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EngineeringHeat TransferConvection

Nusselt flat

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Returns the Nusselt number for a fluid going over a flat surface.

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Interface

#include <codecogs/engineering/heat_transfer/convection/nusselt_flat.h>

using namespace Engineering::Heat_Transfer::Convection;

double Nusselt_flat (double Pr, double Re)[inline]
Returns the Nusselt number for a fluid going over a flat surface.
ExcelReal cc_convectionNusselt_flat (Real Pr, Real Re)
This function is available as a Microsoft Excel add-in.

Function Documentation

Nusselt Flat Calculator
  
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doubleNusselt_flatdoublePr
doubleRe )[inline]
This module calculates the Nusselt number for a fluid which flows over a flat surface, the flow being either laminar or turbulent. The fluid must keep its state of matter during the heat transfer process.

The formulae for each case are given by

{\rm Nu} = 0.335 {\rm Re}^{0.5} {\rm Pr}^{0.5} \qquad \mbox{(laminar case)}

and

{\rm Nu} = 0.36 {\rm Re}^{0.8} {\rm Pr}^{0.75} \qquad \mbox{(turbulent case)}

where {\rm Re} is the Reynolds number and {\rm Pr} is the Prandtl number of the fluid. If the Reynolds number is less than 2000 the flow is considered laminar, while if it is greater than 4000 the flow is considered turbulent.

In the diagram below the relation between the velocity of the fluid and its corresponding Reynolds number is shown, as well as the unit heat flow in the laminar, unpredictable and turbulent cases.

1/flat-378.png
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Example 1:
The following code calculates the Nusselt number for Ethylene Glycol at 17 degrees Celsius, considering both the laminar and turbulent cases.
#include <codecogs/engineering/heat_transfer/convection/nusselt_flat.h>
#include <stdio.h>
 
int main()
{
  double Pr = 233.7745380139, Re1 = 1700, Re2 = 4200;
 
  printf("\nEthylene Glycol at 17 deg. Celsius\n\n");
 
  printf("Re = %.2lf (laminar flow)\n", Re1);
  printf("Nu = %.4lf\n\n", 
  Engineering::Heat_Transfer::Convection::Nusselt_flat(Pr, Re1));
 
  printf("Re = %.2lf (turbulent flow)\n", Re2);
  printf("Nu = %.4lf\n\n", 
  Engineering::Heat_Transfer::Convection::Nusselt_flat(Pr, Re2));
 
  return 0;
}
Output
Ethylene Glycol at 17 deg. Celsius
 
Re = 1700.00 (laminar flow)
Nu = 211.1873
 
Re = 4200.00 (turbulent flow)
Nu = 17041.1869
References:
Dan Stefanescu, Mircea Marinescu - "Termotehnica"
Parameters:
Prthe Prandtl number of the fluid
Rethe Reynolds number of the fluid
Returns:
the Nusselt number of the fluid with given parameters
Authors:
Grigore Bentea, Lucian Bentea (November 2006)
Source Code:

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