polykin.transport.heat¤
Nu_bank_tubes ¤
Nu_bank_tubes(
v: float,
rho: float,
mu: float,
Pr: float,
Prs: float,
aligned: bool,
D: float,
ST: float,
SL: float,
NL: int,
) -> float
Calculate the Nusselt number for cross flow over a bank of tubes.
For flow across a bank of aligned or staggered tubes, the average Nusselt number \(\overline{Nu}=\bar{h}D/k\) is estimated by the following expression:
where \(Re_{max}\) is the Reynolds number based on the maximum fluid velocity within the bank of tubes, and \(Pr\) is the Prandtl number. Additionally, \(C_2\), \(C\) and \(m\) are tabulated constants that depend on the tube bundle configuration.
References
- Žukauskas, Algirdas. "Heat transfer from tubes in crossflow", Advances in heat transfer. Vol. 8. Elsevier, 1972. 93-160.
- Incropera, Frank P., and David P. De Witt. "Fundamentals of heat and mass transfer", 4th edition, 1996, p. 376-381.
PARAMETER | DESCRIPTION |
---|---|
v
|
Nominal velocity outside the tube bank, \(v_{\infty}\) (m/s).
TYPE:
|
rho
|
Density (kg/m³).
TYPE:
|
mu
|
Viscosity (Pa·s).
TYPE:
|
Pr
|
Prandtl number.
TYPE:
|
Prs
|
Prandtl number at the surface of the tubes.
TYPE:
|
aligned
|
Aligned or staggered tubes.
TYPE:
|
D
|
Diameter (m).
TYPE:
|
ST
|
Transversal pitch (m).
TYPE:
|
SL
|
Longitudinal pitch (m).
TYPE:
|
NL
|
Number of rows of tubes.
TYPE:
|
RETURNS | DESCRIPTION |
---|---|
float
|
Average Nusselt number of the tube bank. |
See also
Nu_tube
: specific method for a single tube.
Source code in src/polykin/transport/heat.py
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