Q3-In altitude 1220meter and temperature (10°C) with minimum netpositive suction head of pump 2.5m and flow rate 0. 5m3/sec in 200mm flowdiameter. Find the minimum suction head (Z)Altitude (m) 03054576101220 1830 2439Pressure(KPA)101989694888175Temperature (°C) 04.4 10 15.6Vapor pressure 0.61 0.86 1.23 1.76Кра222.51521.126.732.2 37.83.54.81 6.54

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Answered: Q3-In altitude 1220meter and…

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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Chow, Ven Te, Handbook of Applied Hydrology, McGraw-Hill, 1964. FRICTION FACTOR f 08 07 Find the Q and V at the exit. Include friction losses (e.g., REAL fluid case) but ignore minor losses. Absolute Roughness e = 1.5 mm (See Moody Diagram next sheet) FE Manual Moody Diagram 06 .05 .04 03 02 01 0.1 0.2 CLAMINAR CRITICAL FLOW ZONE LAMINAR FLOW f-64/Re 0.4 0.6 0.8 1 6 8 10³ 2 TRANSITION ZONE CRITICAL Re 2 GLASS, DRAWN BRASS, COPPER, LEAD COMMERCIAL STEEL, WROUGHT IRON ASPHALTED CAST IRON GALVANIZED IRON CAST IRON CONCRETE RIVETED STEEL -0.03 CORRUGATED METAL PIPE -0.2 LARGE TUNNEL, CONCRETE OR STEEL LINED 0.002 -0.004 BLASTED ROCK TUNNEL 1.0 <-2.0 4 6 8 10 ZIN FI SMOOTH 410.0 feet 0.003 0.1 0.0001 -0.0003 0.0002 -0.0006 0.0002 -0.0008 0.0006 -0.003 0.001 -0.01 2 8" Dia. VALUE OF VD FOR WATER AT 60°F (V IN FPS, DIN INCHES) 4 6 8 10 2 4 6 8 10² 2 4 6 8 10³ 50' COMPLETE TURBULENCE ROUGH PIPES SMOOTH PIPES 4 6 8 105 2 4 6 8 10⁰ VD REYNOLDS NUMBER Re= V 2 3 00002 00001 6 8 10 372.5 feet 2 4 6…
Oil flows at 62 L/s in a pipe of 175mm diameter and 50m length. SG of oil is 0.9 and viscosity is 0.04 Pa-sec. If head loss is 5.22m, determine: a) Mean velocity of flow = [ Select ] m/s b) Type of flow = [ Select ] %3D c) Friction factor = [ Select ] d) Velocity at the centerline of pipe = [ Select ] v m/s e) The shear stress at the wall of the pipe [ Select ] Ра %3D
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)
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the unknown fluid? Express your answer in Ib/ft³. TEST 1 Fall 2021 5. For the configuration shown in the figure below what must be the value of the unit weight of the upkontiguration shown in the fiqure below what must be the value of the unit weight of ie unknown fluid? Express your answer in Ib/t. [Max. 10 Points] Open Water 49 in 5.5 in 3.3in JAknown 1.4tin
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"
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The discharge of a liquid of kinematic viscosity 4 x 10-2 m²/s through a 80 mm diameter pipe is 3200 x 10-4 m³/s. The flow is
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A venturi meter with a throat diameter of 100 mm is fitted in the inclined pipeline of 200 mm diameter with oil of specific gravity 0.88 flowing upwards. The venturi meter coefficient is 0.96. Two pressure gauges are fitted at tapping points, one at the throat reads the vacuum pressure of 40 cm of mercury and the other in the inlet pipe 320 mm below the throat is 20.231 N/cm2. If the loss of head in the main and throat is 0.35 times the kinetic head of the pipe, determine2.1 the volume flow rate of oil through the pipe2.2 the difference in level in the two limbs of the mercury manometer if it is connected to the tapping points and connecting pipes are filled with the same oil
b.) What is the specific gravity of the gage fluid if h₂ = 0.5 m and pA - PB = 2.9 kPa 0.5 Flow n. (2)- Flow nozzle -(4)-(5) -(3) %2 '71 M₁ = We

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