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(QI) A pump is used to transport castor oil at 25 C to a refinery located...
4. The discharge pressure gauge reading is 5 lb/in2 (psi) for the pumping system shown in the ske...
4. The discharge pressure gauge reading is 5 lb/in2 (psi) for the pumping system shown in the sketch below, with the outlet nozzle discharging a 2-inch diameter stream of water directly to the atmosphere. The gauge pressure at the pump suction inlet at the point of incipient cavitation is (-2,071.12) lb/ft, i.e., for vapor pressure of water at 68° F of 50.54 lb/ft2 absolute, and standard atmospheric pressure 30 in Hg. Friction losses in the suction piping from the reservoir...
(5) Oil is being pumped from a refinery to a distribution center. The pipe has a...
(5) Oil is being pumped from a refinery to a distribution center. The pipe has a length L 1000 m, diameter D-30 cm, and friction factor f-0.015. The change in elevation between the refinery and distribution center is H-10 m up. The pump power required to pump Q-o2 m3/s is P-70 kW. Calculate the pump efficiency and the power required to pump 2Q (i.e. 0.4 m'/s). Ignore local losses including the inlet and outlet velocity head and assume that the...
(Q1) The piping system shown here has a pump that delivers 10 hp to the fluid...
(Q1) The piping system shown here has a pump that delivers 10 hp to the fluid ant a flow rate of 55 gpm of water at 80 F. Neglecting other losses, (a) evaluate the friction losses in the 272 ft-long discharge pipe and in the 12 ft- long suction pipe. (b) Calculate the pressure (psig) on top of the discharge tank. ...(25 marks) an 7 1.5 in Schedule 80 pipe 220 2 in Schedule 80 pipe
The sketch shows a system used to spray polluted water into the air to increase the water's oxygen content and to cause volatile solvents in the 6. water to vaporize. The pressure at B of the...
The sketch shows a system used to spray polluted water into the air to increase the water's oxygen content and to cause volatile solvents in the 6. water to vaporize. The pressure at B of the nozzle must be 25 psig for proper nozzle performance. The pressure at point A (the pump inlet) is -3.5 psig. The volume flow rate is 0.5 ft3/s. The dynamic viscosity of the fluid is 4.0 x 10 Ib-s/ft?. The specific gravity of the fluid...
Q) Methyl alcohol at 25 C is flowing at the rate of 54000 lit/h. The suction line is a standard 4...
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Q) Methyl alcohol at 25 C is flowing at the rate of 54000 lit/h. The suction line is a standard 4-in Schedule 40 steel pipe, 1500 cm long. The total length of 2-in Schedule 40 steel pipe in the discharge line is 200 m. Assume the entrance from reservoir 1 is through a square-edged inlet and that the elbows are 90° standard. The valve is fully open globe valve. A) List the piping systems components B) Generate...
Water is drawn into the pump, such that the pressure at the inlet A is -45...
Water is drawn into the pump, such that the pressure at the
inlet A is -45 kPa and the pressure at B is 110 kPa . The pipe has
a constant diameter of 100 mm. The discharge at B is 0.08 m3/s.
Take h = 2 m.
Determine the power output of the pump. Neglect friction
losses.
Course Homepage - Fall 2019T X Mastering Engineering Mastering x C Get Homework Help With Chege x + -ox € → C session.masteringengineering.com/myct/itemView?assignmentProblem...
Problem #5 The figure below shows a submersible pump being used to circulate 60L/min of water...
Problem #5 The figure below shows a submersible pump being used to circulate 60L/min of water based coolant (sg=0.95) to the cutter of a milling machine. The outlet is through a 3/4" Sch 40 steel pipe. Assuming a total energy loss due to the piping is 3.0 N.m/N, calculate the total head developed by the pump and the power delivered to the coolant. Milling machine Flow . C Problem 14 The pipeling shown takes water from a reservoir and terminates...
02. centrifugal pump draws benzene at 25°C (sp. weight of benzene 8.59 kN/m) om a tank whose level is 2.6 m below the pump inlet. The atmospheric pressure (abs). The head loss in the suction pipi...
02. centrifugal pump draws benzene at 25°C (sp. weight of benzene 8.59 kN/m) om a tank whose level is 2.6 m below the pump inlet. The atmospheric pressure (abs). The head loss in the suction piping due to friction and minor osses is 0.8 N.m /N. The vapor pressure of benzene is 13.3 kPa (abs). Determine he available net positive suction head (NPSH) and tell f it is acceptable or not. (10 points) Discharge ine Flew 2.6 m What is...
(100 points) Water at 25°C is pumped at a rate of 0.075m'/s from a reservoir 20m above a pump to a free di...
(100 points) Water at 25°C is pumped at a rate of 0.075m'/s from a reservoir 20m above a pump to a free discharge (this means discharged to atmosphere) 35m above the pump. The pressure on the intake side of the pump is 150kPa and the pressure on the discharge side of the pump is 450kPa. The pipe between the reservoir and the pump is 3 meters of 5in diameter cast iron. From the pump to the discharge the pipe is...
