Pressure Change Due to Piping Length
Pressure Change Due to Piping Length
(OP)
DILEMMA
Because the length of piping and no other variables are changing, I am looking for a basic formula for determining the additional pressure change, as it relates to additional pipe length.
BACKGROUND
I am doing a basic, dual-phase vacuum process.
There are times when the process is only removing ambient air and minor levels of vapors. There are also times when the dual-phase is operating and water is also being removed.
I need to perform the same task, at an alternate location, on the site. The only variable that is changing is the necessary length of the 1" ID plastic tubing.
Because the length of piping and no other variables are changing, I am looking for a basic formula for determining the additional pressure change, as it relates to additional pipe length.
BACKGROUND
I am doing a basic, dual-phase vacuum process.
There are times when the process is only removing ambient air and minor levels of vapors. There are also times when the dual-phase is operating and water is also being removed.
I need to perform the same task, at an alternate location, on the site. The only variable that is changing is the necessary length of the 1" ID plastic tubing.
RE: Pressure Change Due to Piping Length
Patricia Lougheed
RE: Pressure Change Due to Piping Length
Is this publicly available or something that must be purchased?
RE: Pressure Change Due to Piping Length
I'll try to condense the basics here, but I need to warn you I may be leading you astray...I'm a nuclear engineer and picked up my fluid flow knowledge over the years. Also I've only worked with water systems so don't know how two-phase flow affects the pressure drop and what limitations you have on it.
Basically the head loss (h) (or pressure drop) is a function of the (1) roughness of the pipe (f) , (2) length of pipe (L), (3) diameter of pipe (D) and (4) velocity of the fluid through the pipe (v).
formula is h=f*L/D*(v^2)/2g for non-compressible fluids
For compressible fluids (such as air and vapor), the formulae change with the amount of pressure drop expected. If the pressure drop is fairly small (you're not adding a whole lot of piping), you can use the above formula. If it's large, then the formulas get complicated.
If you're looking for more than a rough answer, it might be worthwhile to hire someone who knows about this.
Patricia Lougheed