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- Q. Determine the kinematic viscosity at the average temperature and determine the Reynolds number and type of flow using the data shown below and table values: Data obatined from a Reynolds Number test: Water temperature at the beginning of the experiment = 25 oC Water temperature at the end of the experiment = 30 oC The Volume of water collected in 25 seconds = 240 ml Pipe diameter, d= 10 mm. (use eq'n reynold's number, Re = VD/vA flow rate measuring device is installed in a horizontal pipe through which water is flowing. A U-tube manometer is connected to the pipe through pressure taps located 3 in. on either side of the device. The gage fluid in the manometer has a specific weight of 112 lb/ft3. Determine the differential reading of the manometer corresponding to a pressure drop between the taps of 0.5 lb/in². h = ftQ1) Mott recommends the following formula for the friction head loss hf, for flow through a pipe of length L and diameter D : where Q is the volume flow rate , A is the pipe cross-section area , and Ch is a dimensionless coefficient . Determine the dimensions of hf? hf = LG *0.551. A. Ch. Do.63)1.85
- Q3: A pitot-static tube is used to measure the flow velocity of turpentine flowing in a pipeline if the manometer reading is 8 cm of mercury, calculate the average velocity, pressure drop, and volumetric flow rate at that point in the pipe line. Also evaluate Reynold number for turpentine and which type of flow in the pipe. Ph J Re Density of turpentine is 850 kg/m³, density of mercury is 13600 kg/m³, cv = 1, D=10 cm, turpentine 0.001375 and 0 = 45°. =A calibration test of a 12.5 mm diameter circular sharped-edged orifice in a vertical side of a large tank showed a discharge of 590 N of water in 81 seconds at a constant head of 4.70 m. Measurement of the jet showed that it traveled 2.35 m horizontally while dropping 300 mm a. Compute the coefficient of velocity. b. Compute the coefficient of discharge. c. Compute the coefficient of contraction. URGENT Please answer this problem in 30minutes. I need correct answers with complete and step by step solution. Box the final answers. Do not shortcut your solution. I will give an upvote if it satisfies. Thank you!The pressure drop in a Venturi meter varies only with the fluid density, pipe approach velocity, and the diameter ratio of the meter. A model Venturi meter tested in water at 20 ?C shows a 5-kPa drop when the approach velocity is 4 m/s. A geometrically similar prototype meter is used to measure 680 kg/m3) at 20 ?C and a flow rate of 9 m3/min. If the prototype pressure gage is most accurate at 15-kPa, what should the upstream pipe diameter be? gasoline (? =
- SITUATION 4. AN OIL WITH SG = 0.86 FLOWS THROUGH A PIPE 30in. IN DIAMETER AT 700gpm 5. Determine the average velocity in m/sec. Your answer 6. Determine the average flowrate in ft3/sec. Your answerWhile using Darcy-Weisbach equation for estimating head loss in a pipe flow, the friction factor was misjudged by -15%. For this case, the error in estimating the discharge isComplete solution please. 3DECIMALS thank you Determine the head loss in feet in PIPE 1 Determine the head loss in feet in PIPE 5 Determine the velocity of flow in the lower branch, PIPE 3, in feet per second. Determine the velocity of flow in the upper branch, PIPE 2, in feet per second. Determine the velocity of flow in the lower branch, PIPE 4, in feet per second. Determine the head loss in feet in PIPE 2. Determine the head loss in feet in PIPE 3. Determine the head loss in feet in PIPE 4. Determine the total head loss in feet between the inlet A and the outlet B.
- Refer to the illustration below. All friction factor f = 0.02 All pipe lengths L 200m %3D Diameter of Pipe A = 400mm Diameter of Pipe B = 300mm Diameter of Pipe C = 200mm Diameter of Pipe D = 400mm Flow Rate at Pipe A = 300 L/s Solve for the following: 1. Headloss in meters at Pipe A 2. Flow rate in L/s at Pipe B 3. Flow rate in L/s at Pipe C 4. Flow rate in L/s at Pipe D 5. Headloss in meters at Pipe B 6. Headloss in meters at Pipe C 7. Headloss in meters at Pipe D 8. Difference in elevation between reservoirs in metersQsn. Plot the flow curve of liquid limit according to the data given in the table.A differential "U"-tube manometer containing mercury of density 13000 kg/m³ is used to measure the pressure drop along a horizontal pipe. If the fluid in the pipe is water and the manometer reading is 0.65m, what is the pressure difference between the two tapping points? Fluid density Pw A B a b datum Manometric fluid density p Hg Figure of manometer setup