Hi all, firstly I apologize if I am asking this in the wrong place. I am thankful for any guidance I can receive on this.
I have been studying over pressure drops in pipes, and in some cases get wild answers in comparison to when I try to use a canned online-calculator. By hand I've checked units and they cancel where they need to. I may be getting the right answer, but it's the results from other sources that make me doubt my own.
Consider a 1" ID stainless steel drawn pipe (roughness epsilon = 0,0015), 2200 feet long, no elevation change.
The fluid being circulated is Cyclopentane, viscosity of 0.44cPs, at 27GPM. Density 746kg/m3.
27GPM is 0.00170343m3/s through a pipe cross-section of 0.001141m2.
I calculate a flow velocity of 1.494m/s.
Reynold's number is calculated to be 144,772.
Using Darcy Weisbach: p2-p1 = friction factor * (length/diameter) * (density*velocity^2/2) :: my result is appx 300psi pressure drop in the line.
I have found "other" Darcy Weisbach equations, but the one I've described seems the most appropriate. Using others can show numbers down to factors of 1-10psi and over 1,000psi. I want to practice these for this reason - I can't get to the bottom of why my results are unconfirmable.
I hope I've explained my problem well - I look forward and appreciate any help that comes from this.
Tucker
I have been studying over pressure drops in pipes, and in some cases get wild answers in comparison to when I try to use a canned online-calculator. By hand I've checked units and they cancel where they need to. I may be getting the right answer, but it's the results from other sources that make me doubt my own.
Consider a 1" ID stainless steel drawn pipe (roughness epsilon = 0,0015), 2200 feet long, no elevation change.
The fluid being circulated is Cyclopentane, viscosity of 0.44cPs, at 27GPM. Density 746kg/m3.
27GPM is 0.00170343m3/s through a pipe cross-section of 0.001141m2.
I calculate a flow velocity of 1.494m/s.
Reynold's number is calculated to be 144,772.
Using Darcy Weisbach: p2-p1 = friction factor * (length/diameter) * (density*velocity^2/2) :: my result is appx 300psi pressure drop in the line.
I have found "other" Darcy Weisbach equations, but the one I've described seems the most appropriate. Using others can show numbers down to factors of 1-10psi and over 1,000psi. I want to practice these for this reason - I can't get to the bottom of why my results are unconfirmable.
I hope I've explained my problem well - I look forward and appreciate any help that comes from this.
Tucker