Abstract
This study purposes to examine the effects of latent heat transfer associated with the liquid films vaporization on the heat transfer in the natural convection flows driven by the simultaneous presence of combined buoyancy forces of thermal and mass diffusion. Results are especially presented for an air-water system under various conditions. The influence of channel length and system temperatures on the momentum, heat and mass transfer in the flow are investigated in great detail. The important role of transport of latent heat of vaporization under the situations of buoyancy-aiding and opposing flows is clearly demonstrated.
Zusammenfassung
Diese Studie beabsichtigt die Effekte der gemeinsamen Wärmeübertragung bei der Verdampfung eines Flüssigkeitsfilms und der Wärmeübertragung bei Strömung mit freier Konvektion, verursacht von kombinierten Auftriebskräften aus thermischer und Massendiffusion, zu untersuchen. Die Ergebnisse werden speziell für ein Luft-Wasser-System unter verschiedenen Bedingungen dargestellt. Der Einfluß der Kanallängen und der Systemtemperaturen auf den Impuls, die Wärme- und Stoffübertragung in der Strömung werden im Detail untersucht. Die wichtige Rolle des Wärmetransportes aus der Verdampfung unter Auftriebs- und Gegenstrombedingungen wird klar gezeigt.
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Abbreviations
- A :
-
[(C p1-C p2)/C p ](W r -W o )
- b :
-
half channel width
- C p :
-
specific heat
- D :
-
mass diffusivity
- D h :
-
hydraulic diameter (=4b)
- g :
-
gravitational acceleration
- Gr M :
-
Grashof number (mass transfer)
- Gr Mr :
-
reference Grashof number (mass transfer)
- Gr T :
-
Grashof number (heat transfer)
- Gr Tr :
-
reference Grashof number (heat transfer)
- h fg :
-
latent heat of vaporization
- h M :
-
local mass transfer coefficient
- k :
-
thermal conductivity
- l :
-
channel length
- M :
-
molecular weight
- Nu l :
-
local Nusselt number (latent heat)
- Nu s :
-
local Nusselt number (sensible heat)
- Nu x :
-
overall local Nusselt number
- p :
-
pressure of the moist air in the channel
- P:
-
dimensionless motion pressure (pressure defect)
- p m :
-
motion pressure (pressure defect),p−p o
- p o :
-
ambient pressure
- Pr :
-
Prandtl number, ν/α
- p w :
-
partial pressure of water vapor at interface
- Q :
-
total heat transfer rate
- Q o :
-
total heat transfer rate without liquid water film
- q′' x :
-
interfacial energy flux flowing into air stream
- Re :
-
Reynolds number at the inlet,u o D h /ν
- S :
-
parameter, Eq. (16)
- Sc :
-
Schmidt number, ν/D
- Sh x :
-
local Sherwood number
- T :
-
temperature
- u :
-
axial velocity
- u o ,U o :
-
average inlet velocity
- U :
-
dimensionless axial velocity
- ν :
-
transverse velocity
- V :
-
dimensionless transverse velocity
- w1 :
-
mass fraction of water vapor
- W :
-
dimensionless mass fraction of water vapor
- w r :
-
saturated mass fraction of water vapor atT w andp o
- x :
-
axial coordinate
- X :
-
dimensionless axial coordinate
- y :
-
transverse coordinate
- Y :
-
dimensionless transverse coordinate
- α :
-
thermal diffusivity
- θ :
-
dimensionless temperature, (T−T o )/(T w −T o )
- θ′ :
-
dimensionless temperature, (T−Tw)/(To−Tw)
- ν:
-
kinematic viscosity
- ϱ :
-
density
- φ :
-
relative humidity of air at ambient condition
- 1:
-
of water vapor
- 2:
-
of air
- w :
-
condition at interface
- 0:
-
at inlet condition
- r :
-
at reference condition
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Yan, W.M., Lin, T.F. & Chang, C.J. Combined heat and mass transfer in natural convection between vertical parallel plates. Wärme- und Stoffübertragung 23, 69–76 (1988). https://doi.org/10.1007/BF01637127
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DOI: https://doi.org/10.1007/BF01637127