- #1
kosig
- 10
- 0
First, I am very confused as to the difference, if any, between head loss and pressure drop/loss. Can someone help me?
Also, I know that the Darcy-Weisbach equation for head loss due to friction is hf=fL/D*V2/2g
and you can plug that into get an equation for delta p that is
dp=fL/D*pV2/2
And this is dimensionally correct. My company says that for our applications all flow will be turbulent Re>4000 and the equation for the friction factor can be approximated to
f=(.0337*v.25)/(V.25*d.25) Which I am assuming is from the Colebrook equation.
So my problem is, when I plug this into the equation for delta p I get an equation which is not dimensionally correct. Why? And what does it mean?
Also, I know that the Darcy-Weisbach equation for head loss due to friction is hf=fL/D*V2/2g
and you can plug that into get an equation for delta p that is
dp=fL/D*pV2/2
And this is dimensionally correct. My company says that for our applications all flow will be turbulent Re>4000 and the equation for the friction factor can be approximated to
f=(.0337*v.25)/(V.25*d.25) Which I am assuming is from the Colebrook equation.
So my problem is, when I plug this into the equation for delta p I get an equation which is not dimensionally correct. Why? And what does it mean?