Heat transfer during film condensation inside plain tubes. Review of experimental research

被引:16
作者
Rifert, Volodymyr [1 ]
Sereda, Volodymyr [1 ]
Gorin, Vadim [1 ]
Barabash, Peter [1 ]
Solomakha, Andrii [1 ]
机构
[1] Natl Tech Univ, Ukraine BIgor Sikorsky Kyiv Polytech Inst, Politehnichna 6, UA-03056 Kiev, Ukraine
关键词
HORIZONTAL SMOOTH TUBES; FLOW CONDENSATION; TRANSFER COEFFICIENTS; PRESSURE-DROP; 2-PHASE CONDENSATION; GENERAL CORRELATION; MASS-TRANSFER; PART I; NUMERICAL CORRELATION; VAPOR CONDENSATION;
D O I
10.1007/s00231-019-02744-5
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper provides a comprehensive review of the published experimental researches on condensation heat transfer inside plain tubes. The existing methods of the research on heat transfer and hydrodynamics have been analyzed and their disadvantages are substantiated (shown). There are considered more than 40 empirical and semi-empirical methods and correlations for prediction of heat transfer coefficients in various heat exchangers, particularly in the evaporative systems of thermal desalinating plants, air conditioning systems, safety systems of reactors, heaters of power plants and condensers of cooling equipment. The given correlations are compared with the experimental data of various authors obtained in the case of condensation of diverse substances in different flow regimes. The correlations are evaluated with the experimental data of different authors for different fluids and flow conditions. According to the comparison performed, the correlations suggested by Thome and others (2003), Cavallini and others (2006), Shah (2015) and Rifert and others (2018) are recommended to be used for the most accurate prediction of heat transfer coefficients in case of condensation of various refrigerants, which in recent years are becoming widespread in power economy (fluid FC-72, methane, carbone dioxide, organic fluids R245fa, Novec (R) 649, HFE-7000, steam, etc.).
引用
收藏
页码:691 / 713
页数:23
相关论文
共 104 条
  • [1] Numerical investigation into the inclination effect on conjugate pool boiling and the condensation of steam in a passive heat removal system
    Abadi, S. M. A. Noori Rahim
    Meyer, J. P.
    [J]. INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2018, 122 : 1366 - 1382
  • [2] Ackers W.W., 1960, Chemical Engineering Progress Symposium, V56, P145
  • [3] Heat transfer coefficients and pressure drops during in-tube condensation of CO2/DME mixture refrigerant
    Afroz, Hasan M. M.
    Miyara, Akio
    Tsubaki, Koutaro
    [J]. INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2008, 31 (08): : 1458 - 1466
  • [4] Agra Ö, 2012, ISI BILIM TEK DERG, V32, P151
  • [5] Akers W.W., 1959, Chemical Engineering Progress Symposium Series, V55, P171
  • [6] Bae Soonhoon., 1969, REFRIGERANT FORCED C
  • [7] A generalized numerical correlation study for the determination of pressure drop during condensation and boiling of R134a inside smooth and corrugated tubes
    Balcilar, M.
    Aroonrat, K.
    Dalkilic, A. S.
    Wongwises, S.
    [J]. INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2013, 49 : 78 - 85
  • [8] A numerical correlation development study for the determination of Nusselt numbers during boiling and condensation of R134a inside smooth and corrugated tubes
    Balcilar, M.
    Aroonrat, K.
    Dalkilic, A. S.
    Wongwises, S.
    [J]. INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2013, 48 : 141 - 148
  • [9] Bivens D B., 1994, International Refrigeration Conference, P299
  • [10] Comparative investigations of the condensation of R134a and R404A refrigerants in pipe minichannels
    Bohdal, Tadeusz
    Charun, Henryk
    Sikora, Malgorzata
    [J]. INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2011, 54 (9-10) : 1963 - 1974