Problem 1 The pipe assembly shown has the following properties: Pipe Length (ft) Diameter (in) 2000 18 2 500 12 3 500 15 4 500 15 S 500 18 6 1000 24 C The velocities in pipes / and 6 are 2 ft/s and 1 ft/s, respectively. It was found out that there are leakages at joints B and C thus, decreasing the discharges in pipes 4 and 5. Determine the decrease in the discharges (in efs) of pipes 4 and 5. Also, calculate the total head loss (in ft) in the pipe assembly. Use the Darcy-Weisbach equation with a friction factor of 0.02.

Problem 1 The pipe assembly shown has the following properties: Pipe Length (ft) Diameter (in) 2000 18 2 500 12 3 500 15 4 500 15 S 500 18 6 1000 24 C The velocities in pipes / and 6 are 2 ft/s and 1 ft/s, respectively. It was found out that there are leakages at joints B and C thus, decreasing the discharges in pipes 4 and 5. Determine the decrease in the discharges (in efs) of pipes 4 and 5. Also, calculate the total head loss (in ft) in the pipe assembly. Use the Darcy-Weisbach equation with a friction factor of 0.02.

Structural Analysis

6th Edition

ISBN:9781337630931

Author:KASSIMALI, Aslam.

Publisher:KASSIMALI, Aslam.

Chapter2: Loads On Structures

Section: Chapter Questions

Problem 1P

See similar textbooks

Similar questions

7. Find the equivalent length of pipe 1 to 2 with a diameter of 300mm and the velocity of line C. Use the figure below and neglect minor losses. U 1 Pipes A B 3C A Length 300 m 150 m 250 m B 00 Diameter 300 mm 200 mm 250 mm C 10 m D f 0.020 0.021 0.020
Within few minutes
HYDRAULICS LABORATORY EXPERIMENT NO.4 3. Using the value of Cd, which you have obtained by experiment, determine the throat diameter of a Venturi meter which would measure a flow of 0.40 m3/s in a pipe of 0.60 meter diameter with a differential head of 0.80 meter
Question 3: A lab test was used to identify the headloss coefficient of a confusor k'e where: h = kE' ,V² -V₂² 2g that is shown in the figure. Two pizometers were installed at A1 and A2, which measured piezometric head of 40 cm and 44 cm, respectively. The diameters are 5 cm, and 10 cm at A1 and A2 respectively Flow was measured as 0.02 m³/s. Find kE' V₁- A1 a A2 -V₂
Does the function, =Ur cose+cose represent possible irrotational flow? r
In the pipe systems (a), (b), and (c) in the Figure, find the flow and velocity in each pipe and the pressure at points A. Assume all nodes are at identical elevations. m/min 20 m/min 20 m /min P- 1000 kP Sm/min 1500 m 1000 m 455 mm 405 mm 1000 m 405 mm 800 m 255 mm 300 m305 mm 300 m 205 men 1100 m 305 mm 1000 m 305 mm A500 m 205 mm 10 m/min 5m/min 10m3/min 5 m/min 15 m /min 5m/min Elev 300 m 405 mm 2000 m 150 2000 m Elev 250 m 5m/min 10 im/min 6 m/min 205 mm 205 mm 2000 m A 2000 m le) 000
ellen 9
O Through the pipeline system in the figure calculate gauge and absulate presures at A and B 12 14 cm 5 Air 15 cm 15 cm A 15 cm Mercury 15 cm Water B 10 cm 5 Cm 25 cm 11 Mercury
QI. s) Q1: A 1 m diameter well penetrates vertically through a confined aquifer (30 m) thick. When the well is pumped at (2712 m³/day), the drawdown in a well 15 m away from pumped well is 1.8 m; while the drawdown in another well 50 m away from pumped well is 0.5 m. Take the maximum head is 40 m. 1- Determine the transmissivity. 2- What is the approximate head in the first well? 3- What is the approximate head in the second well? 4- What is the approximate head in the pumped well for steady-state conditions? 5- What is the approximate drawdown in the pumped well?
Could I get a written solution for this question please?