Flow boiling heat transfer and pressure drop of water in a plate heat exchanger with corrugated channels at low mass flux conditions

Eungchan Lee, Hoon Kang, Yong Chan Kim

Research output: Contribution to journalArticle

23 Citations (Scopus)

Abstract

The plate heat exchanger (PHX) has been widely used as a heat exchanger in fresh water generators (FWGs) at low mass flux conditions. In this study, the flow boiling heat transfer and pressure drop characteristics of water in a PHX for the FWG were measured by varying mass flux from 14.5 to 33.6 kg m -2 s-1, heat flux from 15.0 to 30.0 kW m-2, and mean vapor quality from 0.09 to 0.6 in the pressure range of 112-121 kPa. The flow boiling heat transfer of water in the PHX was in the convective boiling region. The flow boiling heat transfer coefficient decreased with increasing mean vapor quality and decreasing mass flux. However, the effect of the heat flux on the flow boiling heat transfer coefficient was almost negligible. In addition, the two-phase frictional pressure drop increased with increasing mean vapor quality and mass flux, but it remained nearly constant according to the heat flux. Two-phase heat transfer and pressure drop correlations for water in PHXs were developed based on the measured data. The proposed heat transfer and pressure drop correlations showed mean absolute deviations of 4.4% and 10.4%, respectively, compared with the measured data.

Original languageEnglish
Pages (from-to)37-45
Number of pages9
JournalInternational Journal of Heat and Mass Transfer
Volume77
DOIs
Publication statusPublished - 2014 Jan 1

Fingerprint

heat exchangers
pressure drop
boiling
Boiling liquids
Pressure drop
Heat exchangers
Mass transfer
heat transfer
Heat transfer
Water
Heat flux
heat flux
fresh water
water
Vapors
vapors
heat transfer coefficients
Heat transfer coefficients
generators
deviation

ASJC Scopus subject areas

  • Mechanical Engineering
  • Condensed Matter Physics
  • Fluid Flow and Transfer Processes

Cite this

@article{dd47ce44f33842de8d754de8e9a4e337,
title = "Flow boiling heat transfer and pressure drop of water in a plate heat exchanger with corrugated channels at low mass flux conditions",
abstract = "The plate heat exchanger (PHX) has been widely used as a heat exchanger in fresh water generators (FWGs) at low mass flux conditions. In this study, the flow boiling heat transfer and pressure drop characteristics of water in a PHX for the FWG were measured by varying mass flux from 14.5 to 33.6 kg m -2 s-1, heat flux from 15.0 to 30.0 kW m-2, and mean vapor quality from 0.09 to 0.6 in the pressure range of 112-121 kPa. The flow boiling heat transfer of water in the PHX was in the convective boiling region. The flow boiling heat transfer coefficient decreased with increasing mean vapor quality and decreasing mass flux. However, the effect of the heat flux on the flow boiling heat transfer coefficient was almost negligible. In addition, the two-phase frictional pressure drop increased with increasing mean vapor quality and mass flux, but it remained nearly constant according to the heat flux. Two-phase heat transfer and pressure drop correlations for water in PHXs were developed based on the measured data. The proposed heat transfer and pressure drop correlations showed mean absolute deviations of 4.4{\%} and 10.4{\%}, respectively, compared with the measured data.",
keywords = "Flow boiling heat transfer coefficient, Fresh water generator, Low mass flux, Plate heat exchanger, Two-phase frictional pressure drop",
author = "Eungchan Lee and Hoon Kang and Kim, {Yong Chan}",
year = "2014",
month = "1",
day = "1",
doi = "10.1016/j.ijheatmasstransfer.2014.05.019",
language = "English",
volume = "77",
pages = "37--45",
journal = "International Journal of Heat and Mass Transfer",
issn = "0017-9310",
publisher = "Elsevier Limited",

}

TY - JOUR

T1 - Flow boiling heat transfer and pressure drop of water in a plate heat exchanger with corrugated channels at low mass flux conditions

AU - Lee, Eungchan

AU - Kang, Hoon

AU - Kim, Yong Chan

PY - 2014/1/1

Y1 - 2014/1/1

N2 - The plate heat exchanger (PHX) has been widely used as a heat exchanger in fresh water generators (FWGs) at low mass flux conditions. In this study, the flow boiling heat transfer and pressure drop characteristics of water in a PHX for the FWG were measured by varying mass flux from 14.5 to 33.6 kg m -2 s-1, heat flux from 15.0 to 30.0 kW m-2, and mean vapor quality from 0.09 to 0.6 in the pressure range of 112-121 kPa. The flow boiling heat transfer of water in the PHX was in the convective boiling region. The flow boiling heat transfer coefficient decreased with increasing mean vapor quality and decreasing mass flux. However, the effect of the heat flux on the flow boiling heat transfer coefficient was almost negligible. In addition, the two-phase frictional pressure drop increased with increasing mean vapor quality and mass flux, but it remained nearly constant according to the heat flux. Two-phase heat transfer and pressure drop correlations for water in PHXs were developed based on the measured data. The proposed heat transfer and pressure drop correlations showed mean absolute deviations of 4.4% and 10.4%, respectively, compared with the measured data.

AB - The plate heat exchanger (PHX) has been widely used as a heat exchanger in fresh water generators (FWGs) at low mass flux conditions. In this study, the flow boiling heat transfer and pressure drop characteristics of water in a PHX for the FWG were measured by varying mass flux from 14.5 to 33.6 kg m -2 s-1, heat flux from 15.0 to 30.0 kW m-2, and mean vapor quality from 0.09 to 0.6 in the pressure range of 112-121 kPa. The flow boiling heat transfer of water in the PHX was in the convective boiling region. The flow boiling heat transfer coefficient decreased with increasing mean vapor quality and decreasing mass flux. However, the effect of the heat flux on the flow boiling heat transfer coefficient was almost negligible. In addition, the two-phase frictional pressure drop increased with increasing mean vapor quality and mass flux, but it remained nearly constant according to the heat flux. Two-phase heat transfer and pressure drop correlations for water in PHXs were developed based on the measured data. The proposed heat transfer and pressure drop correlations showed mean absolute deviations of 4.4% and 10.4%, respectively, compared with the measured data.

KW - Flow boiling heat transfer coefficient

KW - Fresh water generator

KW - Low mass flux

KW - Plate heat exchanger

KW - Two-phase frictional pressure drop

UR - http://www.scopus.com/inward/record.url?scp=84902164715&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=84902164715&partnerID=8YFLogxK

U2 - 10.1016/j.ijheatmasstransfer.2014.05.019

DO - 10.1016/j.ijheatmasstransfer.2014.05.019

M3 - Article

VL - 77

SP - 37

EP - 45

JO - International Journal of Heat and Mass Transfer

JF - International Journal of Heat and Mass Transfer

SN - 0017-9310

ER -