A vertical venturi meter 150mm diameter is installed in a 300mm diameter vertical pipe as shown. The flow is upward. If the specific gravity of mercury at the bottom part of the manometer is 13.6, determine the a) Discharge if head loss is neglected is Blank 1 cu.m./s b) Discharge if head loss is 2m from point 1 to point 2 is Blank 2 cu.m./s c) Coefficient of discharge is Blank 3

A vertical venturi meter 150mm diameter is installed in a 300mm diameter vertical pipe as shown. The flow is upward. If the specific gravity of mercury at the bottom part of the manometer is 13.6, determine the a) Discharge if head loss is neglected is Blank 1 cu.m./s b) Discharge if head loss is 2m from point 1 to point 2 is Blank 2 cu.m./s c) Coefficient of discharge is Blank 3

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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100mmgl 个一 680mm 320 mm I320m 300mm A H2O A vertical venturi meter 100mm diameter is installed in a 300mm diameter vertical pipe as shown. The flow is upward. If the specific gravity of the mercury at the bottom part of the manometer is 13.6, determine the a) Discharge neglecting head loss, b) Discharge if head loss from point 1 to point 2 is 500mm, and c) Coefficient of discharge (This is a multiple answer question. You must have 3 selected choices since there are 3 required answers in the problem) A No answer among the choices in question A B No answer among the choices in question C C = 0.819 D No answer among the choices in question B E) Q = 70.3 L/s Qt = 86.2 L/s G) Qt = 65.8 L/s H) Q = 86.2 L/s Q = 65.8 L/s C = 0.936 к) с30.753 Qt = 70.3 L/s M) C = 0.668 N) Qt = 57.6 L/s o Q = 57.6 L/s
... 2 150mm dia. 1 300mm dia. 800 mm Water Mercury (SG = 13.6) A vertical venturi meter 150mm diameter is installed in a 300mm diameter vertical pipe as shown. The flow is upward. If the specific gravity of mercury at the bottom part of the manometer is 13.6, determine the a) Discharge if head loss is neglected is Blank 1 cu.m./s b) Discharge if head loss is 2m from point 1 to point 2 is Blank 2 cu.m./s c) Coefficient of discharge is Blank 3
A liquid whose specific gravity is 2.0, is flowing in a 50mm diameter pipe. The total head at a given point was found to be 17.5m. That point is 3m above the datum and the pressure in the pipe is 65.6KPA. Compute the discharge in that point of the pipe. (A 24.31 L/s B) 29.05 L/s (c) No Answer among the choices 32.56 L/s E) 19.28 L/s
M MEQ2.jpg 200mmø 690mm 300 mm 400 mmø Z Hg (13.6) A 200mm diameter venturi meter is installed in a 400mm diameter vertical main pipe as shown. If the deflection of mercury (SG = 13.6) at the manometer reads 300mm and the vertical distance between point 1 and point 2 is 690mm, determine the discharge in the system assuming a head loss of 600mm. Hide answer choices a A) 307.36 L/s B) 279.84 L/s No Answer among the choices D) 224.67 L/s 256.29 L/s O O O O C
Cooling water having a density and viscosity of 998 kg/m3 and 0.95 cP isflowing thru a 25-mm med. wt. steel pipe (I.D. = 0.0272 m). The pipeline isequipped with a venturi meter of 10 mm throat diameter and a U-tubemercury manometer. If the water flows at a rate of 25.0115 liters perminute, determine the corresponding manometer reading.
it a past year so it not a graded question... A vertical venturimeter carries a liquid of specific gravity 0.8 and has inlet and throat diameters of 150mm and 75mm respectively. The pressure connection at the throat is 150mm above that at inlet. The actual flow rate is 40 Liter/s and the discharge coefficient is 0.96, calculate: (i) The pressure different between inlet and throat(ii) The difference of levels in a vertical U-tube mercury manometer connected between these points, the tube above the mercury being full of liquid. (Take specific gravity of mercury= 13.6)
A cylindrical tank with vertical axis contains water. A 50 mm orifice is located at the side 0.60 m above the bottom of the tank and 1.50 m directly above the orifice is another orifice 75mm diameter. Cv is 0.98 and C is 0.61 for both orifices. Determine the: show complete solution thumbs up guaranteeda. h1 in metersb. Discharge in the lower orifice in lit/secc. Total discharge from the 2 orifices in lit/sec
3. A 30m long, 20mm diameter steel pipe is used to drain an oil tank determine the discharge 3E when the oil level in the tank is 4m above the exit of the pipe. Neglect minor losses, (assume f = 0.12) 4m D-20 mm, L-30 m, t 0.12
1. 'Water flows through a 12 inches by 6 inches venturi meter at the rate of 1.49 ft/s and the differential gage is deflected 3.5 ft as shown, the specific gravity of the gage liquid is 1.25 A) Compute the change is pressure from point 1 to point 2 (0.875 ft) B) Compute the velocity at the throat (7.75 fps) C) Compute the coefficient of discharge (0.98) 12" 12"
200mmø 690mm 300 mm 400 mmø 金Ho0 Z Hg (13.6) A 200mm diameter venturi meter is installed in a 400mm diameter vertical main pipe as shown. If the deflection of mercury (SG = 13.6) at the manometer reads 300mm and the vertical distance between point 1 and point 2 is 690mm, determine the discharge in the system assuming a head loss of 600mm.
A liquid whose specific gravity is 2.0, is flowing in a 150mm diameter pipe. The total head at a given point was found to be 17.5m. That point is 3m above the datum and the pressure in the pipe is 65.6KPA. Compute the discharge in that point of the pipe. A) No Answer among the choices В 24.31 L/s C) 19.28 L/s D 29.05 L/s E 32.56 L/s
38 lps of water flows through 90 m of a 6 inches nominal diameter, schedule40, cast iron pipe. The pipe contains two 90 degree-standard elbows, two full-open gate valves,a full-open angle valve, and a backflow limiter (check valve). The discharge is located 6 mhigher than the entrance. Consider the water viscosity of 0.01002 Poise. a) Determine thetotal head loss in the pipe line. b) What is the pressure difference between the two ends ofthe pipe? Use the Moody’s equation for the friction factor.