A condition of the venturi meter is in horizontal with inlet diameter 315 mm. Venturi meter discharge coefficient is 0.97. Mercury level height differences in the different U tube shows 235 mm of the actual flow rate is 0.15 m³/s. Calculate the diameter of the throat of the venturi meter.

A condition of the venturi meter is in horizontal with inlet diameter 315 mm. Venturi meter discharge coefficient is 0.97. Mercury level height differences in the different U tube shows 235 mm of the actual flow rate is 0.15 m³/s. Calculate the diameter of the throat of the venturi meter.

Name: pls do step by step. Fluid mechanics diploma level... Don't type. Writ
Uploaded: 2024-03-20T06:56:55.000Z
Channel: Bartleby
Description: pls do step by step. Fluid mechanics diploma level... Don't type. Write on a paper step by step. showsA condition of the venturi meter is in horizontal with inlet diameter 315 mm. Venturi meterdischarge coefficient is 0.97. Mercury level height diffe

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

See similar textbooks

Similar questions

peton with a relative density of 0.78 flows upward in a vertical venturimeter having a discharge coefficient Cd of 0.98.it has a diameter of 160mm and 80mm at inlet and throat respectively.U Tube manometer connected by normal way and shows level of different of 299mm determine ,1) the flow rate???
The following system is fed by a centrifugal pump. The piping is constructed from smooth plastic of OD 55 mm, wall thickness 2.5 mm. The minor losses for the system prior to the pump are given by KL = 12.0. The system curves for this pump are attached. If the flowrate is reduced to 1.4 m3/hr, and the upstream head requirement were 17 m, what would the electrical power requirement of the pump be?
An oil of specific gravity 0.89 is flowing through a horizontal venturimeter fitted to a 242 mm diameter pipe at the rate of 108 liters/s and throat diameter is 98 mm. The entrance and throat of the venturimeter are connected in the two limbs of a U-tube mercury manometer. The difference in mercury level shows 841 mm. Calculate (i) the head difference in m of oil, (ii) the theoretical discharge in m3/s, (iii) the actual discharge in m3/s, and (iv) the coefficient of discharge of a venturimeter. If instead of a U-tube mercury manometer, the pressure gauges are inserted at the entrance and throat of venturimeter. Find (v) the pressure at the throat in N/mm2, if the entrance pressure gauge shows0.13 N/mm2.
The venturi meter experiment observation readings are 308 mm, 285 mm, and the flow meter reads 165 liter/hr. The area of the pipe is 338.6 mm2 and the throat area is 84.6 mm2. Calculate the coefficient of discharge. coefficient of discharge=
A test on 30-cm-diameter pipe with water showed a gage difference of 33 cm on mercury-water manometer connected to two piezometer rings 120 m apart. The flow was 0.23 m/s. What is the friction factor?
A pipe experienced a total head loss of 15 m, determine thepressure difference from its starting point to discharge point inkPa.
Estimate the power developed by a hydro project which has a stream of 100 l/s of flow at s 60 m of head. Assume the density of water is 993 kg/m3 and efficiency of the whole setup is 63 %.
The 28-in-diameter pump in Fig. at 1170 r/min isused to pump water at 20°C through a piping system at14,000 gal/min. (a) Determine the required brake horsepower.The average friction factor is 0.018. (b) If there is65 ft of 12-in-diameter pipe upstream of the pump, how farbelow the surface should the pump inlet be placed to avoidcavitation?
An inclined venturi meter has an entrance of 0.08 m in diameter and throat of 0.02 m in diameter. Calculate the coefficient of discharge when the pressure difference between the entrance and the throat is 173kN/m^2. The venturi meter used to measure the discharge of the 311 dm^3/minute. Throat is 0.46m higher than the entrance.
In a 225 mm pipeline 0.14 m3/s of water are pumped from a reservoir of surface elevation30 over a hill of elevation 50. A pump of what power is required to maintain a pressure of 345kPa on the hilltop if the head lost between reservoir and hilltop is 6 m?
A venturi meter of 20 mm throat diameter is used to measure. The velocity of water in a horizontal pipe of 40 mm diameter. If the pressure difference between the pipe and the throat sections is found to be 30 KPa then, neglecting frictional losses, the flow velocity is?
estimate the allowable distance Y if the allowable pressure in the systems is -18kPa (gage). aasume that the volume flow rate is 5.6 x 10^-3 m^3/s