parameters
Module containing parameters used in the convective heat transfer modules.
Interface
#include <codecogs/engineering/thermodynamics/convection/parameters.h>
using namespace Engineering::Thermodynamics::Convection;
Overview
This module contains parameters which are used in studying various convective heat transfer phenomena.
References
Fluid Properties Calculator giving the values of the kinematic viscosity , thermal diffusivity
and thermal expansion coefficient
, for fluids at various temperatures: [url]http://www.mhtl.uwaterloo.ca/old/onlinetools/airprop/airprop.html[/url]
FUNCTION
Prandtl
The Prandtl number is a dimensionless parameter of a convecting system that gives the regime of convection. It has the formula
where is the kinematic viscosity and
is the thermal diffusivity of the fluid.
Example 1
The code below computes the Prandtl number in the case of Ethylene Glycol at 17 degrees Celsius.
#include <codecogs/engineering/heat_transfer/convection/parameters.h>
#include <stdio.h>
int main()
{
double mu = 2.1936E-5, a = 9.3834E-8;
printf("\nEthylene Glycol at 17 deg. Celsius\n\n");
printf("Pr = %.4lf\n\n",
Engineering::Heat_Transfer::Convection::Prandtl(mu, a));
return 0;
}Output
Ethylene Glycol at 17 deg. Celsius
Pr = 233.7745Parameters
Returns
Interactive Calculator
Computing…
Set a range above first to export a graph.
FUNCTION
Grashof
The Grashof number approximates the ratio of the buoyancy forces to the viscous forces in a fluid. It is given by the formula
where is the gravitational acceleration constant,
is the thermal expansion coefficient of the fluid,
is the temperature difference between the fluid and the wall,
is the characteristic length and
is the kinematic viscosity of the fluid.
Example 1
In the following example the Grashof number is calculated for air at 25 degrees Celsius going through a pipe at 15 degrees Celsius with internal diameter of 0.1 meters.
#include <codecogs/engineering/heat_transfer/convection/parameters.h>
#include <stdio.h>
int main()
{
double mu = 1.5571E-5, beta = 3.3540E-3, dT = 10, L = 0.1;
printf("\nAir at 25 deg. Celsius\n\n");
printf("Gr = %.4lf\n\n",
Engineering::Heat_Transfer::Convection::Grashof(mu, beta, dT, L));
return 0;
}Output
Air at 25 deg. Celsius
Gr = 1356596.6005Parameters
Returns
References
Dan Stefanescu, Mircea Marinescu - "Termotehnica"
Interactive Calculator
Computing…
Set a range above first to export a graph.
FUNCTION
Reynolds
Reynolds number, named after Osborne Reynolds who proposed it in 1883, is the ratio of inertial forces to viscous forces in a fluid. Besides other applications, it can be used to determine whether a flow inside a pipe is laminar, turbulent or in the so-called critical zone. The formula for this dimensionless measure is:
where is the characteristic length,
is the average velocity of the flow and
is the kinematic viscosity of the fluid.
It has been established that in the case of a fluid going through pipes, for Reynolds values less than 2000 the flow is laminar, for values greater than 4000 the flow is turbulent, while for numbers between 2000 and 4000 the flow becomes unpredictable. For this reason the domain from 2000 to 4000 is also called the "critical zone".
Example 1
In the following example the Reynolds number is computed for carbon dioxide at 75 degrees Celsius going through a pipe with internal diameter of 1.5 meters, having a velocity of 5 meters per second.
#include <codecogs/engineering/heat_transfer/convection/parameters.h>
#include <stdio.h>
int main()
{
double mu = 1.1203E-5, velocity = 5, length = 1.5,
Re = Engineering::Heat_Transfer::Convection::Reynolds(mu, velocity, length);
printf("Carbon Dioxide at 75 deg. Celsius\n\n");
printf("Re = %.4lf\n", Re);
if (Re < 2000) printf("Laminar flow.\n");
else if (Re > 4000) printf("Turbulent flow.\n");
else printf("Unpredictable flow (critical zone).\n");
printf("\n");
return 0;
}Output
Carbon Dioxide at 75 deg. Celsius
Re = 669463.5366
Turbulent flow.Parameters
Returns
References
The Engineering Division, Crane Co., "Flow of fluids through valves, fittings, and pipe", Chicago, 1957
Interactive Calculator
Computing…
Set a range above first to export a graph.