Objective
To determine the convective heat transfer coefficient and the rate of heat transfer by forced convection for flow of air inside a horizontal pipe.
Dp - 40mm
Do - 20mm
specimen dimension - 23x300 mm
Set voltage
Q(w)
10
T1(°C)
10
T2(°C)
10
T3(°C)
10
T4(°C)
10
T5(°C)
10
T6(°C)
27
T7(°C)
28
Temperature Gradient
Tm = Ts + Ta/2 K
Ts = T2+T3+T4+T5+T6/5 K
Ta = 303 K
Properties of air at Tm
Please enter a value rounded upto two decimal points
Mass Density of air
ρa = P⁄R.TR kg/m3
Patm - 101325 N/m2
Tatm - 303K
R - 287 J/kg
Upto four decimal places
ρa =
kg/m3
Vair at orifice,
Vo = Cd.(2.g.ha) 1/2 ⁄(1-(do/ dp )4)1/2 m/s
cd - 0.6
Vo =
m/s
Pressure drop
ha = ρm.hm⁄ρa m
ρm(mercury) -13600 kg/m3
manometer reading hm -25mm
ha =
m
Vair in the tube
Va = Vodo2 ⁄ds2 m/s
Va=
m/s
Reynolds number
Re = Va.ds⁄γ
γ - 1.696*10-5
Re =
Nusselt Number
Nu = 0.023(Re)0.8(Pr)n ⁄
n = 0.4 for heating of fluid
n = 0.3 for cooling of fluid
Pr=0.699
Nu =
Heat transfer coefficient
h = Nu.k⁄Ds W/m2k
k = 0.02756
h =
W/m2K
Heat transfer rate
Qc = h.A.⁄(Ts-Ta) W
A = π.Ds.L
Qc =
W
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