On heat transfer in tubes

被引：305

作者：

Gnielinski, V. ^{[1
]}

机构：

[1] KIT, Inst Therm Verfahrenstech, D-76131 Karlsruhe, Germany

来源：

INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER | 2013年 / 63卷

关键词：

Heat transfer; Tubes; Transition regime; PRESSURE-DROP; FLOW; LAMINAR; PIPE; MASS;

D O I：

10.1016/j.ijheatmasstransfer.2013.04.015

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Heat transfer coefficients for thermal design of heat exchangers are taken from equations in laminar or turbulent flow. The equations used to calculate the Nusselt numbers in tubes do not agree in the transition region between laminar and turbulent flow. There is a gap at Re = 2300. A linear interpolation between the Nusselt numbers at Re = 2300 and Re = 4000, each resulting from well-known equations is presented. The linear interpolation is based on the results of a paper published recently. New experimental findings about the Nusselt numbers in tubes at turbulent flow again confirm the respective equation. (C) 2013 Elsevier Ltd. All rights reserved.

引用

页码：134 / 140

页数：7

共 29 条

[1] Internal-flow Nusselt numbers for the low-Reynolds-number end of the laminar-to-turbulent transition regime [J].

Abraham, J. P. ;

Sparrow, E. M. ;

Minkowycz, W. J. .

INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2011, 54 (1-3) :584-588

[2] Heat transfer in all pipe flow regimes: laminar, transitional/intermittent, and turbulent [J].

Abraham, J. P. ;

Sparrow, E. M. ;

Tong, J. C. K. .

INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2009, 52 (3-4) :557-563

[3]

[Anonymous], THESIS U MINNESOTA

[4]

[Anonymous], T ASME J HEAT TRANSF

[5]

[Anonymous], 1966, THESIS U MINNESOTA

[6]

[Anonymous], 1976, THESIS U MINNESOTA

[7]

[Anonymous], 1990, HEAT TRANSF

[8]

[Anonymous], HEAT EXCHANGER DESIG

[9]

[Anonymous], VDI HEAT ATLAS

[10]

[Anonymous], VDI HEAT ATLAS

← 1 2 3 →