--1. For supplying water to a colony, it is intended to store water in a Targe tank, whose water surface elevation is presently 85.37 m RL. This tank is being supplied by a pipe line from a junction J, the friction loss in metres of water in this pipe being 0.6 Q-35 where Q is the discharge in m /sec. Junction J receives water under pressure and without leakage from (i) a large reservoir I whose water surface elevation is constant at 100.00 m RL through a pipe characterised by h, constant water level at 96 m RL, through a pipe characterised by h,=0.46 Q1.85 Neglecting losses other than due to pipe friction, determine the incoming flow into the tank in the colony. 1.95 = 0.35 Q2, and (ii) a second large reservoir II with its %3D

--1. For supplying water to a colony, it is intended to store water in a Targe tank, whose water surface elevation is presently 85.37 m RL. This tank is being supplied by a pipe line from a junction J, the friction loss in metres of water in this pipe being 0.6 Q-35 where Q is the discharge in m /sec. Junction J receives water under pressure and without leakage from (i) a large reservoir I whose water surface elevation is constant at 100.00 m RL through a pipe characterised by h, constant water level at 96 m RL, through a pipe characterised by h,=0.46 Q1.85 Neglecting losses other than due to pipe friction, determine the incoming flow into the tank in the colony. 1.95 = 0.35 Q2, and (ii) a second large reservoir II with its %3D

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

Problem 4 Find the flowrate in each pipe. CH= 130 300 gpm Pipe AB BD DC AC с Diameter (in) Length (ft) 250 100 250 100 2.0 2.0 4.0 4.0 B D 190 gpm 110 gpm
3. The flow form A to I is 300 L/s. Using the following data compute the discharge in each pipe Use conventional solution. 7 C 1 D 3 نيا B 5 2 E 6 F .8 G H 9 10 I Pipe AB BE BC BD DF FE CH EG HG GI n 0.012 0.011 0.013 0.014 0.014 0.014 0.013 0.011 0.011 0.012 Diameter (mm) 450 360 300 200 250 200 350 250 300 450 Length in (m) 300 360 370 150 300 150 660 300 370 600
Two reservoirs 1500 m apart have a water surface elevation difference of 18 m. A cast iron pipe with >= 0.26 mm connects the two reservoirs. The entrance is square-edged. The pipe diameter is 0.5 m. Water at 20°C flows under the action of gravity between the 2 reservoirs. A gate valve (Kv = 10 fully open) controls the flow between reservoirs. Determine the discharge when the gate valve is fully open.
Note: Don't copy from Chegg.
Select correct option
3) A centrifugal pump delivers water between two reservoirs with a 300 ft. elevation difference (Az). The 12-in diameter suction pipe (f1= 0.020) is 100 ft. long (L1) and the 10-in diameter discharge pipe (f2= 0.026) is 5000 ft. long (L2). The pump has a performance curve defined by the equation: h, = 375 - Q² where h, is the pump head in feet and Q is the discharge in ft/s. a) Calculate the discharge, Q. b) Calculate the NPSHA. Assume standard atmospheric conditions, 60°F water, and a pump elevation 8 ft. above the lower reservoir Az D, L2 2 D, Ly. ft LOM
The pumping system below is used in a manufacturing process involving glycerin. Find the minimum pump head, E (P), required to prevent contamination of the piping system from reservoir B. the temperature of the glycerin is 60°F. Assume no losses in pipe 2 which connects reservoir B and node A. The check valve only allows flow from reservoir B to node A.
S.speed of the pump.,
Help pls thankss...
Q-5
5. ol with sp. gr. of 0.88 is being pumped frem a lower reservolr to an elevated tank The pump In the system is 65% efflelent and Is rated at 160kW. Determine the flow rate of the oll in the pipe if the total head los (rom point 1 to point 2 is 5.5m of oll. 150m 200-mm Pump Elev 160m Elev. 150 m
Problem 2: A centrifugal pump with an overall efficiency of 0.56 rotates at 1650 rpm. The flow is purely radial at the inlet of the rotor. The pump has the following characteristics: Flow rate Inlet diameter Outlet diameter Head Width at the inlet Width at the outlet Leakage Mechanical loss Blade angle at the outlet The water density Atmospheric pressure |Q=72 L/s DI = 90 mm D2 = 280 mm H= 25m bl -20 mm b2 = 18 mm q =2 L/s Pm = 1.41 kW B2 = 35 p = 998 kg/m³ 101 kPa