Experimental investigation of transition process from nucleate boiling to microbubble emission boiling under transient heating modes

AIChE Journal ◽  
2019 ◽  
Vol 65 (5) ◽  
pp. e16555 ◽  
Author(s):  
Jiguo Tang ◽  
Licheng Sun ◽  
Min Du ◽  
Hongtao Liu ◽  
Zhengyu Mo ◽  
...  
Author(s):  
Balkrushna A. Shah ◽  
Mohommed Naseem Quanungo ◽  
Mohommed Naseem Quanungo ◽  
Manish Sumera ◽  
Shahil Chaudhary ◽  
...  

Author(s):  
Guangyao Lu ◽  
Junsheng Ren ◽  
Guisheng Zhao ◽  
Wenyuan Xiang ◽  
Huaning Ai

Experiments are carried out to investigate the Onset of Nucleate Boiling (ONB) of refrigerant R-113 through vertical and inclined tube-bundle channels. Several methods are adopted to ascertain ONB in the experiments, and their differences are analyzed. The experiments show that the results of ONB estimation from the visualization experiment, ONB estimation from the wall temperature and that from the heat transfer coefficient are uniform. The influences of heat flux, mass flow rate, the geometric dimensions and inclination angle of the tube-bundle channels on the ONB height are explored in detail. On the foundation of the comparisons and analyses, an equation is put forward for calculating the ONB height in tube-bundle channels, which has a good accordance with the experimental results.


2020 ◽  
Vol 32 (4) ◽  
pp. 597-607
Author(s):  
Iman Nejati ◽  
Axel Sielaff ◽  
Benjamin Franz ◽  
Matthias Zimmermann ◽  
Philipp Hänichen ◽  
...  

2011 ◽  
Vol 24 (3) ◽  
pp. 139-146 ◽  
Author(s):  
Sebastian Fischer ◽  
Stefan Herbert ◽  
Axel Sielaff ◽  
Elena Maja Slomski ◽  
Peter Stephan ◽  
...  

Energies ◽  
2021 ◽  
Vol 14 (18) ◽  
pp. 5972
Author(s):  
Yu Xu ◽  
Zihao Yan ◽  
Ling Li

To protect the environment, a new low-GWP refrigerant R1234ze(E) was created to substitute R134a. However, its flow boiling performances have not received sufficient attention so far, which hinders its popularization to some extent. In view of this, an experimental investigation was carried out in a 1.88 mm horizontal circular minichannel. The saturation pressures were maintained at 0.6 and 0.7 MPa, accompanied by mass flux within 540–870 kg/m2 s and heat flux within 25–65 kW/m2. For nucleate boiling, a larger heat flux brings about a larger heat transfer coefficient (HTC), while for convective boiling, the mass flux and vapor quality appear to take the lead role. The threshold vapor quality of different heat transfer mechanisms is around 0.4. Additionally, larger saturation pressure results in large HTC. As for the frictional pressure drop (FPD), it is positively influenced by mass flux and vapor quality, while negatively affected by saturation pressure, and the influence of heat flux is negligible. Furthermore, with the measured data, several existing correlations are compared. The results indicate that the correlations of Saitoh et al. (2007) and Müller-Steinhagen and Heck (1986) perform best on flow boiling HTC and FPD with mean absolute deviations of 5.4% and 10.9%.


2000 ◽  
Author(s):  
M. S. Lakshminarasimhan ◽  
D. K. Hollingsworth ◽  
Larry C. Witte

Abstract Experiments were performed to investigate nucleate flow boiling and incipience in a flow channel, 1 mm high × 20 mm wide × 357 mm long, vertical, with one wall heated uniformly and others approximately adiabatic. Subcooled R-11 flowed upward through the channel; the mass flux varied from 60 to 4586 kg/(m2s). The inlet subcooling varied from 3.0 to 15.3 °C, and the inlet pressure ranged up to 0.20 MPa. Liquid crystal thermography was used to measure distributions of surface temperature from which the heat transfer coefficients on the heated surface were calculated. Observations of the boiling incipience superheat excursion and the hysteresis phenomenon are presented and discussed. In laminar flow, a boiling front was observed that clearly separated the region cooled by single-phase convection from the region experiencing nucleate boiling. A prediction for the wall temperature and heat flux at boiling incipience based on nucleation theory compared favorably with the data. An incipience turning angle was defined to describe the transition process from the point of incipience to fully developed nucleate boiling. Fully developed saturated nucleate boiling was correlated well by Kandlikar’s technique.


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