3.) A reservoir has a low water level set at 200ft. The pump is set at 190 ft. It was determined through analysis that an existing pump is experiencing cavitation. Which of the following will decrease the risk of cavitation?
a. Increase the elevation of the pump
b. Increase the temperature of the water
c. Decrease the diameter of the suction pipeline
d. Decrease the pump speed
e. Increase the size of the pump impeller
Cavitation is the formation and accumulation of bubbles around a pump impeller.when these bubbkes burst due to pressure, the impeller gets erooded and ruduces the efficiency of system. it can be avoided by many ways :
3.) A reservoir has a low water level set at 200ft. The pump is set at 190 ft. It was determined through analysis that a...
A reservoir has a lower water level set at 200 ft. The pump is set at an elevation of 190 ft. It was determined through analysis that an existing pump is experiencing cavitation. Which of the following will decrease the risk of cavitation? Select all that apply. A) Raise the elevation of the pump. B) Increase the temperature of the water. C) Decrease the diameter of the suction pipeline. D) Operate the pump at a lower speed. E) Increase the...
A reservoir has a lower water level set at 200 ft. The pump is set at an elevation of 190 ft. It was determined through analysis that an existing pump is experiencing cavitation. Which of the following will decrease the risk of cavitation? Select all that apply. A) Raise the elevation of the pump. B) Increase the temperature of the water. C) Decrease the diameter of the suction pipeline. D) Operate the pump at a lower speed. E) Increase the...
The value of (NPSHfor a pump is given by the manufacturer as 20 ft. Water is being pumped from a reservoir at a rate of 25 cfs. The water level in the reservoir is 6.0ft below the pump. Atmospheric pressure is 14.7 psia and water temperature is 40℉. If the total head loss in the suction pipe is 4.0 ft, is the pump safe from cavitation effects?
A centrifugal pump is used to pump water at 77ºF from a reservoir whose surface is 20 ft above the centerline of the pump inlet. The Pipe System consists of 67.5 ft of PVC pipe with a 1.2 in ID and negligible average internal roughness height. The length of the pipe from the bottom of the lower tank to the pump inlet is 12 ft. There are several minor losses in the pipe: an acute edge entry (KL = 0.5),...
3. A pump is to be used to pump water from the lower re servoir at an elevation of 10 ft The pump has a characteristic curve ft up to a reservoir shown in the graph below. What will be the volumetric flow rate of the water in this system? Elevation- 35 ft L- 50 t D-10 in -0.020 L-950 ft rid- Elevation 20A D-10 i -0.020 Elevation-15ft 80 60 40 Pump curve 20 1000 2000 3000 4000 5000 O,...
3· T ump delive lvers water at 60F from the lower at a rate of 2.5 ft/s. The suction line is 12-ft gs shown and the discharge line has a e the long with fittings ength of 190-ft with fittings shown. Assume piping used is Schedule 40 steel pipe. Detc following: a) Suction line size (1 mark) /0aase returs b) Discharge line size (1 mark) c) NPSH,for the suction line (2 marks) d) Pressure at the pump inlet (2 marks)...
1. You are designing a pumping station and have been asked to size and select a pump from 2 models. The system step is as follows: the discharge line is a 21-inch diameter PVC pipe with an assumed constant friction factor of f 0.014. The length of the piping is 2300 ft with an elevation gain of 40 ft and an exit loss (K-1.0).. The pump station is located near sea level and the temperature of the flow stream is...
1. Water at 100°F is pumped from a sea-level reservoir to a tank open to the atmosphere through a new 14-in ID galvanized iron pipe as shown below. The minor loss coefficients in the suction and discharge piping are EK = 1.5 and Eduk = 7.2. Perform the following: a. derive the equation for the system curve as hy = a + b where he and a have units of feet and b has units of ft/gpm); b. plot the...
6. Determine the setting of a centrifugal pump, given that flow rate = 2.4 m/min; diameter of intake pipe = 160 mm; entrance losses = one velocity head in suction pipe; required NPSH = 42 kPa; water temperature = 30°C N D1, D2 : inlet and outlet diameters of impeller (rotor) b : impeller width 0,6 : inlet and outlet impeller vane angles (degrees) : speed of rotation of impeller (and its driver) in rpm V, V :tangential and radial...
3- Assume a pumped hydro energy storage arrangement that pumps up water from a low- level water reservoir to a higher-level reservoir to store energy. The water then is running back from the top reservoir down to the low reservoir through the pipe by passing a turbine. Assume a reasonable case of your choice and calculate the efficiency of this arrangement for storing energy (i.e. the electrical energy delivered by the turbine divided by the electrical energy used by the...