A liquid with density 1010 kg/m2 and viscosity 1.2 mPa.s drains from a building through a...
(b) A Newtonian liquid of viscosity 0.1 N s m2 is flowing through a pipe of 25 mm diameter and 20 m in length, and the pressure drop is 105 Nm2. As a result of a process change a small quantity of polymer is added to the liquid and this causes the liquid to exhibit non-Newtonian characteristics; its rheology is described adequately by the power-law model and the flow index is 0.33. The apparent viscosity of the modified fluid is...
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 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 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. 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 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.
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 1270 kg/m 3 flows steadily through a pipe of varying diameter and height. At Location 1 along the pipe, the flow speed is 9.35 m/s and the pipe diameter d 1 is 10.3 cm . At Location 2, the pipe diameter d 2 is 17.7 cm . At Location 1, the pipe is Δ y = 8.75 m higher than it is at Location 2. Ignoring viscosity, calculate the difference Δ P between the fluid pressure...
Question 3 [20 marks] Water (density p1000 kg/m2; dynamic viscosity 0.001 Pa-s) flows steadily through a horizontal, straight pipe with circular cross section of diameter D=0.2 m. The volumetric flow rate is 0.01 m°/s. Argue that this is turbulent flow. [4 marksl а. Pressure drop in the pipe is due to friction. The pressure drop per unit length can be written as Др 4f L with U the average velocity in the pipe and fthe friction factor. Given the pipe...
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...