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6. A liquid with sg. of 1.26 is...
1 A liquid with a specific gravity of 1.26 is being pumped from A to B...
1 A liquid with a specific gravity of 1.26 is being pumped from A to B through the pipeline of Fig. 55.8. At A the pipe diameter is 24 in (600 mm) and the pressure is 45 psi (300 kPa). At B the pipe diameter is 12 in (300 mm) and the pressure is 50 psi (330| kPa). Point B is 3 ft (1.0 m) lower than A. Find the flow rate if the pump puts 22 hp (16 kW)...
Question - 6 y 1.26 Glycerin (specific gravity 1.26) in a 300 kPa 600 mm dia...
Question - 6 y 1.26 Glycerin (specific gravity 1.26) in a 300 kPa 600 mm dia processing plant flows in a pipe at a rate of (1) 700 L/s. At a point where the pipe diameter is 600 mm, the pressure is 300 kPa. Find the 700 L/S pressure at a second point where the pipe diameter is 300 mm if the second point is 1.0 m lower than the first point, neglect the head loss. 1 m P.? 300...
fluid mechanics SECTION A Petroleum distilate is pumped from one large diameter tank to another higher...
fluid mechanics
SECTION A Petroleum distilate is pumped from one large diameter tank to another higher tank, via a pumping station in an oil refinery. The petroleum is pumped at a speed of 2 ms through a 150 m long pipeline of 100 mm internal diameter. The vertical distance pumped is 20 m. The sum of the entry, exit and other component losses is equivalent to 5 times the velocity head, Table Q1 Fluid density Friction factor f for the...
-2 2 Pipe flow [6 points) A liquid with SG 0.96, 1 = 9.2 x 10-4...
-2 2 Pipe flow [6 points) A liquid with SG 0.96, 1 = 9.2 x 10-4 Nsm-2, and vapor pressure pu = 8000 Nm (absolute) is drawn into the syringe as is indicated in figure 3. What is the maximum flowrate if cavitation is not to occur in the syringe? Assume the flow is laminar. Neglect minor losses. Assume that the velocity of the piston is negligible compared to the velocity in the needle. Atmospheric pressure is Patm 101 325...
Glycerin (specific gravity 1.26) in a processing plant flows in a pipe at a rate of R L/s.
Solve the question below Glycerin (specific gravity 1.26) in a processing plant flows in a pipe at a rate of R L/s. At a point where the pipe diameter is 832mm, the pressure is 300 kPa. Find the pressure at a second point where the pipe diameter is 300 mm if the second point is 1.0 m lower than the first point, neglect the head loss.
4. Water is pumped from a supply reservoir to a water transmission line (ks0.07 mm) as...
4. Water is pumped from a supply reservoir to a water transmission line (ks0.07 mm) as shown below. The highest point of the transmission line is at point A, located 0.5 km (pipe length) downstream of the supply reservoir, and the lowest point of the transmission line is at point B, located 0.25 km (piple length) downstream of point A If the flow rate through the pipeline is 1.1 m3/s, the diameter of the pipe is 700 mm, and the...
2 Pipe flow [6 points) A liquid with SG 0.96, H = 9.2 x 10-Nsm ?,...
2 Pipe flow [6 points) A liquid with SG 0.96, H = 9.2 x 10-Nsm ?, and vapor pressure Pu 8000 Nm-2 (absolute) is drawn into the syringe as is indicated in figure 3. What is the maximum flowrate if cavitation is not to occur in the syringe? Assume the flow is laminar. Neglect minor losses. Assume that the velocity of the piston is negligible compared to the velocity in the needle. Atmospheric pressure is Patm 101 325 Nm-2. =...
lunzontal pipe and pump system in the following figure discharges 0.01583 m3/s. The gage pressure iust...
lunzontal pipe and pump system in the following figure discharges 0.01583 m3/s. The gage pressure iust before the pressure is 400 The m/s2 losses between 20°C water at 57 m3/h 0 kPa and just after the pump the gage a. The pump inlet diameter is 9 cm and the outlet diameter is 3 em. Let g-9.81 pump is 12 o Pwater9 kg/m, Hwate0.001002 kgm-s) and Pat the two pressure points and the pump. But consider frictional losses at the 9-cm...
-2 2 Pipe flow [6 points) A liquid with SG 0.96, 1 = 9.2 x 10-4...
-2 2 Pipe flow [6 points) A liquid with SG 0.96, 1 = 9.2 x 10-4 Nsm-2, and vapor pressure pu = 8000 Nm (absolute) is drawn into the syringe as is indicated in figure 3. What is the maximum flowrate if cavitation is not to occur in the syringe? Assume the flow is laminar. Neglect minor losses. Assume that the velocity of the piston is negligible compared to the velocity in the needle. Atmospheric pressure is Patm 101 325...
