I- An open tank containi ng oil Cspar.= 0.80) is acceleratd vertically at 8m/s". Defermine the pressure 3m belar the surface iF the notion is: a) upward with a k) upward with negative acceleration. c) davnward with positive acceleration di) dawnward with 'negative acceleration. positive acceleration.
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- 4. Evaluate the pressure at the center of pipe A. Given: y of Liquid 1 = 12 kN/m y of Liquid 2 = 25 kN/m. hi = 60 cm h2 = 10 cm L = 60 cm а. -750 Рa c.-650 Pa b. -800 Pa d. -700 Pa Liquid 1 Liquid 2 h, h2ay в 1ft A+ 3ft ах OIL - Sp. Gr. 0.8 3ft 4. With the same figure as Problem 3, if ax = 8.05 ft/s? and ay = 16.1 ft/s?, find the imaginary free liquid surface and the pressure at B, C, D and E. Ans. B = 0.347psi, C = 0.069psi, D= 1.109 psi, E = 0.693 psi... 2 ELEVATION 20m ELEVATION 30m AIR P ? SG-0-84 Oil flows from a tank through a 150mm diameter pipe and then discharges into air as shown. If the head loss from point 1 to point 2 is 600mm, determine the pressure needed at point 1 to cause 17L/s to flow (SG of oil = 0.84) A) 93.30 KPa B) 82.19 KPa (c) 87.74 KPa D 98.23 KPa 76.49 KPa
- i) Which of the following statements about a straight horizontal pipe of 6 inch diameter pressurized pipe carrying water is incorrect? i) The EGL and HGL are parallel to each other. ii) The friction head is equal to the loss in pressure head. iii) The velocity head gradually decreases from the beginning to end of the pipe. iv) The EGL (or) TEL is above the HGL. Answer: ii) Water flows from a 0.75 m pipe into a 1 m pipe. If losses are neglected then the 1 m diameter pipe will most likely (i) Have higher velocity than 0.75 m pipe (ii) Be at the same pressure as the 0.75 m diameter pipe (iii) Be at a higher pressure than 0.75 m pipe (iv) Be at a lower pressure than 0.75 m pipe. Answer:The compressible flow is assumed to be..?3. From d figure below, if the atmos. pressure is 770mm of Hg, fınd: a) Rm if the pressure at B is 797mm of Hg abs. b) If Rm=58mm, find the pres. at B in meters of water abs. Hg A Air Oil Sp. Gr. = 0.8 R. Water 750 mm 80 mmy +B 200 mm ....
- Homework 14 |A cylindrical vessel closed at the top and bo om is 300mm inn diameter, 1m long and contains water up to a depth of 0.8m. The air above the water surface is at a pressure of 60 KPa. If the vessel is rotated at a speed of 250n rpm about its ver cal axis, nd the pressure head at the bo om of the vessel at the center point and at the edge.3. Obtain the gage pressure at the center A of the pipe shown. Ignore surface tension effects. Given: Liquid 1 S.G. = 1.5 Liquid 2 S.G. = 3.2 hi = 15 cm h2 = 30 cm h3 = 75 cm a. 589 Pa с. 452 Ра d. -452 Pa b. -589 Рa Liquid 1 Liquid 2 X1 h,An inclined tank contains three different liquids A, B, and C with specific gravities of 0.40, 1.25, and 11.73, respectively. What will be the pressure in psi on the bottom of the tank if the liquid surfaces are at the elevations shown? El of point T = 35' El of point A = 12' El of point B= 3' C 8 El. = A El.= T EI. 60° h₁ = 35 h₂= 12 hg= 3 Please Solve Correctly and double check final Answers. Civil Engineering: Hydraulics
- 1.1 AN SPECIFIC ACTING VERTICALLY OPEN CUBICAL WEIGHT ON IN THE 8 KN/m3 SIDE UPWARD TANK OF UP A AND WITH To A A TANK DOWNWARD BIDE OF DEPTH OF WHEN 1.8m 1.8m IT IS PIRECTIONS. CONTAINS DETERMINE ACCELERATEO OIL WITH THE 9/3 m/s² FORCE A2. An oil is flowing between two parallel horizontal plates which are 20 mm apart. The top plate is moving with a uniform speed 0.1 m/s. The viscosity of the oil is 0.1 N.s/m². The velocity at the centerline is 1.95 m/s. Consider the flow to be a fully developed one. a) Derive the velocity profile b) Calculate pressure difference between two points (Pi-P2) 5 m apart c) Find the velocity at 3 mm from the wall of the bottom plates. d) Find the velocity at 3 mm from the wall of the top plates. e) Determine force acting on the bottom wall, (W=10 cm) 0.1 m/s Oil P1 P2 2 cm y 5 mFlow Between pipes A viscos flow is taking place b/w the two horizontal parallel fixed plates which are 80mm apart. The maximum velocity is 1.5 m/s and dynamic viscosity of oil is 1.962 N-s/m². The magnitude of pressure gradient in kPa/m is