H₂=4 m f=0.15 D₁ = 50 mm H₁ = 4 m 25 m L=100 m A. Two tanks A and B were connected by a 50 mm-diameter pipe (f=0.15) that is 100 m in length. Calculate the total flow between the two tanks. B. A pipe of 200mm diameter (f-0.01) and length X is to be connected in series to replace X length of the 50mm pipe. If the purpose is to increase flow by 50%. Find Length X. La=X f=0.01 D. = 200 mm

H₂=4 m f=0.15 D₁ = 50 mm H₁ = 4 m 25 m L=100 m A. Two tanks A and B were connected by a 50 mm-diameter pipe (f=0.15) that is 100 m in length. Calculate the total flow between the two tanks. B. A pipe of 200mm diameter (f-0.01) and length X is to be connected in series to replace X length of the 50mm pipe. If the purpose is to increase flow by 50%. Find Length X. La=X f=0.01 D. = 200 mm

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

Given below are pipe lengths, sizes and connections. All pipes have a friction factor of 0.020. If the flow from A to B is 8cfs. a.) Determine the head loss in feet in PIPE 1. b.) Determine the head loss in feet in PIPE 5. c.)Determine the flow in the upper branch pipe Q2 in cubic feet per second.
For the piping system shown below, determine the flow distribution and the piezometric heads at the junction (j) using the Newton-Raphson Method of solution, power 20 Kw D = 0.2 m, D,= 0.15 m, D,= 0.15 m f= 0.021, f,= 0.018, f, = 0.023 L1=100 L2=145 L3=350 30 m В 2 15 m 10 m A Pump 1 j
Two sharp-ended pipes of diameter d₁ = 50 mm, and d₂ = 100 mm, each of length 100 m, are connected in parallel between two reservoirs which have a difference of level h= 10 m, as shown in figure below. If the friction coefficient, f= 0.032 for each pipe, calculate: a. the rate of flow for each pipe, b. the diameter d of a single pipe 100 m long which would give the same flow if it was substituted for the original two pipes, (Notes: Use Darcy Weisbach's equation, h,= (flv²)/(2dg) Pipe 2- Pipe 1 h = 10 m 110
Please answer it soon
Two pipes A and B are connected in parallel between two points M and N as shown in figure. Pipe A is 80 mm diameter, 900 m long and its friction factor is 0.015. Pipe B is of 100 mm diameter, 700 m long and its friction factor is 0.018. A total discharge of 0.030 m³/s is entering the parallel pipes through the division at M. Calculate the discharge in the two pipes A and B. M = 0.015 A fA 80 mm dia, 900 m 100 mm dia, 700 m B fB = = 0.018 N
i need the answer quickly
The pump whose characteristics are: H, = 80 – 600V²2 %3D n = -1500V² + 700V Elevation = 230 m |(2) (1) Elevation = 200 m 1000 m pipe 40 cm in diameter Pump Figure Q3 is used to pump water (µ=0.001kg/ms) a distance of 1000 m between two reservoirs the elevations of which are shown in Figure Q3 and remain constant. The pipe is 40 cm diameter commercial steel (ɛ=0.046 mm). Ignoring minor losses and assuming fully turbulent flow. Determine d) The volumetric flow rate e) The efficiency at the operating point
Time: 60 Q1: pump puts 2kw in to the system. Find: b. The pressure in the pipe on section side of the pump (at C). a. Discharge. C 5 kPa L = 200 m 10m ↓ Air Water 55 marks 15 m P L = 50m D = 6 cm f = 0.025 D = 8 cm f = 0.030
Determine the flow distribution of water in the system shown in Figure below. Assume constant friction factors, with f= 0.03. The head-discharge for the pump is Hp = 70 m el 50 m Pipe L (m) D (mm) ΣΚ el 48 m 1 100 750 850 350 200 200 [2] [4] 3 el 0m [5] 4 500 200 350 250 [1] [3]
Water flows through a concrete pipe 3 ft in diameter between reservoir A and reservoir B. The surface of reservoir A is at 800 ft while the surface of reservoir B is at 300 ft elevation. The length of the pipe is 1000 ft. Calculate: a. the head loss through the pipe b. the flow rate in the pipe
Question 1: For the setup shown in the figure: H = 20 m f = 0.0012 f = 0.0012 D = 250 mm D = 80 mm L = 50 m L = 50 m f = 0.001 D₁ = 150 mm L = 100 m A. Calculate Q in the 150 mm-diameter pipe B. If the NPSHR of the pump is 3 m. Is it feasible to use the pump? You can use: Patm-101 kN/m², and Pvapor = 3.17 kN/m² H₂ = 10 m Pump Q f = 0.0012 D=80 mm L = 50 m Q₁ = 0.2