Impinging_Jets_ARNSquare
Procedure Impinging_Jets_ARNSquare(Fluid$, T, P, u, D, H, L : h_bar, Nusselt, Re) calculates the average heat transfer and Nusselt number for a square array of round nozzles with diameter D positioned perpendicular to a plate with its exit a distance H from the plate. The nozzle centers are positioned a distance L apart in both vertical and horizontal directions.
Inputs
Fluid$ is a string or string variable that can be any fluid in the EES data base. The fluid can be an ideal gas, a real fluid, a brine, or an incompressible fluid in the Solid-Liquid_Props fluids library.
T - the temperature of fluid exiting the jet [C], [K], [F], or [R]
P - pressure can be in [Pa], [kPa], [bar], [MPa], [atm] or [psia] (Note that for brines, this parameter provides the concentration in % instead of pressure.)
u - the velocity of the flow exiting the nozzle [m/s] or [ft/min]
D - the diameter of the nozzle in [m] or [ft]
H - the distance between the nozzle exit and the surface that the jet impinging on in [m] or [ft]
L - the distance between nozzle centers in the vertical and horizontal directions in [m] or [ft].
Outputs
h_bar - average heat transfer coefficient in [W/m^2-K] or [Btu/hr-ft^2-R]
Nusselt - average Nusselt number [-]
Re - Reynolds number [-]
Notes:
This procedure is responsible for determining the property data of the fluid specified and calculating the Reynold and Prandtl numbers. This procedure then passes dimensionless information to the non-dimensional procedure Impinging_Jets_ARNSquare_ND. The non-dimensional procedure returns the values for Nusselt njmber which is used to calculate the heat transfer coefficient.
Example
$UnitSystem SI C kPa J mass
Fluid$='air'
T=25 [C]
P=100 [kPa]
Vel=20 [m/s]
D=0.005 [m]
L=0.025 [m]
H=0.02 [m]
Call impinging_jet_arnsquare(Fluid$, T, P, Vel, D, H, L:h_bar, Nusselt, Re)
{Solution:
h_bar=177.7 [W/m^2-K]
Nusselt=34.82 [-]
Re=6320
}