Problem Statement 1 The pump in the system shown below is used to transport water from...
Problem Statement 1 The pump in the system shown below is used to transport water from reservoir A to and discharge it to the open atmosphere at point B. The elevation difference between the two reservoirs is Az, and the piping has a 2000 ft length of 16-in diameter. The flow is fully turbulent with kinetic energy correction factor = 1.1 and the Darcy-Weisbach friction factor f = 0.0002. The minor losses in the system are negligible and can be...
4. The discharge pressure gauge reading is 5 lb/in2 (psi) for the pumping system shown in the sketch below, with the outlet nozzle discharging a 2-inch diameter stream of water directly to the atmosphere. The gauge pressure at the pump suction inlet at the point of incipient cavitation is (-2,071.12) lb/ft, i.e., for vapor pressure of water at 68° F of 50.54 lb/ft2 absolute, and standard atmospheric pressure 30 in Hg. Friction losses in the suction piping from the reservoir...
(5) Oil is being pumped from a refinery to a distribution center. The pipe has a length L 1000 m, diameter D-30 cm, and friction factor f-0.015. The change in elevation between the refinery and distribution center is H-10 m up. The pump power required to pump Q-o2 m3/s is P-70 kW. Calculate the pump efficiency and the power required to pump 2Q (i.e. 0.4 m'/s). Ignore local losses including the inlet and outlet velocity head and assume that the...
(Q1) The piping system shown here has a pump that delivers 10 hp to the fluid ant a flow rate of 55 gpm of water at 80 F. Neglecting other losses, (a) evaluate the friction losses in the 272 ft-long discharge pipe and in the 12 ft- long suction pipe. (b) Calculate the pressure (psig) on top of the discharge tank. ...(25 marks) an 7 1.5 in Schedule 80 pipe 220 2 in Schedule 80 pipe
The sketch shows a system used to spray polluted water into the air to increase the water's oxygen content and to cause volatile solvents in the 6. water to vaporize. The pressure at B of the nozzle must be 25 psig for proper nozzle performance. The pressure at point A (the pump inlet) is -3.5 psig. The volume flow rate is 0.5 ft3/s. The dynamic viscosity of the fluid is 4.0 x 10 Ib-s/ft?. The specific gravity of the fluid...
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you can
Q) Methyl alcohol at 25 C is flowing at the rate of 54000 lit/h. The suction line is a standard 4-in Schedule 40 steel pipe, 1500 cm long. The total length of 2-in Schedule 40 steel pipe in the discharge line is 200 m. Assume the entrance from reservoir 1 is through a square-edged inlet and that the elbows are 90° standard. The valve is fully open globe valve. A) List the piping systems components B) Generate...
Water is drawn into the pump, such that the pressure at the
inlet A is -45 kPa and the pressure at B is 110 kPa . The pipe has
a constant diameter of 100 mm. The discharge at B is 0.08 m3/s.
Take h = 2 m.
Determine the power output of the pump. Neglect friction
losses.
Course Homepage - Fall 2019T X Mastering Engineering Mastering x C Get Homework Help With Chege x + -ox € → C session.masteringengineering.com/myct/itemView?assignmentProblem...
Problem #5 The figure below shows a submersible pump being used to circulate 60L/min of water based coolant (sg=0.95) to the cutter of a milling machine. The outlet is through a 3/4" Sch 40 steel pipe. Assuming a total energy loss due to the piping is 3.0 N.m/N, calculate the total head developed by the pump and the power delivered to the coolant. Milling machine Flow . C Problem 14 The pipeling shown takes water from a reservoir and terminates...
02. centrifugal pump draws benzene at 25°C (sp. weight of benzene 8.59 kN/m) om a tank whose level is 2.6 m below the pump inlet. The atmospheric pressure (abs). The head loss in the suction piping due to friction and minor osses is 0.8 N.m /N. The vapor pressure of benzene is 13.3 kPa (abs). Determine he available net positive suction head (NPSH) and tell f it is acceptable or not. (10 points) Discharge ine Flew 2.6 m What is...
(100 points) Water at 25°C is pumped at a rate of 0.075m'/s from a reservoir 20m above a pump to a free discharge (this means discharged to atmosphere) 35m above the pump. The pressure on the intake side of the pump is 150kPa and the pressure on the discharge side of the pump is 450kPa. The pipe between the reservoir and the pump is 3 meters of 5in diameter cast iron. From the pump to the discharge the pipe is...
Problem Statement 1 The pump in the system shown below is used to transport water from reservoir A to and discharge it to the open atmosphere at point B. The elevation difference between the two reservoirs is Az, and the piping has a 2000 ft length of 16-in diameter. The flow is fully turbulent with kinetic energy correction factor = 1.1 and the Darcy-Weisbach friction factor f = 0.0002. The minor losses in the system are negligible and can be...
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