2
]
Salehianfard, Amin
[1
]
机构:
[1] Jundi Shapur Univ Technol, Mech Engn Dept, Dezful, Iran
[2] Amirkabir Univ Technol, Mech Engn Dept, Tehran, Iran
[3] Jundi Shapur Univ Technol, Mech Engn, POB 64615-334, Dezful, Iran
关键词:
Heat transfer coefficient;
Fluidized bed;
Pulsed flow;
Double pipe;
MPCM;
STABILIZED FLUIDIZATION;
FLOW;
PCM;
PULSATION;
BIOMASS;
PARTICLES;
DRYER;
D O I:
10.1016/j.powtec.2022.117832
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
This paper presents an experimental study on the heat transfer and hydrodynamic of a concentric double-pipe gas-solid pulsed fluidized bed filled in outer tube with microencapsulated phase change material and inner tube with sand. The effect of flow velocity, frequency and bed height are investigated on the heat transfer. Experiments are carried out at frequency in the range of 1 to 5Hz with the bed height of 15, 18.5and 22 cm and the ratio of air velocity to minimum fluidization velocity (U/Umf) of 1, 1.1, 1.2, 1.3, 1.4, 1.5. Results show that heat transfer enhances as the frequency, bed height and U/Umf increase. Besides, it is found that pulsed flow has higher heat transfer enhancement than continuous flow. For example, at U/Umf of 1.5, the heat transfer coefficient of the pulsed flow increases by 7.5% than that of the continuous flow at the bed height of 22 cm.
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页数:11
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