Abstract
This paper presents experimental results of the heat and mass transfer characteristics of a water–LiBr horizontal tube absorber made of small diameter tubes. The experimental set up includes a tube absorber, a generator, solution distribution system and cooling water system. Three different tube diameters of 15.88, 12.70 and 9.52 mm have been installed inside the absorber to investigate the effect of the tube diameter on the absorber performance. The experimental results show that the heat and mass transfer performance of the absorber increases as the tube diameter decreases. A comparison of the heat and mass transfer coefficients of the present study agree reasonable well with that of the previous studies.
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Abbreviations
- A :
-
heat transfer area (m2)
- C :
-
LiBr concentration (wt%)
- c p :
-
specific heat at constant pressure (J/kg K)
- d :
-
tube diameter (m)
- h :
-
heat transfer coefficient (W/m2 K)
- h mass :
-
mass transfer coefficient (m/s)
- k :
-
thermal conductivity (W/m K)
- L :
-
tube length (m)
- M :
-
mass flow rate (kg/s)
- Nu :
-
Nusselt number
- n :
-
number of tube
- OD:
-
outer diameter (m)
- Pr :
-
Prandtl number
- Q :
-
heat transfer rate (W)
- Re :
-
Reynolds number
- T :
-
temperature (K)
- U :
-
overall heat transfer coefficient (W/m−2 K)
- u :
-
velocity (m/s)
- μ:
-
dynamic viscosity (kg/m s)
- ν:
-
kinematic viscosity (m2/s)
- ρ:
-
density (kg/m3)
- Γ:
-
liquid mass flow rate per unit width (kg/m s)
- c:
-
cooling water
- i, in:
-
inside
- in:
-
Inlet
- lm:
-
logarithmic mean temperature or concentration difference
- o, out:
-
outside
- out:
-
outlet
- s:
-
solution
- v:
-
vapor
References
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Yoon, JI., Phan, T.T., Moon, CG. et al. Heat and mass transfer characteristics of a horizontal tube falling film absorber with small diameter tubes. Heat Mass Transfer 44, 437–444 (2008). https://doi.org/10.1007/s00231-007-0261-8
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DOI: https://doi.org/10.1007/s00231-007-0261-8