Calculator start selection

download
desktop app

online
web app

web start
Java™ app

Read all about available deployments. In any way of utilizing calculator, Internet connection is not required, but nice to have for authentication at least.

Watch example #4

Available in download version

save/open multiple results
export to word and excel
print results
common and custom fluid properties
K factor for fittings, resistance coefficient
pipe surface roughness selection
pipe material selection
select between gauge and absolute pressure
compressible isothermal flow
dry air isothermal flow
gas offtake flow
natural gas flow

Download

Administrator role not needed to install calculator

When is this calculator applicable?

You can use pressure drop in pipe calculator for pressure drop and flow rate calculation for all Newtonian fluids (gases and liquids) with constant density (incompressible flow) in closed, round or rectangular duct.

If the flowing fluid is gas, pressure change due to friction, local resistances or height change has to be low (less than 5-10%) to be sure that this calculator is applicable and that it gives correct results. If the pressure change is higher than 10%, you should use the calculator for compressible gas flow.

If you select gas as flowing fluid, the calculator assumes that gas has perfect (ideal) gas properties, i.e., the ideal gas law is applied to calculate any of the unknown gas state values - pressure, temperature or density.

Pressure drop calculator is suitable for laminar and turbulent flow regime.

Also, when it is not applicable?

You can't use this calculator for compressible gas flow where the pressure of the gas is changing more than 5-10%. For that purpose, you can use one of available gas pressure drop calculators.

You can't use this calculator if the fluid is non-Newtonian, i.e., its viscosity is changing with the shear rate or due to some other changed condition.

Pressure drop calculator is not applicable if the flowing fluid contains solid particles or if the flowing fluid is the mixture of liquid and gas, i.e., multiphase flow.

If the flowing fluid is gas but not a perfect (ideal) gas, i.e., if it's pressure, temperature and density are not related according to ideal gas law, this calculator is not applicable, also.

If the viscosity of flowing fluid is changing due to flow temperature change, this calculator is not applicable as it takes viscosity as a constant value.

Need a helping hand?

If you need a quick calculation, but you are not still familiar how to use the calculator, you can order calculation service from the calculator developer.

Order calculation service

What has to be known to calculate pressure drop?

To calculate pressure drop, you have to know pipe properties - pipe length, internal pipe diameter and interior pipe surface roughness. For rectangular ducts, instead of diameter, channel width and height has to be known.

For pipeline that has local flow resistances like bends, tees, reducers, valves, and alike, you have to know minor resistance factor as a sum of all individual resistance.

Also, fluid viscosity (dynamic or kinematic) and density for liquids, or temperature and gas constant for gases are required.

In the end, the flow rate (volume or mass flow rate) has to be known as well.

What has to be known to calculate flow rate?

The most important thing to know when you want to calculate flow rate - pressure on the start AND the end of the pipe, has to be identified. It is not possible to calculate flow rate if only the pressure at one point is determined. If at the end of the pipe is open air, then end pressure is atmospheric pressure. If not, the pressure on the pipe end must be known to calculate the flow rate.

You have to know pipe and fluid properties also, to calculate flow rate in a pipeline.

How is the calculation performed?

Pressure drop and flow rate calculation use the Darcy-Weisbach equation for head loss due to friction in closed, round or rectangular duct.

For turbulent flow, where is Reynolds number Re > 4000, friction factor is calculated using on the Colebrook and White equation (1937).