Structural Analysis
6th Edition
ISBN: 9781337630931
Author: KASSIMALI, Aslam.
Publisher: Cengage,
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- A Venturi tube will be used to measure the flow speed in a river. The instrument is shown in the figure. V1, Patm V2, P2 The Venturi tube has a limit of operation. This limit regards to the fact that pressure p2 cannot drop too much below the atmospheric pressure because the water will boil. With a normal temperature (i.e. 20 °C), the water will evaporate with a pressure below 20340 [Pa] (while the atmospheric pressure is Patm 101000 Pa or 1010 hPa). Determine the maximum velocity v₁ which can be measure by a Venturi tube in which A1/A2=2 (i.e. ratio of area at the entrance over the constriction). Help: Specify the atmospheric pressure as an absolute pressure of Patm-101000 Pa (i.e. do not use Patm=0) Note: The evaporation of water inside pipes with fast flows is a recurrent problem in hydraulics. This phenomenon is called cavitation.arrow_forwardI need the answer as soon as possiblearrow_forwardA U-tube manometer is arranged, as shown in Fig. 2.15, to measure the pressure difference between two points A and B in a pipeline conveying water of density 1000 kg/m³. The density of the manometric liquid Q is 13600 kg/m³ and point B is 0.3 m higher than point A. Calculate the pressure difference when h = 0.7 m. T Manometric liquid Q of density Pman Figure 2.15 Measurement of pressure difference Fluid P, of density blup all to 20 lensarrow_forward
- Gasoline flows steadily downward through the pipe shown in the figure below. Viscous effects are negligible, and the pressure gage indicates the pressure is zero at point (1). Determine (a) the flowrate and (b) the pressure at point (2). (a) Q = (b) p2 = 2.0ft 3.5ft 18 -0.12 ft -0.1 ft -free jet ft³/s lb/ft²arrow_forwardProblem 10.56 The 100-mm-diameter commercial steel pipe discharges water at 25°C through the 40-mm-diameter nozzle. (Figure 1) Figure 40 mm g 60e 3m A 100 mm 1 of 1 Part A If the pressure at A is 250 kPa, determine the discharge. The minor loss coefficient of the nozzle is KL = 0.15. Express your answer to three significant figures and include the appropriate units. Q= Submit OL μА Value Provide Feedback Request Answer Units ? (v 5 of 6 Review Next >arrow_forward4- Consider the system shown in the figure. If a change of P kPa in the pressure of air causes the brine- mercury interface in the right column to drop by d mm in the brine level in the right column while the pressure in the brine pipe remains constant, determine the ratio of A₂/A₁. P (kPa) d (mm) 6 Sum of last 2 digits of 35 YorkU ID# ending with 0, 2, 4, 6, 8 Sum of last 2 digits of 45 YorkU ID# ending with 1, 3,5,7,9 7 Area, A₁. Air Water Mercury SG = 13.56 Brine pipe SG = 1.1 Area, A₂arrow_forward
- b) Two pipes (at points A and B) have been connected with the manometer as shown in Figure Q1. i) Determine the pressure at point B if the pressure at point A is 10 kPa. ii) If pipe at point B is not connected with the pipe and open to the atmosphere, what happens to the current manometer? A. B. 0.3 m Water Spesific Weight for Air = 11.43 N/m³ 3 m Oil (sg = 0.86) Figure Q1: Compound manometerarrow_forwardE9arrow_forward11. Please answer no. 11 thank you!arrow_forward
- Two pressure tanks are built one inside the other as shown in the figure. A Bourdon gauge M is connected to the inner tank reads 20 kPa. Another Bourdon gauge N connected to the M outer tank reads 35 kPa. An aneroid barometer reads 750 mm of mercury. Calculate the absolute pressure recorded at Mand N mm in of mercury.arrow_forward(Bernoulli/continuity/Pitot tube) Two Pitot tubes and two static pressure taps are placed in the pipe contraction shown in the figure below. The flowing fluid is water, and viscous effects are negligible. Determine the two manometer readings, h and H. V=1.7 ft/s h = H= 6.4 in. Air ↓ SG= 1.10 ft ft TH 3.8 in.arrow_forwardQ-4 Define coeffecient of velocity, coefficient of discharge, coefficient of contraction. An oil of sp. gr. 0.8 is flowing through a venturimeter having inlet diameter 30 cm and throat diameter 15 cm and the oil- mercury differential manometer shown a reading of 25 cm. Calculate the discharge of oil through the horizontal venturimeter. Take C₁ = 0.98.arrow_forward
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