Abstract
Heat transfer of viscoelastic liquids in five flattened tubes with aspect ratios ranging from 1.4 to 5.7 were presented. Water was used as the heating medium; and solutions of polyacrylamide were used as the viscoelastic solutions. Heat transfer increase from flattening was 101% higher while secondary flow contributed a maximum increase of 65% for the 250 ppm solution and about 85% for the 500 ppm solutions at an aspect ratio of 1.6.
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Abbreviations
- a:
-
Major axis
- A:
-
Area
- b:
-
Minor axis
- c:
-
Straight section of the flattened tube cross-section = a−b
- cp :
-
Specific heat
- C:
-
Constant
- d:
-
Original tube diameter
- de :
-
Equivalent diameter
- dc :
-
Characteristic dimension
- F, G, H:
-
Shear rate functions
- F0, G0, H0 :
-
Shear rate functions coefficients
- Gz:
-
Greatz number
- Gze :
-
Graetz number using equivalent diameter
- hc :
-
Heat transfer coefficient, circular tube
- hf :
-
Heat transfer coefficient, flattened tube
- k:
-
Thermal conductivity
- K:
-
Material constant
- K’:
-
Constant in Graetz–Leveque equation
- L:
-
Length
- Nu:
-
Nusselt number
- Nue :
-
Nusselt number using equivalent diameter
- Nul :
-
Local Nusselt number
- p:
-
Aspect ratio
- P:
-
Pressure gradient
- q:
-
Heat flux
- qr :
-
Shear rate
- Q:
-
Volumetric flow rate
- Q1 :
-
Flow rate for central region, flattened tube
- Q2 :
-
Flow rate for semi-circular ends, flattened tube
- R:
-
Radius
- t:
-
Time
- T:
-
Temperature
- T1 :
-
Inlet temperature
- T2 :
-
Outlet temperature
- Tw :
-
Wall temperature
- ΔTA :
-
Temperature difference between the two streams at entry
- ΔTB :
-
Temperature difference between the two streams at exit
- ΔTLM :
-
Log mean temperature difference
- U:
-
Overall heat transfer coefficient
- v:
-
Velocity
- vmax :
-
Peak velocity
- vs :
-
Secondary flow velocity
- w:
-
Mass flow rate
- W:
-
Watt
- γ:
-
Strain
- λ1 :
-
Relaxation time
- λ2 :
-
Retardation time
- ρ:
-
Density
- τ:
-
Shear stress
- μw, μb :
-
Viscosity at wall, bulk viscosity
- Φ:
-
Geometric factor
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Ismail, Z., Karim, R. Determination of optimum aspect ratio for laminar flow heat transfer of dilute viscoelastic solutions in flattened tube heat exchangers. Heat Mass Transfer 48, 1319–1331 (2012). https://doi.org/10.1007/s00231-012-0981-2
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DOI: https://doi.org/10.1007/s00231-012-0981-2