化工学报 ›› 2011, Vol. 62 ›› Issue (S1): 118-122.
鲍伟,马虎根,白健美, 谢荣建
摘要:
在压力为0.5~1.7 MPa,质量流量为381~2291 kg·m-2·s-1,干度为0~1.0的工况范围内试验研究微尺度通道内低沸点混合工质R32/R134a的流动沸腾压降性能,同时对两相流流型进行可视化观察。微尺度通道内径为1.92 mm,0.86 mm和0.5 mm
Abstract:
An experiment was conducted to investigate the pressure drop characteristics during flow boiling in micro-channel with low boiling point〖JP〗 non-azeotropic refrigerant mixtures of R32/R134a.The experimental conditions are chosen as follows: inlet pressure is 0.5—1.7 MPa, mass flow is 381—2291 kg·m-2·s-1 and vapor quality is 0—1.0.At the same time, flow pattern in the exit of micro-channel were observed by a high speed camera.The diameter of three microtubes is 1.92 mm, 0.86 mm and 0.5 mm respectively.The experimental results reveal that two-phase pressure drop rises with increasing mass flow rate.At low heat flux, two-phase pressure drop increases with increasing heat flux.The trend was different that when heat flux q>150 kW·m-2, pressure drop kept unchanged with increasing heat flux.The diameter of micro-channel has significant effect on the two-phase pressure drop in micro-channel.There were some pressure drop fluctuations when flow pattern transited from slug to annular.Pressure drop increased slowly when flow pattern was slug and was stable when flow pattern was annular.