Abstract
Absorber is an important component in absorption machines and its characteristics have significant effects on the overall efficiency of absorption machines. This article reports a model of simultaneous heat and mass transfer process in absorption of refrigerant vapor into a lithium bromide solution of water––cooled vertical plate absorber in the Reynolds number range of 5 < Re < 150. The boundary layer assumptions were used for the transport of mass, momentum and energy equations and the fully implicit finite difference method was employed to solve the governing equations in the film flow. Dependence of lithium bromide aqueous properties to the temperature and concentration and film thickness to vapor absorption was employed. This model can predict temperature, concentration and properties of aqueous profiles as well as the absorption heat and mass fluxes, heat and mass transfer coefficients, Nusslet and Sherwood number of absorber. An analysis for linear distribution of wall temperature condition carries out to investigation the reliability of the present numerical method through comparing with previous investigation.
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Abbreviations
- D :
-
Mass diffusivity (m²/s)
- g:
-
Gravitational acceleration (m/s²)
- h fg :
-
Heat of absorption (J/kg)
- h m :
-
Local mass transfer coefficient (m/s)
- \( \overline{h}_{\text{m}} \) :
-
Average mass transfer coefficient (m/s)
- h t :
-
Local heat transfer coefficient (W/m² K)
- \( \overline{h}_{\text{t}} \) :
-
Average heat transfer coefficient (W/m² K)
- k :
-
Thermal conductivity (W/m K)
- L :
-
Plate length (m)
- M abs :
-
Average mass flux (kg/m² s)
- m abs :
-
Absorption mass flux (kg/m² s)
- M :
-
Number of nodes in ε direction
- N :
-
Number of nodes in η direction
- Nu :
-
Nusselt number
- P :
-
Absorber pressure (Pa)
- Pr :
-
Prandtl number = υ/α
- q :
-
Heat flux (W/m²)
- Re :
-
Reynolds number
- Sc :
-
Schmidt number = υ/D
- Sh :
-
Sherwood number
- T :
-
Temperature (°C)
- x :
-
Axis to flow direction (m)
- y :
-
Axis perpendicular to flow direction (m)
- u :
-
Velocity in x direction (m/s)
- v :
-
Velocity in y direction (m/s)
- α :
-
Thermal diffusivity (m²/s)
- δ :
-
Film thickness (m)
- ε :
-
Non-dimensional x axis
- Г:
-
Film flow rate (kg/m.s)
- η :
-
Non-dimensional y axis
- μ :
-
Solution viscosity (kg/m s)
- υ :
-
Kinematic viscosity (m²/s)
- ρ :
-
Solution density (kg/m3)
- ω:
-
Salt (LiBr) mass concentration in the solution
- abs:
-
Absorption
- e:
-
Equilibrium
- f:
-
Film
- in:
-
Inlet
- surf:
-
Surface
- s:
-
Solution
- w:
-
Wall
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Karami, S., Farhanieh, B. A numerical study on the absorption of water vapor into a film of aqueous LiBr falling along a vertical plate. Heat Mass Transfer 46, 197–207 (2009). https://doi.org/10.1007/s00231-009-0557-y
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DOI: https://doi.org/10.1007/s00231-009-0557-y