Imperial College London

ProfessorChristosMarkides

Faculty of EngineeringDepartment of Chemical Engineering

Professor of Clean Energy Technologies
 
 
 
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Contact

 

+44 (0)20 7594 1601c.markides Website

 
 
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Location

 

404ACE ExtensionSouth Kensington Campus

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Summary

 

Publications

Citation

BibTex format

@article{Dirker:2021:10.1016/j.ijheatmasstransfer.2021.121017,
author = {Dirker, J and van, den Bergh WJ and Moran, HR and Markides, CN and Meyer, JP},
doi = {10.1016/j.ijheatmasstransfer.2021.121017},
journal = {International Journal of Heat and Mass Transfer},
pages = {1--12},
title = {Influence of inlet vapour quality perturbations on the transient response of flow-boiling heat transfer},
url = {http://dx.doi.org/10.1016/j.ijheatmasstransfer.2021.121017},
volume = {170},
year = {2021}
}

RIS format (EndNote, RefMan)

TY  - JOUR
AB - The effect a transient heat flux has on in-tube boiling has not been studied extensively for some refrigerants commonly proposed for use in concentrated solar power organic Rankine cycle systems. In this study, the effect of abrupt step changes (upwards and downwards) in the inlet vapour quality to a flow-boiling test section on the heat transfer coefficient was considered. Tests were conducted with R-245fa at a saturation temperature of 35°C in an 800 mm horizontal smooth tube with an inner diameter of 8.31 mm and a constant test section heat flux of 7.5 kW/m2. Initial inlet vapour qualities ranged between base values of 0.15 and 0.40 with mass fluxes of 200 and 300 kg/m2s. Baseline heat transfer coefficients at steady-state conditions were determined, followed by a series of transient-state response investigations. For these, sharp upward and downward step perturbations of the inlet vapour quality were considered. It was found that for a step size magnitude of 0.13 in the vapour quality, the actual heat transfer coefficient differed from the expected quasi-steady-state heat transfer coefficients during the transient. During the downward step, it was 8.7 to 11.7% higher than the expected heat transfer coefficient, while during the upward step, it was 9.3 to 26.0% lower for a mass flux of 200 kg/m2s, depending on the initial inlet vapour quality. For a mass flux of 300 kg/m2s, it was 7.2% and 16.7% higher and 13.8 to 17.8% lower for the downward and upward step respectively.
AU - Dirker,J
AU - van,den Bergh WJ
AU - Moran,HR
AU - Markides,CN
AU - Meyer,JP
DO - 10.1016/j.ijheatmasstransfer.2021.121017
EP - 12
PY - 2021///
SN - 0017-9310
SP - 1
TI - Influence of inlet vapour quality perturbations on the transient response of flow-boiling heat transfer
T2 - International Journal of Heat and Mass Transfer
UR - http://dx.doi.org/10.1016/j.ijheatmasstransfer.2021.121017
UR - https://www.sciencedirect.com/science/article/pii/S0017931021001204?via%3Dihub
UR - http://hdl.handle.net/10044/1/86871
VL - 170
ER -