nalasimbha
Mechanical
- Oct 5, 2009
- 15
Hi,
I have a question in calculating Nusselt and friction factor for flow in pipes. The flow in a pipe could be hydrodynamically developing, hydrodynamically fully developed, thermally developing and simultaneously developing and these four scenarios can occur for laminar and turbulent flow conditions.
After evaluating x* (thermal entrance length) and x+ (axial entrance length) for a given pipe of length L and dia D, I would need to select a suitable correlation and evaluate Nu and f. What I would like to know is that, if the length of the pipe is greater than x* and lets say the fluid has a high Pr, then will I use the correlations for fully developed for the entire length or should i used developing flow correlation till the point the flow is developing and then use the fully developed flow equations for the remaining length?
Thank you
I have a question in calculating Nusselt and friction factor for flow in pipes. The flow in a pipe could be hydrodynamically developing, hydrodynamically fully developed, thermally developing and simultaneously developing and these four scenarios can occur for laminar and turbulent flow conditions.
After evaluating x* (thermal entrance length) and x+ (axial entrance length) for a given pipe of length L and dia D, I would need to select a suitable correlation and evaluate Nu and f. What I would like to know is that, if the length of the pipe is greater than x* and lets say the fluid has a high Pr, then will I use the correlations for fully developed for the entire length or should i used developing flow correlation till the point the flow is developing and then use the fully developed flow equations for the remaining length?
Thank you