A 9.8 m A fluid of relative density 0.88 is flowing through a pipe constant diameter of 15 mm (see the Figure). The pressure at A is 150 kPa and the pressure at B is 225 kPa. The elevation between points A and B is 9.8 m. Calculate the friction loss of the fluid (in meters). (provide your answer with four decimal points)

A 9.8 m A fluid of relative density 0.88 is flowing through a pipe constant diameter of 15 mm (see the Figure). The pressure at A is 150 kPa and the pressure at B is 225 kPa. The elevation between points A and B is 9.8 m. Calculate the friction loss of the fluid (in meters). (provide your answer with four decimal points)

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

See similar textbooks

Similar questions

The device shown in the figure is known as a venturi. In this specific venture, the differential pressure between locations 1 and 2 is 7 psi and the diameter ratio is D2/D1 = 0.35. If D2 = 8 inches, find the air flow rate through the frictionless venture in ft3/min. * (2) Your answer
Water flows into a tank and out through another pipe, as shown in the figure below. The water in the tank has a surface area, Asurf = 5 m². At the bottom of the tank there is a door inclined at an angle = 30 degrees with respect to the horizontal. The door has a length L=0.8 m and a width w=1 m (out of the page). The flowrate into the tank is Q;(t) = 0.18 m³/s and the flowrate out is Qo(t) = 0.03 m³/s At time t = 0, the water has a depth ho = 2.3 m. The density of water is p =1000 kg/m³. Asurf fo ke h(t) Qout
2. Oil with a S.G. pf 0.82 is flowing in a pipe under the condition below (see figure). If the total head loss from point 1 to point 2 is 3 ft, find the pressure at point 2 in PSI. Note: cfs = cubic ft per sec Point 1 D₁-6 im P₁ = 65 psi Q-2.08 efs . Q-2.08 efs Point 2 D₂-9 in P₂ = ? 10.70 ft 4.00 ft Reference datum
In the system given in the figure, oil is pumped from one tank to another tank that is open to the atmosphere with a flow rate of 0.03 m3/s in a commercial steel pipe system of 4 inch 40 Schedule size. The pressure measured at point A is 180 mmHg (ρMercury = 13600 kg/m3 ), calculate the required pump power (kW).
A commercial venturi meter is placed in a vertical pipe as shown below. Pressure gauges are located at section 1 and section 2 and the pipe and throat diameters are as indicated. Assume that Cd-0.97 and calculate the downward discharge of water corresponding to pressures p1=65 kPa and p2=40 kPa.. Also, calculate the velocity at section 2. 20 cm 1 0.4 m 2 10 cm
Prob 4.Draw fbd.
a. 2 +5i-4en +6i 44 en 个 \ 23° 1 - i i
= Water flows into a tank and out through another pipe, as shown in the figure below. The water in the tank has a surface area, Asur f 5.6 m². At the bottom of the tank there is a door inclined at an angle = 25 degrees with respect to the horizontal. The door has a length L = 1.1 m and a width w=1 m (out of the page). The flowrate into the tank is Q₁ (t) flowrate out is Qo(t) = 0.05 m³/s At time t = Asurf = 0.26 m³/s and the 0, the water has a depth ho = 2.5 m. The density of water is p = 1000 kg/m³. Ө h(t) Qout
A capillary tube d =5 mm in dia meter is placed in a liquid.The surface tension is = 0.05N/m, and the angle B made by the liquid with the wetted tube wall is 60 degrees. Thedensity of the liquid is p = 500kg/m3. What is the height to which the liquid will rise in the tube?
An oil of viscosity 0.24 Ns/m² and relative density 0.89 is flowing through a circular pipe of diameter 70 mm and length of 200 m. The rate of flow of fluid through the pipe is 4.8 litres/s. Find the pressure drop in a length of 200 m and also the shear stress at the pipe wall.
Q2: Water flow in a pipe as shown in the figure if the velocity of the fluid at section A is 1.8 m/s and at section D 1.36 m/s. Find A 1. pressure drop at section C d-300 mm d-400 mm 2. head losses at section D Take the density of water 1000 kg/m³ and viscosity of water 998 × 10-6 N.s/m² B 5 m- d-150 mm d-125 mm D
Given an open tank filled with oil that is discharging through a 35-meter long commercial annulus pipe as shown in figure below. Calculate the volume flowrate at point 2 when the oil surface is 5 meters from it. Neglect entrance effects take kinematic viscosity equal to 4 x10* m/s. (Ro and Ri are radaii). h = 5 m Ro = 5 cm %D Ri = 2 cm Q. V L= 35 m Oil (SG = 0.9) %3D