Heat transfer by forced convection

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.

apparatus

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 = PR.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.hmρa 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.dsγ

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.kDs W/m2k

k = 0.02756

h =

W/m2K

Heat transfer rate
Qc = h.A.(Ts-Ta) W

A = π.Ds.L

Qc =

W