Air at 100 kPa and density of 1.2 kg/m3 flows upward through a 5-cm diameter inclined...
Air at 100 kPa and density of 1.2 kg/m3 flows upward through a 5-cm diameter inclined duct at a rate of 50 L/s. The duct diameter is then reduced to 4 cm through a reducer. The pressure change across the reducer is measured by a water manometer. The elevation difference between the two points on the pipe where the two arms of the manometer are attached is 0.1 m. Determine the differential height between the fluid levels of the two arms of the manometer.
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Air at 100 kPa and density of 1.2 kg/m3 flows upward through a
5-cm diameter inclined...
Problem #4 (30 Points) Air at 110 kPa and 323°K flows upward through a 0.06m diameter...
Problem #4 (30 Points) Air at 110 kPa and 323°K flows upward through a 0.06m diameter inclined duct at a volume flow rate of 0.045 m3/s. The duct diameter is then reduced to 0.04m through a reducer. The pressure change across the reducer is measured by a water monometer (Density 1000 kg/m3) The elevation difference between the two points on the center of the pipe where the two arms of the monometer are attached is 0.2m. (1) Determine the density...
10.00 points Air 129 MPa and 334 Kows upward through a 0.084-m-diameter inclined duct at a...
10.00 points Air 129 MPa and 334 Kows upward through a 0.084-m-diameter inclined duct at a rate of 65 USThe duct diameter is then reduced to 0.064 m through a reducer. The pressure change across the reduceris measured by a water manometer. Determine the differential height between the fluid levels of the two arms of the manometer in centimeters The oferential height between the fuld levels of the two arms Hints esc 80 888
2. (10 points) A uniform air flow in a duct of 10 cm diameter is connected...
2. (10 points) A uniform air flow in a duct of 10 cm diameter is connected a manometer using working fluid of specific gravity of 0.7. The square well of the slant-tube manometer is sufficiently large that the elevation of the manometer fluid in it does not change T-200 significantly when fluid moves up in the leg of the manometer. When there is no flow in the duct, the liquid surface in the manometer les at 2.3 cm measured on...
A liquid of density 1.39 × 103 kg/m3 flows steadily through a pipe of varying diameter...
A liquid of density 1.39 × 103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.67 m/s and the pipe diameter is 11.5 cm. At location 2 the pipe diameter is 14.9 cm. At location 1 the pipe is 8.31 m higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location 1.
A liquid of density 1.11 × 103 kg/m3 flows steadily through a pipe of varying diameter...
A liquid of density 1.11 × 103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.09 m/s and the pipe diameter is 10.9 cm. At location 2 the pipe diameter is 14.1 cm. At location 1 the pipe is 8.03 m higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location 1.
A liquid of density 1.33 x103 kg/m3 flows steadily through a pipe of varying diameter and...
A liquid of density 1.33 x103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.01 m/s and the pipe diameter 12.3 cm is 12.3 cm. At location 2 the pipe diameter is 17.5 cm. At location 1 the pipe is 8.09 m higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location...
A liquid of density 1.21 x103 kg/m3 flows steadily through a pipe of varying diameter and...
A liquid of density 1.21 x103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.97 m/s and the pipe diameter is 10.5 cm. At location 2 the pipe diameter is 16.5 cm. At location 1 the pipe is 8.59 nm higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location 1 10.5...
A liquid of density 1230 kg/m3 flows steadily through a pipe of varying diameter and height....
A liquid of density 1230 kg/m3 flows steadily through a pipe of varying diameter and height. At Location 1 along the pipe, the flow speed is 9.31 m/s and the pipe diameter d1 is 12.9 cm . At Location 2, the pipe diameter d2 is 17.7 cm . At Location 1, the pipe is Δ y = 8.09 m higher than it is at Location 2. Ignoring viscosity, calculate the difference Δ P between the fluid pressure at Location 2...
A liquid of density 1390 kg/m3 flows steadily through a pipe of varying diameter and height....
A liquid of density 1390 kg/m3 flows steadily through a pipe of varying diameter and height. At Location 1 along the pipe, the flow speed is 9.45 m/s and the pipe diameter d1 is 10.3 cm. At Location 2, the pipe diameter d2 is 14.9 cm. At Location 1, the pipe is Δy=9.91 m higher than it is at Location 2. Ignoring viscosity, calculate the difference ΔP between the fluid pressure at Location 2 and the fluid pressure at Location...
A liquid of density 1.29 Ý 103 kg/m3 flows steadily through a pipe of varying diameter...
A liquid of density 1.29 Ý 103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.07 m/s and the pipe diameter is 11.1 cm. At location 2 the pipe diameter is 15.7 cm. At location 1 the pipe is 9.11 m higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location 1.
Problem #4 (30 Points) Air at 110 kPa and 323°K flows upward through a 0.06m diameter inclined duct at a volume flow rate of 0.045 m3/s. The duct diameter is then reduced to 0.04m through a reducer. The pressure change across the reducer is measured by a water monometer (Density 1000 kg/m3) The elevation difference between the two points on the center of the pipe where the two arms of the monometer are attached is 0.2m. (1) Determine the density...
10.00 points Air 129 MPa and 334 Kows upward through a 0.084-m-diameter inclined duct at a rate of 65 USThe duct diameter is then reduced to 0.064 m through a reducer. The pressure change across the reduceris measured by a water manometer. Determine the differential height between the fluid levels of the two arms of the manometer in centimeters The oferential height between the fuld levels of the two arms Hints esc 80 888
2. (10 points) A uniform air flow in a duct of 10 cm diameter is connected a manometer using working fluid of specific gravity of 0.7. The square well of the slant-tube manometer is sufficiently large that the elevation of the manometer fluid in it does not change T-200 significantly when fluid moves up in the leg of the manometer. When there is no flow in the duct, the liquid surface in the manometer les at 2.3 cm measured on...
A liquid of density 1.33 x103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.01 m/s and the pipe diameter 12.3 cm is 12.3 cm. At location 2 the pipe diameter is 17.5 cm. At location 1 the pipe is 8.09 m higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location...
A liquid of density 1.21 x103 kg/m3 flows steadily through a pipe of varying diameter and height. At location 1 along the pipe the flow speed is 9.97 m/s and the pipe diameter is 10.5 cm. At location 2 the pipe diameter is 16.5 cm. At location 1 the pipe is 8.59 nm higher than it is at location 2. Ignoring viscosity, calculate the difference between the fluid pressure at location 2 and the fluid pressure at location 1 10.5...
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