2002
DOI: 10.1007/s00231-001-0283-6
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Determination of heat transfer coefficients on the surfaces of plastic tubes

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Cited by 6 publications
(8 citation statements)
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“…This leads to differences between the flow friction factor and energy losses during the flow through channel. Different friction factor leads also to different heat transfer coefficient [9]. Errors induced by the poor choice of CFD modelling method may have an influence on the simulations of the recuperator, where heat exchange occurs in a gaseous medium.…”
Section: Introductionmentioning
confidence: 99%
“…This leads to differences between the flow friction factor and energy losses during the flow through channel. Different friction factor leads also to different heat transfer coefficient [9]. Errors induced by the poor choice of CFD modelling method may have an influence on the simulations of the recuperator, where heat exchange occurs in a gaseous medium.…”
Section: Introductionmentioning
confidence: 99%
“…It is known from the literature that the friction factor, coefficients of heat and mass transfer take in the areas of laminar-turbulent transition have much higher values than the corresponding coefficients characteristic for laminar or turbulent flow (Gnieliński, 1999; Kandlikar et al , 2014; Rup et al , 2002). In Rup et al (2002), the determined turbulent exchange of momentum and heat during flows in the inlet area of plastic pipes was analysed. Due to the small diameters of pipes, the flows analysed were described by small values of the Reynolds number 5,000 < Re < 50,000.…”
Section: Introductionmentioning
confidence: 99%
“…The reasons for this inconsistency are most likely changes in the velocity profile and significant amplitude of disturbances in the inlet cross-section. The laminar-turbulent transition region is distinguished by higher values of friction factor and heat transfer coefficient compared to those in the region of fully developed laminar or turbulent flow [3][4][5][6]. Rup et al in [3] analyses the statistical steady turbulent exchange of momentum and heat in the range of small values of Reynolds number (5000 < Re < 50000) implemented in the inlet region of a plastic pipe.…”
Section: Introductionmentioning
confidence: 99%
“…The laminar-turbulent transition region is distinguished by higher values of friction factor and heat transfer coefficient compared to those in the region of fully developed laminar or turbulent flow [3][4][5][6]. Rup et al in [3] analyses the statistical steady turbulent exchange of momentum and heat in the range of small values of Reynolds number (5000 < Re < 50000) implemented in the inlet region of a plastic pipe. Research described in [3] includes changes in turbulence intensity in the inlet cross-section and changes in the turbulent Prandtl number, Pr t , in the flow area.…”
Section: Introductionmentioning
confidence: 99%
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