Flow Boiling Heat Transfer Of R134a: Effect Of Heat Flux And Dry-Out Characteristics
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F46747885%3A24210%2F23%3A00011438" target="_blank" >RIV/46747885:24210/23:00011438 - isvavai.cz</a>
Výsledek na webu
<a href="https://doi.org/10.11159/ffhmt23.161" target="_blank" >https://doi.org/10.11159/ffhmt23.161</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.11159/ffhmt23.161" target="_blank" >10.11159/ffhmt23.161</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
Flow Boiling Heat Transfer Of R134a: Effect Of Heat Flux And Dry-Out Characteristics
Popis výsledku v původním jazyce
This study presents an experimental analysis of flow boiling heat transfer of R134a refrigerant in a smooth horizontal stainless-steel tube with the goal of investigating the effect of heat flux on heat transfer coefficient and dry-out characteristics. The experiment was performed for heat fluxes ranging from 7.2 kW/m2 to 47.4 kW/m2, mass flux of 300 kg/m2s and saturation pressure of 460 kPa. At low heat flux, the heat transfer is predominantly controlled by convection boiling with a higher slope of heat transfer coefficient. As heat flux increases, nucleate boiling begins to predominate the heat transfer. The predominance of nucleate boiling is strongly experienced at low vapor quality when the higher slope in convective boiling begins to disappear as nucleate boiling dominates. Dry-out vapor quality incipience is not highly affected by heat flux. All the dry-out vapor quality incipience correlations investigated predicted well the vapor quality for which dry-out begins and end
Název v anglickém jazyce
Flow Boiling Heat Transfer Of R134a: Effect Of Heat Flux And Dry-Out Characteristics
Popis výsledku anglicky
This study presents an experimental analysis of flow boiling heat transfer of R134a refrigerant in a smooth horizontal stainless-steel tube with the goal of investigating the effect of heat flux on heat transfer coefficient and dry-out characteristics. The experiment was performed for heat fluxes ranging from 7.2 kW/m2 to 47.4 kW/m2, mass flux of 300 kg/m2s and saturation pressure of 460 kPa. At low heat flux, the heat transfer is predominantly controlled by convection boiling with a higher slope of heat transfer coefficient. As heat flux increases, nucleate boiling begins to predominate the heat transfer. The predominance of nucleate boiling is strongly experienced at low vapor quality when the higher slope in convective boiling begins to disappear as nucleate boiling dominates. Dry-out vapor quality incipience is not highly affected by heat flux. All the dry-out vapor quality incipience correlations investigated predicted well the vapor quality for which dry-out begins and end
Klasifikace
Druh
D - Stať ve sborníku
CEP obor
—
OECD FORD obor
20301 - Mechanical engineering
Návaznosti výsledku
Projekt
—
Návaznosti
S - Specificky vyzkum na vysokych skolach
Ostatní
Rok uplatnění
2023
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název statě ve sborníku
Journal of fluid flow, heat and mass transfer
ISBN
978-199080024-5
ISSN
23686111
e-ISSN
—
Počet stran výsledku
8
Strana od-do
—
Název nakladatele
—
Místo vydání
—
Místo konání akce
Ottawa
Datum konání akce
1. 1. 2023
Typ akce podle státní příslušnosti
WRD - Celosvětová akce
Kód UT WoS článku
—