1[1]Hausbrand E. Condensing and Cooling Apparatus [M]. New York Van Nostrand, 1933.
2[2]Klipstein DH. Heat Transfer to a Vaporising Drop [M]. Cambridge D Sc Thesis MIT, 1963.
3[3]Sideman S and Taitel Y. Direct-Contact Heat Transfer with Change of Phase: Evaporation of Drops in an Immsicible Liquid Medium [A]. Int J of Heat Mass Transfer, 1964 : 1273- 1289.
4[4]Sideman S and Hirsch G. Direct Contact Heat Transfer with Change of Phase[A]. Ⅲ Analysis of the Transfer Mechanism of Drops Evaporating in Immisible Liquid Media[M]. Isreal J Technol, 1964:234 -241.
5[5]Sideman S and Isenberg J. Direct Contact Heat Transfer with Change of Phase: Bubble Growth in ThreePhase Systems[J]. Desalination, 1967,2: 207-214.
6[6]Prakash CB and Pinder KL. Direct Contact Heat Transfer Between Two Immisible Liquids During Vaporization, Part Ⅰ: Measurement of Heat Transfer Coefficient[J]. Can J Chem Engng, 1967, 45: 210-214.
7[7]Simpson HC, Beggs GC and Nazir. Evaporation of Butane Drops in Brine[J]. Desalination, 1974, 15:11 -23.
8[8]Selecki A and Gradon L. Equation of Motion of an Expanding Vapour Drop in an Immiscible Liquid Medium [J]. Int J Heat Mass Transfer, 1976,19 : 925- 929.
9[9]Gradon L and Selecki A. Evaporation of a Liquid Drop Immersed in Another Immiscible Liquid. The Case of σc>σd [J]. Int J Heat Mass Transfer, 1977,20: 459-466.
10[10]Tochitani Y, Mori YH and Komotori K. Vaporization of Single Liquid Drops in an Immiscible Liquid,Part Ⅰ: Forms and Motions of Vaporizing Drops[J].Warme-und Stoffuber tragung, 1977,10: 51-59.
