Calculate the NPSHA in ft for the following configuration of pumping system. (Hint: Use steam tables for the properties of water at the given temperature) Suction Line Losses =5 t (1.52m) Atmospheric Pressure= 14.000 psia (1.013 bara) Datum 10 A (3.05 m) Minimum Operable Liquid Level Water, 68F (20C)

Calculate the pressure range for the given bubbler? A = 5 cm, B = Max Level = 1 m, S.G. = 1.4 Blank #1: Min = Blank #2: Max = cmWC cmWC

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The differential pressure is 15"WC and the distance between the bubbler tubes is 3". Calculate the density of the liquid?

Fluid mechanic is our subject

Water is contained in both sides of the cylinder system shown below and the valve is closed. If the pressure on the right hand side of the valve is 119.6 kPa, what is the height in tank B, i.e. what is hp 1? Assume that the atmospheric pressure is 100 kPa, the acceleration due to gravity is 9.807 m/s² and the density of water is 1000 kg/m³. A Po B ha,1=1.5 m Water Water hg,1 1.0 m 0.5 m Pval,left Pyal,right A) 1.0 m B) 1.5 m C) 2.0 m D) 2.5 m

If the compressor suction pressure is 70 pounds per square inch gaugepressure (psig) and the outside temperature is 85°F, what should thedischarge pressure be reading?

please include fbd A 22 L kerosene tank is filled with 2 cm diameter hose equipped with a 1.5 cm nozzle meter If it takes 20 s to fill the tank, determine the pressure differnce indicated by the nozzle if Cd= 0.96. The specific gravity of kerosene is 0.82. a. 12.8 kPa b. 11.8 kPa c. 10.8 kPa d. 9.8 kPa

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2. A turbine is used to produce 2700 hp by expanding the water between points 1 and 2. Water flow rate, static pressures and pipe diameters are given. Calculate the power lost in between point one and two. Note that the static pressure at point 2 is given in vacuum. (SGH =13.6) P1 = 60 psi Q = 150 ft³/s D = 3 ft Section (1) Turbine 10 ft P2 10-in. Hg %3D vacuum D2 = 4 ft Section (2)