2009
DOI: 10.1016/j.ijheatmasstransfer.2008.12.033
|View full text |Cite
|
Sign up to set email alerts
|

Flow boiling in horizontal flattened tubes: Part II – Flow boiling heat transfer results and model

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

1
9
0

Year Published

2014
2014
2023
2023

Publication Types

Select...
4
4

Relationship

0
8

Authors

Journals

citations
Cited by 55 publications
(13 citation statements)
references
References 25 publications
1
9
0
Order By: Relevance
“…Quibén et al [13,14] [15] experimentally studied saturated flow boiling and critical heat flux (CHF) in small flattened tubes with an equivalent diameter of 2.2 mm using R134a and R245fa at T sat =304.15 K. For mass fluxes higher than 200 kg/m 2 s, similar heat transfer coefficients were found for flattened and round tubes. The heat transfer correlation for round tubes could predict the data of flattened tubes well with a mean absolute error lower than 20%.…”
Section: Introductionmentioning
confidence: 92%
“…Quibén et al [13,14] [15] experimentally studied saturated flow boiling and critical heat flux (CHF) in small flattened tubes with an equivalent diameter of 2.2 mm using R134a and R245fa at T sat =304.15 K. For mass fluxes higher than 200 kg/m 2 s, similar heat transfer coefficients were found for flattened and round tubes. The heat transfer correlation for round tubes could predict the data of flattened tubes well with a mean absolute error lower than 20%.…”
Section: Introductionmentioning
confidence: 92%
“…They assessed the validity of existing two-phase heat transfer and pressure drop correlations for a range of local temperature and pressure measurements obtained for DSG in a PTC test rig (DISS facility in Almeria, Spain) by Lobón et al (2014) The facility consists of 13 parabolictrough collectors connected in series, with a total length of 700 m where the collector tubes have an inner diameter of 25 mm. The tested correlations for heat transfer were those of Gungor and Winterton (1986), Shah (1982), and Wojtan et al (2005b), whereas for the pressure drop the Lockhart and Martinelli (1949), Grönnerud (1972), and Quibén et al (2009) correlations were used. The temperature and pressure gradient profiles predicted by the correlations had an RMSE of <2.10% and <0.57%, respectively, when compared with the measurements.…”
Section: Considerations On Flow Boiling Under High Radiative Heat Fluxmentioning
confidence: 99%
“…To predict the heat transfer coefficient in flattened tubes, Kim et al [16] and Quibén et al [19] proposed new correlations based on their experimental data. The reported geometrical parameters and the used refrigerant in [13,16] are different from the ones covered in this study.…”
Section: Heat Transfer Coefficient Inside the Flattened Tubesmentioning
confidence: 99%
“…This specific tube profile yields lower hydraulic diameter according to its lower cross-sectional area to internal perimeter ratio. There are some studies in the literature that reported the privileges of flattened channels for the sake of heat transfer enhancement [16][17][18][19][20][21]. Wilson et al [17] carried out an experimental investigation on condensation heat transfer of R134a and R410a inside different flattened tubes.…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation