## 1. Introduction

The pressure drop through common
fittings and valves found in fluid piping can be calculated thanks to
a friction coefficient K. This coefficient must be determined for
every fitting. In pre-project, common values are often sufficient.
Usual coefficients are given in the tables below.

## 2. Pressure drop calculation

The pressure drop through a fitting or a valve can be calculated
thanks to K.

**Equation 1 : pressure drop through a pipe singularity (valve,
fitting...)**

With

ΔP

_{s} = pressure drop through pipe singularity (valve,
fitting...) (Pa)

K = friction coefficient from tables below

ρ = fluid density (kg/m3)

u

_{m} = average fluid velocity (m/s)

K coefficient in a same pipe section can be added, the pressure drop
can then be expressed the following way.

**Equation 1 : pressure drop through
all pipe singularities of a pipe section (valve, fitting...)**

For compressible fluids, it is important to use the average velocity.
If the pressure drop is too important and density and velocity change
too much, the pipe section considered must be broken down in smaller
sections to keep a good calculation accuracy.

## 3. K coefficient for additional friction loss due to pipe and
fittings

The values below are only valid in TURBULENT FLOW

**Table 1 : K coefficient for
calculation of pressure drop through valves and fittings**

Note : Re>4000 : turbulent regime

**Source**

Mecanique et Rheologie des Fluides en
Genie Chimique, Midoux, Tec et Docs, 1993, pages 329-331

Perry's Chemical Engineers Handbook, Perry, McGraw Hill, 2008, page
6-18