Pipeline Pressure Loss

When a liquid or gas flows along a pipe, friction between the pipe wall and the liquid or gas causes a pressure or head loss. This pressure or head loss is an irreversible loss of the fluids potential energy. Calculating this loss is fundamental to the design of any pipeline system.

The relationship between pressure and head is defined by the following formula

                    P= ρgh           

Where

P          is pressure (N/m2)

ρ          is density (kg/m3),

g          is gravitational acceleration (9.81 m/s2)

h          is head (m).

When working with liquids it is usually better to calculate the friction loss as a head loss, as this makes the hydraulic calculations simpler. For gas flow a constant density cannot be defined so it is simpler to calculate the friction loss as a pressure.

The head loss in a length of pipe is given by the Darcy equation

Darcy equation

Where

f           is the friction factor

L          is the pipe length (m)

U         is the fluid mean velocity(m/s)

D         is the pipe diameter or the hydraulic diameter (m).

The hydraulic diameter is defined as

D= 4 x cross-sectional area / wetted perimeter.

For a standard circular pipe the hydraulic diameter is the same as the actual pipe diameter.

To determine the friction factor the Reynolds number needs to be calculated first.  The Reynolds number is defined as

Re=UD/ ν

Where ν is the kinematic viscosity

The Reynolds number is the ratio of inertia forces to viscous forces. For Reynolds numbers up to 2000 the flow is normally considered to be laminar, above 3000 the flow is turbulent, at Reynolds numbers between 2000 and 3000 the flow is in a critical zone, predicting the friction factor in the critical zone is difficult because it is not obvious if the flow should be treated as laminar or turbulent.

For laminar flow conditions the friction factor

laminar flow friction factor formula

For turbulent flow the friction factor

Fricton factor formula         (Note: use base 10 log)

where k is the pipe wall roughness value(m).

Table of Roughness Values , k (mm)

 

  mm
Smooth Pipes  
Drawn brass, copper, aluminium 0.0025
Glass, plastic, Perspex, fibreglass 0.0025
   
Steel Pipes  
New smooth pipes 0.025
Centrifugally applied enamels 0.025
Mortar lined, good finish 0.05
Mortar lined, average finish 0.1
Light rust 0.25
Heavy brush asphalts, enamels and tars 0.5
Heavy rust 1.0
Water mains with general tuberculations 1.2
   
Concrete pipes  
New, unusually smooth concrete with smooth joints 0.025
Steel forms, first class workmanship with smooth joints 0.025
New, or fairly new, smooth concrete and joints 0.1
Steel forms, average work workmanship, smooth joints 0.1
Wood floated or brushed surface in good conditions with good joints 0.25
Eroded by sharp materials in transit marks visible from wooden forms 0.5
Precast pipes, good surface finish, average joints 0.25
Segmentally lined conduits in good ground conditions with expanded wedge block linings 1.0
Segmentally lined conduits in other conditions 2.0
   
Other pipes  
Sheet metal ducts with smooth joints 0.0025
Galvanised metals, normal finish 0.15
Galvanised metals, smooth finish 0.025
Cast iron, uncoated and coated 0.15
Asbestos cement 0.025
Flexible straight rubber pipe with a smooth bore 0.025
Mature foul sewers 3.0

 

Fluid Densities and Kinematic Viscosities of some fluids and gases

 

Fluid Density (ρ) kg/m3 Kinematic viscosity (ν)  m2/s
Hydrogen 0.09 1.1 x 10-4
Air 1.2 1.5 x10-5
Crude oil 860 1.0 x 10-5
Jet  A1(-40oC) Kerosene 851 9.5 x 10-6
Jet  A1(0oC) Kerosene 823 2.5 x 10-6
Jet  A1(50oC) Kerosene 786 1.0 x 10-6
Water (0oC) 999.8 1.79 x 10-6
Water (4oC) 1000 1.52 x 10-6
Water (10oC) 999.7 1.31 x 10-6
Water (15oC) 999.1 1.14 x 10-6
Water (20oC) 998 1.0 x 10-6
Water (30oC) 996 0.80 x 10-6
Water (40oC) 992.1 0.66 x 10-6
Sea Water (0oC) 1030 1.73 x 10-6
Sea Water (15oC) 1027 1.46 x 10-6
Sea Water (30oC) 1022 0.85 x 10-6
Mercury 13600 1.1 x 10-7

The information and data provided on this site are for information only. Fluid Mechanics Ltd does not guarantee the validity of any information provided.   If you have a specific hydraulic problem then please contact us for technical advice.

  • Rahul Garg

    i want to solve a transient problem in pipelines which is connected in series. three pipes r connected with each other with reducing diameter. this problem is give in the book titled hydraulic transients by streeter and wiley. but i cant able to solve this problem. please help me in this matter.
    thanks