Heat transfer and critical heat flux of subcooled water flow boiling in a HORIZONTAL circular tube

• Published in: Experimental thermal and fluid science Vol. 44; pp. 844 - 857
• Main Authors: Hata, K., Shirai, Y., Masuzaki, S.
• Format: Journal Article
• Language: English
• Published: Amsterdam Elsevier Inc 01.01.2013; Elsevier
• Subjects: Applied sciences; Austenitic stainless steels; Boiling; Correlation; Critical heat flux; Energy; Energy. Thermal use of fuels; Exact sciences and technology; Flow velocity; Heat transfer; Horizontal; HORIZONTAL circular test tube; Nucleate boiling heat transfer; Steady state; Subcooled water flow; Theoretical studies. Data and constants. Metering; Tubes; Turbulent heat transfer; Water flow; Turbulent heat transfer; Nucleate boiling heat transfer; Subcooled water flow; Critical heat flux; HORIZONTAL circular test tube; Flow boiling; Turbulent flow; Circular pipe; Critical heat flow; Experimental study; Subcooled boiling; Test facility; Nucleate boiling; Horizontal tube; Heat transfer
• ISSN: 0894-1777; 1879-2286
• DOI: 10.1016/j.expthermflusci.2012.10.001

The steady-state turbulent heat transfer (THT) due to exponentially increasing heat inputs with various exponential periods (Q=Q0exp(t/τ), τ=6.55–21.81s) were systematically measured with the flow velocities, u, of 4.15, 7.05, 10.07 and 13.50m/s by an experimental water loop flow. Measurements were made on a 6mm inner diameter, a 59.2mm effective length and a 0.4mm thickness of HORIZONTAL Platinum (Pt) circular test tube. The relation between the steady-state turbulent heat transfer and the flow velocity was clarified. The steady state nucleate boiling heat transfer (NBHT) and the steady state critical heat fluxes (CHFs) of the subcooled water flow boiling for HORIZONTAL SUS304 circular test tube were systematically measured with the flow velocities (u=3.93–13.86m/s), the outlet and inlet subcoolings (ΔTsub,out=60.40–130.30K and ΔTsub,in=81.30–154.20K), the inlet pressures (Pin=786.29–960.93kPa) and the increasing heat input (Q0exp(t/τ), τ=8.36s). The HORIZONTAL SUS304 test tube of inner diameter (d=6mm), heated length (L=59.4mm), effective length (Leff=48.4mm), L/d (=9.9), Leff/d (=8.06) and wall thickness (δ=0.5mm) with surface roughness (Ra=3.89μm) was used in this work. The NBHT and the steady state CHFs of the subcooled water flow boiling for the HORIZONTAL SUS304 circular test tube were clarified at the flow velocities, u, ranging from 3.93–13.86m/s. The steady-state THT data, the NBHT ones and the steady state CHF ones were compared with the values calculated by authors’ THT correlation, their NBHT ones and their transient CHF ones against outlet and inlet subcoolings based on the experimental data for the VERTICAL circular test tubes with the flow velocities, u, ranging from 4.0 to 42.4m/s. The influences of test tube orientation on the THT, the NBHT and the subcooled flow boiling CHF are investigated into details and the widely and precisely predictable correlations of the THT, the NBHT and the transient CHFs against outlet and inlet subcoolings in a HORIZONTAL circular test tube are derived based on the experimental data. The THT correlation, the NBHT ones and the transient CHF ones for the HORIZONTAL test tube can describe the THT data, the NBHT ones and the subcooled flow boiling CHF ones for the wide ranges of ΔTsub,out, ΔTsub,in and u obtained in this work within ±15% difference.