参考文献 :[1 ] 　KURUL N , PODOWSKI M Z. On the modeling ofmultidimensional effects in boiling channels [ C ] ∥27th National Heat Transfer Conference. Minneapo2lis , Minnesota , USA : ANS , 1991 : 28Ο31.[2] 　 BASU N , WARRIER G R , DHIR V K. Onset of nu2cleate boiling and active nucleation site density duringsubcooled flow boiling [J ]. ASME Journal of HeatTransfer , 2002 , 124(4) : 717Ο728.[3 ] 　TU Jiyuan. On numerical modeling of low pressuresubcooled boiling flows [J ]. International Journal ofHeat and Mass Transfer , 2002 , 45 (6) : 1197Ο1209.[4 ] 　KONCAR B , KLJ ENA K I. Modeling of local two2phase flow parameters in upward subcooled flow boil2ing at low pressure [J ]. International Journal of Heatand Mass Transfer , 2004 , 47(6/ 7) : 1499Ο1513.[5 ] 　ZEITOUN O , SHOU KRI M. Bubble behavior andmean diameter in subcooled flow boiling [J ]. ASMEJournal of Heat Transfer , 1996 , 118(1) : 110Ο116.[6 ] 　UNAL H C. Maximum bubble diameter , maximumbubble2growth time and bubble2growth rate duri