Problem 2: Oil at 20 °C (SG 0.88) flows in the 3-cm P= 180 kPa diameter pipe shown in the figure. For the pressure...
Problem 2: Oil at 20 °C (SG 0.88) flows in the 3-cm P= 180 kPa diameter pipe shown in the figure. For the pressure measurements in the figure, determine: a) Whether the flow is up or down b) The head loss between points A and B P 500 kPa 15 m c) The flow rate if losses are about 16% of the 370 velocity head 20 m
Problem 2: Oil at 20 °C (SG 0.88) flows in the 3-cm P=...
1 A liquid with a specific gravity of 1.26 is being pumped from A to B through the pipeline of Fig. 55.8. At A the pipe diameter is 24 in (600 mm) and the pressure is 45 psi (300 kPa). At B the pipe diameter is 12 in (300 mm) and the pressure is 50 psi (330| kPa). Point B is 3 ft (1.0 m) lower than A. Find the flow rate if the pump puts 22 hp (16 kW)...
Question - 6 y 1.26 Glycerin (specific gravity 1.26) in a 300 kPa 600 mm dia processing plant flows in a pipe at a rate of (1) 700 L/s. At a point where the pipe diameter is 600 mm, the pressure is 300 kPa. Find the 700 L/S pressure at a second point where the pipe diameter is 300 mm if the second point is 1.0 m lower than the first point, neglect the head loss. 1 m P.? 300...
fluid mechanics
SECTION A Petroleum distilate is pumped from one large diameter tank to another higher tank, via a pumping station in an oil refinery. The petroleum is pumped at a speed of 2 ms through a 150 m long pipeline of 100 mm internal diameter. The vertical distance pumped is 20 m. The sum of the entry, exit and other component losses is equivalent to 5 times the velocity head, Table Q1 Fluid density Friction factor f for the...
-2 2 Pipe flow [6 points) A liquid with SG 0.96, 1 = 9.2 x 10-4 Nsm-2, and vapor pressure pu = 8000 Nm (absolute) is drawn into the syringe as is indicated in figure 3. What is the maximum flowrate if cavitation is not to occur in the syringe? Assume the flow is laminar. Neglect minor losses. Assume that the velocity of the piston is negligible compared to the velocity in the needle. Atmospheric pressure is Patm 101 325...
4. Water is pumped from a supply reservoir to a water transmission line (ks0.07 mm) as shown below. The highest point of the transmission line is at point A, located 0.5 km (pipe length) downstream of the supply reservoir, and the lowest point of the transmission line is at point B, located 0.25 km (piple length) downstream of point A If the flow rate through the pipeline is 1.1 m3/s, the diameter of the pipe is 700 mm, and the...
2 Pipe flow [6 points) A liquid with SG 0.96, H = 9.2 x 10-Nsm ?, and vapor pressure Pu 8000 Nm-2 (absolute) is drawn into the syringe as is indicated in figure 3. What is the maximum flowrate if cavitation is not to occur in the syringe? Assume the flow is laminar. Neglect minor losses. Assume that the velocity of the piston is negligible compared to the velocity in the needle. Atmospheric pressure is Patm 101 325 Nm-2. =...
lunzontal pipe and pump system in the following figure discharges 0.01583 m3/s. The gage pressure iust before the pressure is 400 The m/s2 losses between 20°C water at 57 m3/h 0 kPa and just after the pump the gage a. The pump inlet diameter is 9 cm and the outlet diameter is 3 em. Let g-9.81 pump is 12 o Pwater9 kg/m, Hwate0.001002 kgm-s) and Pat the two pressure points and the pump. But consider frictional losses at the 9-cm...
-2 2 Pipe flow [6 points) A liquid with SG 0.96, 1 = 9.2 x 10-4 Nsm-2, and vapor pressure pu = 8000 Nm (absolute) is drawn into the syringe as is indicated in figure 3. What is the maximum flowrate if cavitation is not to occur in the syringe? Assume the flow is laminar. Neglect minor losses. Assume that the velocity of the piston is negligible compared to the velocity in the needle. Atmospheric pressure is Patm 101 325...
Problem 2: Oil at 20 °C (SG 0.88) flows in the 3-cm P= 180 kPa diameter pipe shown in the figure. For the pressure measurements in the figure, determine: a) Whether the flow is up or down b) The head loss between points A and B P 500 kPa 15 m c) The flow rate if losses are about 16% of the 370 velocity head 20 m
Problem 2: Oil at 20 °C (SG 0.88) flows in the 3-cm P=...
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