Conical plate (120o) a) The apparatus were set as shown in figure 2 using a conical plate b) The procedure in A above was repeated C. Hemispherical cup (180) a) The apparatus were set as shown in figure 2 using a hemispherical plate b) The procedure in A above was repeated Results and Calculations Diameter of nozzle, D = 10.0 mm. Cross sectional area of nozzle, A =πD2 /4 = 78.5 mm2 Implying A= 7.85×10−5m2 Height of vane above nozzle tip s = 35 mm = 0.035 m Distance from centre of vane to pivot of lever L= 150 mm= 0.
15m Mass of jockey weight, M = 0.600 kg Weight of jockey weight, W = Mg = 0.600×9.81 = 5.89 N When the jockey weight is moved a distance y mm from its zero position, the force F on the vane which is required to restore balance is given by: F×150 = W×y Inserting the value of W, namely 5.89 N, gives589×y F=.or F = 0.03924 y N/150 The mass flow rate m in the jet is found by timing the collection of a known mass of water. The velocity u1 of the jet as it leaves the nozzle is found from the volumetric flow rate Q and the cross sectional area A of the nozzle.
The velocity u0 with which the jet strikes the vane is slightly less than u1because of the deceleration due to gravity. This effect may be calculated from the expression Inserting the value s = 0.035 m leads to the result Recorded values of quantity collected, measured time, and jockey displacement y are presented in tables together with the ensuing calculations below. Mass flow rate is computed by the total mass divided by the time taken as shown below in an illustration. M= weight/time Eg M=5/28.
6 kg/s This was used for volumetric computations Volumetric flow rate Q is mass flow rate divided by the density, which is 1000 kg/m3 for water. Q=m/1000 m3/s Table 2: Results for the flat plate, conical and cup vane Volume (L) Time (s) Y (m) W (kg) m (kg/s u (m/s) uo (m/s) muo (N) Force (N) cup 5 28.6 0.141 0.6 0.174825175 #REF! #REF! #REF! 5.535096 cup 5 39.32 0.107 0.6 0.12716175 #REF! #REF! #REF! 4.200392 cup 5 45.46 0.093 0.6 0.109986802 #REF! #REF! #REF! 3.650808 cup 15 196.81 0.05 0.6 0.
076215639 #REF! #REF! #REF! 1.9628 Flat 15 65.72 0.087 0.6 0.228241023 #REF! #REF! #REF! 3.415272 Flat 15 75.85 0.034 0.6 0.197758734 #REF! #REF! #REF! 1.334704 Flat 5 165.97 0.018 0.6 0.030125926 #REF! #REF! #REF! 0.706608 Flat 5 190.45 0.015 0.6 0.02625361 #REF! #REF! #REF! 0.58884 Conical 15 68 0.114 0.6 0.220588235 #REF! #REF! #REF! 4.475184 Conical 15 88.56 0.092 0.6 0.169376694 #REF! #REF! #REF! 3.611552 Conical 15 103.74 0.069 0.6 0.14459225 #REF! #REF! #REF! 2.708664 Conical 15 111.44 0.035 0.6 0.
134601579 #REF! #REF! #REF! 1.37396 A comparative plot for the flat plate (90o), conical plate (120o) and the hemispherical cup (180o) is as shown below Figure1: The experimental result for jet impact at different angles. The figure shows a highest jet impact at 180o and lowest impact at 90o. Taking into account that the flat plate represents 90 degrees of exit, conical plate 120 and the cup 180 degrees of momentum, the comparison between the experimental results and the ideal results was as shown in the tables below.
A comparison between experimental and ideal jet impact for 90, 120 and 180 degrees Figure2: Comparison between experimental and ideal result for jet impact at 90o Figure 3: Comparison between experimental and ideal result for jet impact at 120o Figure 4: Comparison between experimental and ideal result for jet impact at 180o Discussion From the comparative results, it can be seen that highest impact for a given rate of delivery of momentum by the change occurs at 180o. This can be explained mathematically using the approaches below Thus taking to the beta approach and taking into account that beta is the cosine of the angle of deflection, then from the equation above for F, it can be shown/seen that F is maximum for a maximum –ve β1.
This is at 180 degrees where β1= -1 hence the force being at the maximum. The force reduces as β1 becomes more positive.
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