Major Head Loss
The major head loss considers the drop in pressure due to viscous effects, ie friction, this can either be as a result of the Darcy Weisbach equation or Poiseuille’s equation, depending on whether or not the flow is deemed to be laminar or turbulent.
Minor Head Loss
Minor head loss is due to any pressure drop caused by an elbow, tee, valve, etc. and is usually expressed as some coefficient (K) of the velocity head (M SHE).
Minor Head Loss Pipe Entrance
Minor Head Loss Pipe Exit
Minor Head Loss Conical Diffuser
Minor Head Loss 90 Degree Bend
all images and info from above are courtesy of http://sbainvent.com/fluid-mechanics/head-loss.php#.UNveGW_Za8A
The above info is courtesy of <http://docs.bentley.com/en/HMSewerCAD/SewerCAD_Help-14-117.html>
TYPE OF COMPONENT / FITTING | MINOR LOSS COEFFICIENT |
Tee, Flanged, Dividing Line Flow | 0.2 |
Tee, Threaded, Dividing Line Flow | 0.9 |
Tee, Flanged, Dividing Branched Flow | 1 |
Tee, Threaded , Dividing Branch Flow | 2 |
Union, Threaded | 0.08 |
Elbow, Flanged Regular 90 | 0.3 |
Elbow, Threaded Regular 90 | 1.5 |
Elbow, Threaded Regular 45 | 0.4 |
Elbow, Flanged Long Radius 90 | 0.2 |
Elbow, Threaded Long Radius 90 | 0.7 |
Elbow, Flanged Long Radius 45 | 0.2 |
Return Bend, Flanged 180 | 0.2 |
Return Bend, Threaded 180 | 1.5 |
Globe Valve, Fully Open | 10 |
Angle Valve, Fully Open | 2 |
Gate Valve, Fully Open | 0.15 |
Gate Valve, 1/4 Closed | 0.26 |
Gate Valve, 1/2 Closed | 2.1 |
Gate Valve, 3/4 Closed | 17 |
Swing Check Valve, Forward Flow | 2 |
Ball Valve, Fully Open | 0.05 |
Ball Valve, 1/3 Closed | 5.5 |
Ball Valve, 2/3 Closed | 200 |
Diaphragm Valve, Open | 2.3 |
Diaphragm Valve, Half Open | 4.3 |
Diaphragm Valve, 1/4 Open | 21 |
Water meter | 7 |
The above table is courtesy of http://www.engineeringtoolbox.com/minor-loss-coefficients-pipes-d_626.html
LOSS COEFFICIENTS FOR PIPE COMPONENTS
The above image is courtesy of http://faculty.olin.edu/~jtownsend/Transport%20Fall%202008/docs/Supplemental%20Reading%20-%20Pumps.pdf
HEAD LOSS DUE TO SUDDEN CONTRACTION / EXPANSION
this is simply (the difference between the upstream and downstream velocities) [squared] /2g, ie:
SIDE NOTE:
no copyright infringement is intended, this is for purely personal and educational purposes only, all information used is that of the original creater (referenced), I do not bare any responsibility towards the use of this information.
hallo, in your final equation I believe it should be V1^2 – V2^2 instead, not the square of the difference of the velocities as expressed. But that said, this is very useful! =)
I want to calculate head loss in the butterfly valve using a formula h=k×v^2/2g. And for this I need the value of valve loss coefficient k, can you help me with that?