8. A vertical Venturi meter, 150 mm in diameter is connected to a 300-mm diameterpipe. The vertical distance from the inlet to the throat being 750-mm. If the deflection ofthe mercury in the differential manometer connected from the inlet to the throat 360-mm, determine the flow of water through the meter if the meter coefficient is 0.68.Determine also the head lost from the inlet to the throat.

Venturi meters generally flow measurement instruments that use a converging section of make an…

Answered: 8. A vertical Venturi meter, 150 mm 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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Installed is a venturi meter on a pipe 30 cm diameter in which the maximum flow is 2.7 cum of water in one minute. The throat is 15 cm in diameter. Compute the theoretical discharge that would be passing through the meter when the differetial manometer is as shown. Calculate also the discharge coefficient, C.
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.
For Fig. Water flows through a pipe at rate of 350 L/S. The Pipe consists of two sections of diameters 300mm and 150 mm with a smooth reducing section that connects them. The elevation difference between the two points on the pipe where the two arms of the mercury manometer are attached is 0.20m. Determine the reading of manometer (Answer with sketch)
5. Z is a draft tube is a) Temperature difference b) Pressure drop c) Kinetic energy difference d) Datum head View Answer
This problem uses Figure 2. Select all that are true about this manometer set-up. Open Air Tank (A) (1) BU (4) Z₁ (2) (3) P₁-P₁=1²1 - 7222 P4 - PA = 71 (21 +22) P₁ = PA-1²1 + 72²2 PA = P₁ Y2
Calculate the pressure difference between points A and B for the differential manometer below.
Connected to an 18-inch water line is a 6-inch horizontal Venturi meter, with a meter coefficient of 0.94. Theobserved average deflection on the differential manometer from the start of the converging cone to the through is15 inches of a fluid with a specific gravity of 8.0. Compute for the head loss between the inlet and the throat.
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600mm water diameter 300mm 1. diameter 02 150mm Mercury (SG = 13.6) A venturi meter with diameter of 300mm is attached to a 600mm main pipe and has its axis inclined downward as shown. a) Discharge if head loss is neglected is Blank 1 cu.m./s b) Discharge if head loss is 500mm from point 1 to 2 is Blank 2 cu.m./s c) Coefficient of discharge is Blank 3 The manometer shows a deflection of 15cm of mercury (SG =13.6). If the flowing fluid is water and direction is from 1 to 2, determine the
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The throat area of a c-d nozzle is 10 cm^2 and its exit is 20 cm^2. If the stagnation pressure is 1 bar, what is the exit pressure (Pe) range needed to ?chock the throat greater or equal 0.935 bar O less or equal 0.937 bar O greater or equal 0.0935 bar and less or equal 0.937 bar greater or equal 0.937 bar and less or equal 1 bar O

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