Michael Duncan
Mechanical
- Jul 31, 2024
- 1
Hi everyone, I'm working on a calculation regarding heat loss due to no insulation on a pipe and wanted to get some feedback on how accurate my logic may be and how to proceed.
My process is superheated steam. I used resistance conduction and convection formulas to get a BTU/hr loss rate of heat for uninsulated pipe. Knowing that the evaporation enthalpy is 777 BTU/lb for saturated steam, I can get a lb/hr value for steam loss. However, this is of course for saturated and not superheated so it won't be entirely accurate.
What's the best way to proceed forward to get an estimated energy loss of superheated steam for noninsulated pipe?
Thanks very much.
My process is superheated steam. I used resistance conduction and convection formulas to get a BTU/hr loss rate of heat for uninsulated pipe. Knowing that the evaporation enthalpy is 777 BTU/lb for saturated steam, I can get a lb/hr value for steam loss. However, this is of course for saturated and not superheated so it won't be entirely accurate.
What's the best way to proceed forward to get an estimated energy loss of superheated steam for noninsulated pipe?
Thanks very much.