Calculation
of Total Heat Load Required to Raise at Maintain Temperature
Heat Up
for Product: -
Q1 = (P1 x Vc1 X Cp1 X (Tm-Ta)) / 860*T
If we consider mass here then:-
Q1 = (m X Cp1 X (Tm-Ta))/860*T
Because
m = P1 x
Vc1
Heat Up
for Pipe:-
Q2 = (m X Cp2 X (Tm-Ta)) / 860*T
Q1 = Heat Up for Product in Pipe (W/hr)
P1 = Density of Product (kg/m3)
Vc1 = Volume of Product (m3)
Cp1 = Specific Heat of product (kcal/kg ⁰C)
Tm = Maintenance Temperature (◦C)
Ta = Minimum Ambient Temperature (◦C)
T = Time Period to Raise the Temperature (hr)
m = Mass of Product
Q2 = Heat Up for Pipe
Cp2 = Specific Heat of pipe (kcal/kg ⁰C)
Calculation
of volume: -
Vc1 =
3.14*r2*l
Where
Vc1 = Volume of Product (m3)
r = Radius of Pipe
l = Length of Pipe
Qi = K X N X (Ti – Ta)
Where
Qi = Heat Loss on Pipe Surface @ Initial Temperature(W/m)
Ti = Initial Temperature (◦C)
K = Thermal Conductivity (W/m ◦C)
N = Normalization Factor (Consider Value from Table V of Bs6351
Part 2)
Ta = Minimum Ambient Temperature (◦C)
Qf = K X
N X (Tm-Ta)
Where
Qf = Heat Loss on Pipe Surface @Final Temperature(W/m)
Tm = Maintenance Temperature (◦C)
K = Thermal Conductivity (W/m ◦C)
N = Normalization Factor (Consider Value from Table V of Bs6351
Part 2)
Ta = Minimum Ambient Temperature (◦C)
Q3 = (Qi
+ Qf) / 2
Where
Q3 = Average Heat Loss on Pipe Surface (W/m)
Qi = Heat Loss on Pipe Surface @ Initial Temperature (W/m)
Qf = Heat Loss on Pipe Surface @Final Temperature (W/m)
Total
Heat Load Required Raising at Maintain Temperature
Q = Q1 +
Q2 +Q3
Q = Total Heat Load required raising at Maintain Temperature
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