Heat transfer and frictional pressure drop during condensation in plate heat exchangers

Heat transfer and frictional pressure drop during condensation in plate heat exchangers: Assessment of correlations and a new method

Toa, X. (TU Delft Engineering Thermodynamics)
Infante Ferreira, C.A. (TU Delft Engineering Thermodynamics)

2019

The corrugation channels of plate heat exchangers enhance the heat transfer and complicate the prediction of heat transfer coefficients and frictional pressure drop. This paper reviews the heat transfer and frictional pressure drop correlations for condensation in plate heat exchangers, and classifies the correlations into basic forms. An experimental database is developed including the data of HFCs, hydrocarbons, HFOs and CO ₂ . The mass fluxes are in the range of 2–150 kg·m ⁻² ·s ⁻¹ . The chevron angles and hydraulic diameters are distributed in 25.7°–70° and 3.23–8.08 mm. The saturated temperatures are −34.4 to 72.1 °C, while the reduced pressures are from 0.03 to 0.49. Eight heat transfer correlations are assessed with the database. The correlation of Longo et al. [48] predicts the experimental data best, while the correlation of Kuo et al. [16] shows the second best performance. Six frictional pressure drop correlations are compared with the database. The prediction of frictional pressure drop is relatively poor, and a new correlation is developed using multi-variable regression analysis with non-dimensional numbers. This new correlation predicts 87.5% of the experimental data within ±50%.

Assessment
Condensation heat transfer
Multi-variable regression analysis
Plate heat exchangers
Two-phase frictional pressure drop

http://resolver.tudelft.nl/uuid:12f80a97-3397-4ab0-942d-46ba51f8062f

https://doi.org/10.1016/j.ijheatmasstransfer.2019.01.132

0017-9310

International Journal of Heat and Mass Transfer, 135, 996-1012

Institutional Repository

review

© 2019 X. Toa, C.A. Infante Ferreira