It depends on the pressure you wish to achieve.
3
The future amount itself and a discount rate.
The dimension of the side in cm are required to calculate the volume (cm3) and density in g/cm3 or specific gravity of the substance is then used to calculate the mass. Mass = Volume x Density
To find which object has a bigger volume, you may be required to use formula to calculate their volumes.
WDF dia npsh WDF WDFWDFWDFWDFWDFWDFWDFWDFWDFWDFWDFWDFWDFWDFWDFWDFWDDFFFF a lot of enters WHO THE **** MADE THIS GAY QUESTION BECUZ THEY ARE VERY DUMB I THINK THATS WHY ****en RETARD!!!!!!!!!!!!!!!!!!!!!!!!!!
first of all the term NPSH should be clear.It is pressure which should be available at the eye of the pump impeller,so as to avoid vaporisation of liquid. Second which arises ,how this liquid will vaporise?Ans-if a vapour pressure of a liquid falls at constt temperature or temperature of liquid is raised at constt pressure it vaporises.In case of pump it's mostly the first case. Now,how to manitain NPSH. NPSHa> NPSHr (always) where NPSHa= available NPSH NPSHr = Required NPSH NPSH = Hps+Hsl-Hvp-Hfl Hps= pressure acting on the eye due to pressure in the suction drum. Hsl = pressure acting due to height of liquid in the suction line. Hvp= vapour pressure of the liquid Hfl= head loss due to friction losses Thus, to maintain the NPSH, variables in hand are,Hps and Hsl.increase the height of the suction line or increase the pressure of the suction drum.
to develop NPSH in BFP
Net Positive Suction Head. It is the difference between hydraulic pressure and vapor pressure, usually of concern at the inlet of a pump. Without sufficienty high NPSH at a pump inlet, there will be cavitation in the pump. Within a centrifugal pump there can be pressures lower than at the inlet as the fluid is moved by the impeller. If any of those pressures is lower than the vapor pressure, vapor pockets- bubbles- form and you get cavitation. A more complete explanation: http://en.wikipedia.org/wiki/NPSH
How do you calculate the production line personnel required?
Use full bore for applications where pressure drop should be minimum (such as in the suction pipe of a pump with required NPSH very close to available NPSH), or for pipes which could be cleaned with a pig (so that the pig doesn't get stuck on the valve). In other applications a reduced bore should be OK.
Capacity, Net Positive Suction Head (NPSH), and Efficiency
Its very easy please follow the steps below, 1. Calculate the DN Required by using Hydrauic calculation 2. Calculate the PN required 3. Calculate the SN required 4. Use the mixuture formula to decide the composition 5. Convert this into Kg/m 6. Use the classical laminate theory to calculate the thicness by forming a nine by nine matrix
The length of pipe is required to be known to help procure the required quantity of pipe.
By calculate do you mean calculate the connections required or phasor diagrams? full question would be helpful
put it in water
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