Abstract
The design of the absorber of absorption chillers is still subject to great uncertainty since the coupled processes of heat and mass transfer as well as the influence of systemic interactions on the absorption process are not fully understood. Unfortunately, only a few investigations on the transport phenomena in the absorber during operation in an absorption chiller are reported in the literature. Therefore, experimental investigations on the heat and mass transfer during falling film absorption of steam in aqueous LiBr-solution are carried out in an absorber installed in an absorption chiller in this work. An improvement of heat and mass transfer due to the increase in convective effects are observed as the Ref number increases. Furthermore, an improvement of the heat transfer in the absorber with increasing coolant temperature can be identified in the systemic context. This is explained by a corresponding reduction in the average viscosity of the solution in the absorber. A comparison with experimental data from literature obtained from so-called absorber-generator test rigs shows a good consistency. Thus, it has been shown that the findings obtained on these simplified experimental setups can be transferred to the absorber in an absorption chiller. However, a comparison with correlations from the literature reveals a strong deviation between experimental and calculated results. Hence, further research activities on the development of better correlations are required in future.
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Abbreviations
- A:
-
Area (m2)
- cp :
-
Specific heat capacity (kJ/kgK)
- Cpc :
-
Compactness factor (−)
- d:
-
Diameter of tube(m)
- D:
-
Diffusion coefficient (m2/s)
- g:
-
Gravitational acceleration (m/s2)
- j:
-
Number of parallel tube columns
- k:
-
Overall heat transfer coefficient (W/m2K)
- l:
-
Length of tube (m)
- L:
-
Inter tube distance in the bundle (m)
- \( \dot{\mathrm{m}} \) :
-
Mass flow rate(kg/s)
- p:
-
Pressure (bar)
- \( \dot{\mathrm{q}} \) :
-
Heat flux (W/m2)
- \( \dot{\mathrm{Q}} \) :
-
Rate of heat flow (W)
- R:
-
Radius (m)
- T:
-
Temperature (°C)
- x:
-
Mass related concentration (mass fraction kgLiBr/kgsolution) (%)
- Nu:
-
Nusselt number (−)
- Pr:
-
Prandtl number(−)
- Re:
-
Reynolds number (−)
- Ref :
-
Film Reynolds number (−)
- Sc:
-
Schmidt number (−)
- Sh:
-
Sherwood number (−)
- α:
-
Heat transfer coefficient (W/m2K)
- β:
-
Mass transfer coefficient (m/s)
- Γ:
-
Mass flow rate per tube length and side (kg/m·s)
- ε:
-
Roughness (m)
- η:
-
Dynamic viscosity (Pa s)
- λ:
-
Heat conduction (W/m)
- ν:
-
Kinetic viscosity (m2/s)
- ρ:
-
Density (kg/m3)
- ξ:
-
Friction factor
- 0:
-
Reference
- c:
-
Coolant
- coolant:
-
Cooling water
- cold:
-
Cold water
- crit:
-
Critical
- Cu:
-
Copper
- exp:
-
Experimental
- f:
-
Film
- h:
-
Horizontal
- H2O:
-
Water
- hot:
-
Hot water
- i:
-
Inner / inlet
- L:
-
Liquid
- LiBr:
-
Lithium bromide
- lm:
-
Logarithmic mean
- o:
-
Outer / outlet
- p:
-
Parallel
- pred:
-
Predicted
- poor:
-
Poor solution
- ref:
-
Refrigerant
- rich:
-
Rich solution
- s:
-
Solution
- st:
-
Steam
- sv:
-
Symmetric vertical
- svref:
-
Symmetric vertical reference
- eq:
-
Equilibrium
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Olbricht, M., Luke, A. Experimental investigation of the heat and mass transfer in a tube bundle absorber of an absorption chiller. Heat Mass Transfer 55, 81–93 (2019). https://doi.org/10.1007/s00231-018-2363-x
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DOI: https://doi.org/10.1007/s00231-018-2363-x