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Watch more technical videos:👇1. Industrial Engineering Videos:ruclips.net/p/PLrqNx2OqGF51_BYmmF_z2TrR2x0EkVH3z2.Industrial Pump Videos: ruclips.net/p/PLrqNx2OqGF51IVvA2ivV1XdiMRnlWMLsC3. Centrifugal Pump Videos:ruclips.net/p/PLrqNx2OqGF513HW1AN7M9sw0kTqnO1ESX4. Instrumentation Engineering Videos:ruclips.net/p/PLrqNx2OqGF50F-gYBOccjSb9E-9F8zCi75. Piping Engineering Videos:ruclips.net/p/PLrqNx2OqGF513CRbtuqu77IKBuIak9M3S
Can you please make a video for run out condition of pump?
Already prepared please check it out the playlist
70Mtr
how %rise to shut off effect the pump if it increase the margin and decrease the margin how it effects
We use to multiply 1.30 in shut-off head..why??
62m Shut Off pressure will be there if the flowrate reaches to 0
sir shut off pressure is density x acceleration due to gravity x height = density is kg/m3 x 9.81 m/sec2 x height in meters how we will get in kg/m2........
Kg-m /s2 is newton got the answer thank you sir
if i have a pump of 2.5 horsepower, will the shut-off head be different for different-density liquid?
Head is independent of density
Sir plz answer the graph why pr vs Q is not considered...
Because head is unchanged with fluid density.
Why we take 30% margin in calculation of shut-off head??
It's safe to take margin
Watch more technical videos:👇
1. Industrial Engineering Videos:
ruclips.net/p/PLrqNx2OqGF51_BYmmF_z2TrR2x0EkVH3z
2.Industrial Pump Videos: ruclips.net/p/PLrqNx2OqGF51IVvA2ivV1XdiMRnlWMLsC
3. Centrifugal Pump Videos:
ruclips.net/p/PLrqNx2OqGF513HW1AN7M9sw0kTqnO1ESX
4. Instrumentation Engineering Videos:
ruclips.net/p/PLrqNx2OqGF50F-gYBOccjSb9E-9F8zCi7
5. Piping Engineering Videos:
ruclips.net/p/PLrqNx2OqGF513CRbtuqu77IKBuIak9M3S
Can you please make a video for run out condition of pump?
Already prepared please check it out the playlist
70Mtr
how %rise to shut off effect the pump if it increase the margin and decrease the margin how it effects
We use to multiply 1.30 in shut-off head..why??
62m Shut Off pressure will be there if the flowrate reaches to 0
sir shut off pressure is density x acceleration due to gravity x height = density is kg/m3 x 9.81 m/sec2 x height in meters how we will get in kg/m2........
Kg-m /s2 is newton got the answer thank you sir
if i have a pump of 2.5 horsepower, will the shut-off head be different for different-density liquid?
Head is independent of density
Sir plz answer the graph why pr vs Q is not considered...
Because head is unchanged with fluid density.
Why we take 30% margin in calculation of shut-off head??
It's safe to take margin