600mm diameter water 300mm diameter 02 --------- 150mm Mercury (SG = 13.6) a) Discharge if head loss is neglected is 0.44 cu.m./s b) Discharge if head loss is 500mm from point 1 to 2 is 0.38 cu.m./s c) Coefficient of discharge is 0.86 A venturi meter with diameter of 300mm is attached to a 600mm main pipe and has its axis inclined downward as shown. 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

600mm diameter water 300mm diameter 02 --------- 150mm Mercury (SG = 13.6) a) Discharge if head loss is neglected is 0.44 cu.m./s b) Discharge if head loss is 500mm from point 1 to 2 is 0.38 cu.m./s c) Coefficient of discharge is 0.86 A venturi meter with diameter of 300mm is attached to a 600mm main pipe and has its axis inclined downward as shown. 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

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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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.
... 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
150mm dia. 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 Blank 1 Add your answer Blank 2 Add your answer Blank 3 Add your answer 10
- Determine the total head loss hf from A to o in U the susem shown in the figure iF the discharge is |. G0 m ls. Assume f=002 for all pipes 450 mm &, G00m qoomm &, 900m 750mmo,450m IC GO mm & ,720m D
3)a: For the figure below, find the discharge in pipe, neglect the minor losses only. (e-0.001m, D-Im, L-600m, u-1.307*10 m/sec). LAS 5m 2 1.96 D. b: In a pipe of 300 mm diameter the maximum velocity of the flow is found to be 2 m/s. If the flow in the pipe is laminar, determine: 1) The average velocity and the radius at which having the same velocity magnitude as the average velocity. 2) The velocity at 50 mm from the wall of the pipe. 5964 11.62
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
Q2) The network shown in Fig. using Hardy Cross method, find the discharge flow through cach pipe. All data of pipes in table below. Pipe No. AB ВС AC CD AD 100 L/s D(mm) 600 400 200 300 200 L (m) 300 250 250 300 250 30L/s 20 L/s 0.021 0.02 0.022 0.018 0.021 50 L/s
PROBLEM: The discharge of the pipe system shown is 420 liters/sec, Deter- mine the head loss from A to D. Assume f = 0.020 30mmo; GOO m 750 mmo; 900 250 mm d; 450 m GOo mm 6; 1200m 3 Solution 375 mma; 750 m 0 0826 10
Pipe 1 and Pipe 2 converges together flowing into Pipe 3. Pipe Discharge (LPS) Diameter (mm) 200 100 100 150 If Pipe 3 is designed for a maximum velocity of 3 m/s. what should be the nominal diameter in millimeters? The answer has a margin of 1mm from exact ansSwer.
- Dekrmine the total head loss hf. from Å to o in the systen shomwn in the figure iF the discharge is 1. G0 mls. Assume f=0:02 for all pipes 450 mm o, GO0 m 9oomm ở , 90 m 구5Dmmd,40m D GUD mm,720m
Problem 7 - 66 Determine the flow in each of the pipes shown in the figure. Assume f 0.02 for all pipes. El. 90 m El. 75 m B El. 50 m El, 30 m D. Line 3: 45um - 300mm Line 4: 900m - 150mm Line 1: 600m - 600mm Line 2: 300m - 200mm C.
Pipe 1, 2, 3, 4 and 5 have lengths and diameters of 915m of 762mm, 610m of 300mm, 450mm of 250mm,760m of 380mm, and 1200m of 600mm. Pipes 2,3,and 4 are laid in parallel, both drawing from 1 and discharging into 5.If the discharge of pipe system is 10,000,000 gpd, what is total head loss from 1 to 5. Assume C = 100 for all pipes.