1. A Venturi meter, 12 in. by 6 in., is installed in a vertical pipe line carrying water. A differentialmanometer containing mercury is attached to inlet and throat, the difference z in gage levelsbeing 2.50 ft. Compute the actual discharge assuming a Venturi coefficient of 0.97.12 inDatum Plane

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Answered: 1. A Venturi meter, 12 in. by 6 in..,…

Structural Analysis

6th Edition

ISBN:9781337630931

Author:KASSIMALI, Aslam.

Publisher:KASSIMALI, Aslam.

Chapter2: Loads On Structures

Section: Chapter Questions

Problem 1P

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2. A venturimeter is used to determine the flow of water through the reading of a manometer connected through it (Figure 1). Figure 1: Schematic diagram of a venturimeter. 15p7 The relationship between the pressure drop and flow rate is as follows: P – P, = - 24 Where, V = Volumetric flow rate of water. P1, P2= Pressure at point 1 and point 2 respectively. p= Density of the fluid, and Ai= Area at point 1. Data: Density of water = 1000 kg/m³. Diameter if inlet pipe = 2 m.
The total head loss from A to E is 12 meters. Determine the following: discharge in pipe no. 1. = _________ m3/s head loss in pipe no. 3. = _________ meter discharge in pipe no. 2. = _________ m3/s
A pump draws water from a sump through a vertical 6" pipe. The pump has a horizontal discharge pipe 4" in diameter that is 10.6 ft above the water level in the sump. While pumping 1.25 cfs, gases near the pump at the entrance and discharge read -4.6 psi and +25.6 psi, respectively. The discharge gage is 3.0 ft above the suction gage. Compute the horsepower output of the pump and the head lost in the 6" suction pipe.Answer: 10.7 hp, 2.4 ft
... 300 mmg 100 mmø H20, 500mm EHgC(13-6) A 100mm diameter venturi meter is installed in a 300mm diameter horizontal main pipe as shown. If the deflection of mercury (SG = 13.6) at the manometer reads 500mm, determine the discharge in the system assuming no head loss. (A) No Answer among the choices (B) 94.12 L/s 82.44 L/s 77.36 L/s (E) 87.86 L/s
300 mmg 100 mmø H2O, 2) 500mm A 100mm diameter venturi meter is installed in a 300mm diameter horizontal main pipe as shown. If the deflection of mercury (SG = 13.6) at the manometer reads 500mm, determine the discharge in the system assuming no head loss.
A differential gauge was attached to a venturi meter. The deflection of mercury is 14.3 inches. Assume no headloss. Point B is located at the 6 inches diameter pipe. Point A is located at the 12 inches pipe. Determine the flow rate in ft^3/s. 6 indves 12 inches 143 in
a. Determine the velocity of flow in the pipe in m/s. b. Determine the discharge Q in m^3/s. c. How many meters above the center of the pipe will water stand in piezometer tube 3? d.
2. A Venturi meter having a diameter of 6 in. at the throåt is installed in a horizontal 12-in. water main. In a differential gage partly filled with mercury (the remainder of the tube being filled with water) and connected with the meter at the inlet and throat, what would be the difference in level of the mercury columns if the discharge is 5.0 cfs? Neglect loss of head.
Q3: In venture meter, the volume water through 10 second is 500ml.the total head of water for points (1) and (5) are 0.13 and 0.16 m. Find:- 1) Actual of discharge 2) Theoretically of discharge 3) Coefficient of discharge 4) If coefficient of discharge is 0.96, find theoretically of discharge.
A nozzle meter is another device used to determine the flow velocity and flow rate in pipe. The nozzle meter installed in a pipe shown in Figure 4 is horizontal. Derive the equation for the flow velocity and the flow rate in the pipe. (1) Nozzle P,V d2 Pipe Figure 4 Cs Scanned with CamScanner
Determine (a) the discharge in the tube immediately after it is opened. Determine (b) the time for the water surface in each tank to be at the same level. Determine (c) the time for the difference in the water surface to be 4 meters.....
According to the Engineering Tool Box com. a standard value for the discharge coefficient of an orifice meter is ....... 1 O 0.6 O 0.92_0.99 O

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1. A Venturi meter, 12 in. by 6 in.., is installed in a vertical pipe line carying water. A differential manometer containing mercury is attached to inlet and throat, the difference z in gage levels being 2.50 ft. Compute the actual discharge assuming a Venturi coefficient of 0.97.