Pump Performance Curve Explained | Master the Pump Curve for Optimal Results | Pump Curve

Centrifugal Pump Performance Curve Explained | Master the Pump Curve for Optimal Results | Core Engineering
In this video we are going to discuss about the ;
Mastering Centrifugal pump curves
Mastering centrifugal pump performance
The secrets of pump performance curves
Pump performance curve explained
Master the pump curve for optimal results
Pump performance curve explained
Centrifugal pump performance
Pump performance curve
centrifugal pump efficiency curve
Pump characteristics
Pump performance analysis
Pump selection
Centrifugal Pump Performance curve explained
Pump performance evaluation
Head vs Flow rate Pump curve
Efficiency vs flow rate pump curve
NPSH vs flow rate pump curve
Power vs Flow rate pump curve
how to read pump performance curve?
What is pump curve?
how is pump curve obtained?
The characteristics curve of a centrifugal pump
How to read a pump curve: complete curve
Reading a centrifugal pump
Understanding centrifugal pump curves
Centrifugal Pump Series:
• Centrifugal Pump Series
Industrial Pump Videos:
• Industrial Pump Videos
Process Engineering Series Videos:
• Process Engineering
Industrial Engineering Series:
• Industrial Engineering
Unit Conversion Series:
• Unit Conversion Series
Instrumentation Engineering Series:
• Instrumentation Engine...
Engineering Shorts Series:
• Engineering Shorts
#CoreEngineering #engineering #refinery #powerplant #pumpcurve #hydraulicsystems #mechanicalengineering #pumpknowledge #centrifugalpump #fluidmechanics
About the Channel :
Core Engineering is a TH-cam Channel for those Engineering Students as well as Engineers i.e. Chemical Engineer, Process Engineer, Instrumentation Engineer, Mechanical Engineer, Electrical Engineer, Electronics Engineer, Civil Engineer, etc. who wants to learn about the Engineering concepts from the scratch, wants to know the Technical How of each concept and those engineers who are already working in a Industry.
We will upload the videos related to Industrial concepts i.e. Pump, Centrifugal pump, Reciprocating pump, Compressor, Centrifugal compressor, Heat exchangers, Valves, Reactors, Plant shut down and plant start up, Process safety during plant startup and shutdown and Software used in an Industry, Industrial Engineering, Process Engineering related videos.
That is why! You must Subscribe the Core Engineering TH-cam Channel and follow our other social media handles.
Your Suggestions are Always Welcome!
Best!
Core Engineering Team
Contact us : [e-mail]

[@Coreengineers]

Watch more technical videos:👇
1. Industrial Engineering Videos:
th-cam.com/play/PLrqNx2OqGF51_BYmmF_z2TrR2x0EkVH3z.html
2.Industrial Pump Videos: th-cam.com/play/PLrqNx2OqGF51IVvA2ivV1XdiMRnlWMLsC.html
3. Centrifugal Pump Videos:
th-cam.com/play/PLrqNx2OqGF513HW1AN7M9sw0kTqnO1ESX.html
4. Instrumentation Engineering Videos:
th-cam.com/play/PLrqNx2OqGF50F-gYBOccjSb9E-9F8zCi7.html
5. Piping Engineering Videos:
th-cam.com/play/PLrqNx2OqGF513CRbtuqu77IKBuIak9M3S.html

[@Thuganomer]

You are just telling how to read the graph. Please explain how the graph/curve is obtained.

[@iraqiman8928]

God bless your efforts

[@ACPilot]

How to read KSB multitec pump curves? I need a guide..

[@katuraysalad]

Great video ❤. Very informative

[@adhilmusthafa4195]

Shut off head= 60m

[@ChintanModi-v6u]

By increasing Q, Why H is reducing? Technical reason...

[@Coreengineers]

do practically this in your home by flexible pipe then you'll find the reasons very simple

[@faisal-gd3zy]

By increasing Q, you are increasing the velocity. For real fluid, increasing velocity results in decreasing the head. Because, for greater velocity, head loss by friction is greater as they are proportional.

[@langaliyaparam5436]

60m

[@abdullahmdsadik1668]

I think, if Q decreases, npsh will decrease. So possibility of cavitation will increase. am I right sir?

[@Coreengineers]

Absolutely right! Could you tell why will it happen?

[@gramesh8874]

Sir i think pump develop pressure so increase liquid pressure and reaches to it's temperatures so vapours pressure will increase so available pump suction pressure will be less than vapours pressure of liquid so chances to Cavitation

[@pranali6meshram707]

In our case shut off head is 60m at 0 flowrate .am I right sir?

[@Coreengineers]

yes!

[@pranali6meshram707]

@@Coreengineers made video on cause and effect

[@77steele90]

Ohp

[@pavanvishwakarmatechnicalc4770]

Pls sir hindi me bhi ye vido chyae

[@velaravind7545]

Pls educate yourself

[@aqsam5187]

How I will calculate efficiency if Q and H are in this condition that are not intersecting efficiency curve?

[@Coreengineers]

mainly it consist the that one as well. the curve which I shared individually was for the reference purpose to elaborate the each curve.