Sorry, the length was meant to be 585 feet long. The goal was to have the process gas end within a range of 140-250F. I figured the calculation would be more intensive than anticipated and I need to dig out my old heat transfer textbook.
Hi, I need to calculate the end temp of natural gas sent over 585' in 1/2" bare SS316 tubing. Temp is initially 660F and a constant flow of 40scfh. How do I go about finding the final temp of natural gas from the end of the tube to determine if I need insulation/heat trace?
I read some...