Module 5.02 - Heat Transfer Through a Composite Cylinder
Data
Thermal Conductivity of pipe, km = 28 Btu/(hr·ft·°F)
Thermal Conductivity of Insulation #1, k1 = 0.033 Btu/(hr·ft·°F)
Thickness of Insulation #1, Δr1 = 0.5 in
Bulk Temperature, Inside, Tib = 300 °F
Bulk Temperature, Outside, Tob = 70 °F
Film Coefficient, Inside, hi = 1500 Btu/(hr·ft2·°F)
Film Coefficient, Outside, ho = 2.23 Btu/(hr·ft2·°F)
Inner Film Resistance, Ri = 0.001 °F/(Btu·hr)
Pipe Material Resistance, Rm = 0.001 °F/(Btu·hr)
Insulation #1 Resistance, R1 = 1.694 °F/(Btu·hr)
Outside Film Resistance, Ro = 0.507 °F/(Btu·hr)
Total Resistance, Rc = 2.204 °F/(Btu·hr)
Inside Film Temperature Difference, ΔTib = 0.13 °F
Inner Pipe Surface Temperature, Ti = 299.87 °F
Pipe Temperature Difference, ΔTm = 0.10 °F
Outer Pipe Surface Temperature, Tm = 299.76 °F
Insulation #1 Temperature Difference, ΔT1 = 176.81 °F
Interface Temperature, T1 = 122.95 °F
Outer Bulk Temperature Difference, ΔTob = 52.95 °F
Outside Temperature, To = 122.95 °F
Heat Transfer Rate, q = 104.37 Btu/hr