lab 5-6 civi 381

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Dec 6, 2023

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EXPERIMENT 5: Flow through a Horizontal Contraction EXPERIMENT 6 : Flow through a Horizontal Expansion Date of submission : October 30, 2022
INTRODUCTION When we evaluate flow that goes inside a horizontal contraction or expansion we often use the continuity, energy and momentum equations. In this experiment we will consider the cross section 1 (CS1) and throat cross section (CST). The objectives of this experiment are : validate the energy relationship and to draw the total energy gradient line and the hydraulic gradient line. DESCRIPTION EXPERIMENTAL METHODS In this experiment we got to let the flow in the flume and we have to keepthe flow depth around 12 inches. We have to pivot down the tailgate at the downstream to finish the flume in the experiment 5. But for experiment 6, we have to pivot in the up direction the downstream tailgate. Also, we have to take note of the flow depth, the discharge, the depth at the throat and the downstream depth. OBSERVATIONS Table 1 : general values Length of the contraction (L 1 ) (m) 0.208 Length of the expansion (L 2 ) (m) 0.632 Length of the contraction/expansion transition (L) (m) 0.840 Flume width (B 1 ) (m) 0.313 Throat width (B t ) (m) 0.155 Table 2 : Experiment 5 Run 1 Run 2 Run 3 Discharge (Q) (m 3 /s) 0.0151 0.0212 0.0269 Initial reading of depth gauge at CS1 (y 1i ) (m) 0 0 0
Final reading at CS1 (y 1f ) (m) 0.141 0.177 0.208 Flow depth at CS1 (y 1 ) (m) 0.141 0.177 0.208 Initial reading of depth gauge at CST (y ti ) (m) 0 0 0 Final reading at CST (y tf ) (m) 0.882 0.400 0.136 Flow depth at CST (y t ) (m) 0.882 0.400 0.136 Initial reading of depth gauge at CS2 (y 2i ) (m) 0 0 0 Final reading at CS2 (y 2f ) (m) 0.346 0.406 0.447 Flow depth at CS2 (y 2 ) (m) 0.346 0.406 0.447 Stagnation pressure head (cm) 21.6 26.4 29.56 Static pressure head (cm) 10.6 11.1 11.9 Table 3: Experiment 6 Run 1 Run 2 Run 3 Discharge (Q) (m 3 /s) 0.0268 0.0216 0.0103 Initial reading of depth gauge at CS1 (y 1i ) (m) 0 0 0 Final reading at CS1 (y 1f ) (m) 0.207 0.180 0.146 Flow depth at CS1 (y 1 ) (m) 0.207 0.180 0.146 Initial reading of depth gauge at CST (y ti ) (m) 0 0 0 Final reading at CST (y tf ) (m) 0.133 0.116 0.106 Flow depth at CST (y t ) (m) 0.133 0.116 0.106 Initial reading of depth gauge at CS2 (y 2i ) (m) 0 0 0 Final reading at CS2 (y 2f ) (m) 0.142 0.119 0.132 Flow depth at CS2 (y 2 ) (m) 0.142 0.119 0.132 Sample calculations Continuity : B 1 v 1 y 1 = B t v t y t = B t v c y c Energy : y + z + 𝑣1 2 = y + z + 𝑣? 2 1 1 2? t t 2?
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Momentum : 0.5*B 1 y*y 1 ^2 - 0.5*B t y*y t ^2 - F w = Qp*(v t – v 1 )
Flow velocity : v = ?? ? Discharge per unit width : q = √?? 3 Experiment 6 run #1 q = (Q/B t ) = (0.0268/0.155) = 0.173 m^3/s V 1 = (Q/B 1 *y 1 ) = (0.0268/(0.313*0.207) = 0.414 m/s Vt = (Q/B t *yt) = (0.0286/(0.155*0.133) = 1.300 m/s V 2 = (Q/B 1 *y 2 ) = (0.0268/(0.313*0.142) = 0.603m/s E1 = y1 + v1^2/(2*g) = (0.207 m) + (0.414^2)/(2.9.81) = 0.216 m Et = yt + vt^2/(2*g) = (0.133 m) + (1.300^2)/(2*9.81) = 0.219 m E2 = y2 + v2^2/(2*g) = (0.142 m) + (0.603^2)/(2*9.81) = 0.203 m Yt = yc Yt theory = ((q^2)/(9.81))^(1/3) = ((0.173^2)/9.81))^(1/3) = 0.145 m ?
Difference with Yt experimental 0.145 – 0.133 = 0.012 In % = 0.012/0.145 = 8.26% Fw = 0.5*B 1 y*y 1 ^2 - 0.5*B t y*y t ^2 - Qp*(v t – v 1 ) = (0.5*(0.313*9810*(0.207^2)) – (0.5*9810*(0.133^2)) – (0.0268*1000*(1.300-0.414) = 28.58 N Table 4 : Calculations of given table (see excel sheet for details
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DISCUSSION a) Table 5 : Evaluation of Yt (exp) and Yt (theory) Variable Experiment 5 Experiment 6 Run #1 #2 #3 #1 #2 #3 q (m^3/s) 0.097 0.137 0.174 0.173 0.139 0.066 Yt (experimental) (m) 0.882 0.400 0.136 0.133 0.116 0.106 Yt(theory) (m) 0.099 0.124 0.145 0.145 0.126 0.077 difference (m) 0.783 0.276 0.009 0.012 0.010 0.029 difference in % 88.79 69.00 6.43 8.26 7.62 27.70 b) In experiment 5, the difference in % of the Yt theory and experimental are 88.79% for run 1, 69% for run 2 and 6.43% for run 3. In experiment 6, the difference in % of the Yt theory and experimental are 8.26% for run 1, 7.62% for run 2 and 27.70% for run 3. We see the huge differences in percentage specially for run 1 and 2 for experiment 5 and run 3 of experiment 6. These differences can be due of wrong gauges used or human error such as someone not reading the manometer properly.
c) Figure 1 : experiment 5 Figure 2 : experiment 6 Experiment 5 1 0.9 0.8 0.7 0.6 Yc line 0.5 0.4 Total energy line water surface profile 0.3 0.2 0.1 0 0.0000.2000.400 E (m) 0.600 0.800 1.000 0.250 0.200 0.150 E (m) 0.100 0.050 0 0.000 0.05 Yc line total energy line water surface profile 0.15 0.1 0.2 0.25 Experiment 6 y (m) y (m)
d) Table 6 : Values of Fw Variable Experiment 5 Experiment 6 Run #1 #2 #3 #1 #2 #3 Fw (N) -557.41 -72.68 29.15 28.58 21.84 20.05 We can see huge values and negatif values for run 1 and run 2 for experiment 5. These were probably cause by human error. e) With table number 2 we can see that the more the stagnation pressure head is high (run 1 : 21.6 run 2: 26.4 run 3 : 29.56) the v2 is going to be higher (0.139 , 0.167 and 0.192). CONCLUSION To conclude, all the objectives were made, we verified the energy equation and we drew the total energy gradient and hydraulic gradient line.
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REFERENCES Civi lab manual