FACULTY OF ENGINEERING TECHNOLOGY DEPARTMENT OF CIVIL TECHNOLOGY ENGINEERING COURSE CODE BNP 10303 COURSE NAME FLUID MECHANIC LABORATORY TITLE Flow Through Orifice with Hydraulic Bench 1. AFIQ AFZAL BIN AB SOBI (CN240385) 2. MUHAMMAD HARRIS SHAZWAN BIN ROSMAINOOR (CN240297) 3. NURSHAMIRA BINTI ZAKARIA (CN240153) 4. NUR SYAHMINA BINTI ABDUL GROUP MEMBERS MALEK(CN240166) SECTION 1 SEMESTER 2024/2025 LECTURER’S NAME DR. NUR AINI BINTI MOHD ARISH @ ARSHAD DATE OF SUBMIT 28/05/2025 1 STUDENT CODE OF ETHICS FACULTY OF ENGINEERING TECHNOLOGY DEPARTMENT OF CIVIL ENGINEERING TECHNOLOGY I hereby declare that I have prepared this report with my own efforts. I also admit to not accept or provide any assistance in preparing this report and anything that is in it is true. 1) Group Leader Name: Afiq Afzal Bin Ab Sobi Matrix No. : CN240385 Signature: 2) Group Member 1 Name: Muhammad Harris Shazwan Bin Rosmainoor Matrix No. : CN240297 Signature: 3) Group Member 2 Name: Nurshamira Binti Zakaria Matrix No. : CN240153 Signature: 4) Group Member 3 Name: Nur Syahmina Binti Abdul Malek Matrix No. : CN240116 Signature: 2 Assessment PO SK Rubric elements Criteria Subcriteria SP Description of the labwork: objective and introduction SK3 Explanation of principles and theories Perform labwork with correct procedure and equipment Level 0 SK4 Excellent Good Weight Score Comprehensive description 5 0.6 3 2 3 P1 Lackor not related description Minimal description Some description shown P2 Equipment or procedurenot shown Incorrect equipment or procedureshown Correct equipment but procedure briefly shown Correct equipment and adequate procedureshown Correct equipment and comprehensive procedureshown 5 0.6 3 Lack of data collection and no calculation shown Complete data collection but no calculation shown Complete data collection but incorrectcalculation shown Complete data collection and correct calculation Complete and correct data collection and calculation 5 0.4 2 Not concluding the whole report Minimalconclusion of the whole report Someconclusion of the report shown Adequateconclusion of the whole report Conciseconclusion of the whole report 5 0.4 2 Correct and precise data collection: results and calculation PLO4 (Investigation) Conduct investigations of broadly-defined problems; locate, search and select relevant data from codes, databases, and literature, design andconduct experiments to provide valid conclusions. 4 Rate Adequate description shown 5 SP1 Show thecorrect equipment and procedure Labwork (Written report) 1 Fair SP4) Poor Demonstrate standard measurement techniques of fluid mechanics and their applications in order to solve fluid mechanics problems. (LOD4, PLO4, P5) (SK3, SK4, SK8) (SP1, SP3, V.Poor CLO3: No Participation Report Assessment Rubrics Data collection, analysis, and conclusion SP3 P3 Concise conclusion Discussion of the result, analysis, and conclusion None at all SK8 Demonstration of analysis using related relevant data from codes, databases, and literature. Analyse and discuss the data trends using correct graphs SP4 P4 Incorrect analyses and discussion Correctanalyses with minimal discussion Correct analyses withsome discussion Correct analyses with adequate discussion Correct analyses with comprehensive discussion 5 0.4 2 SK3 Appraisal of the suitable and efficient solutions. Solve the question with correct answers and discussions SP4 P4 Incorrect answers and discussion Correctanswers with minimal discussion Correct answers with some discussion Correct answers with adequate discussion Correct answers with comprehensive discussion 5 0.4 2 SK1 Selection of suitable analytical techniques. Adapt to the correct used of equipment and measurement technique Incorrect equipment and measurement technique used Correct equipment used but minimal measurement technique shown Correct equipment used with average measurement technique shown Correct equipment used with adequate measurement technique shown Correct equipment used with well-versed measurement technique shown 5 0.6 3 Incorrect procedure shown with lack of understanding Correct procedure shown but minimal understanding Correct procedure shown with average understanding Correct procedure shown with adequate understanding Correct procedure shown with enthusiasam and wellversed understanding 5 0.6 3 Adapt appropriate method and solutions relate to the labwork Labwork (pratical) SK3 Well-versed with the correct and safe operational procedures SP3 Adapt to the correct procedure P5 Total(%) 3 20.0 TABLE OF CONTENT CONTENT PAGE 1.0 Objective 2.0 Learning Outcomes 3.0 Theory 5-7 4.0 Equipment 8-9 5.0 Procedure 10-13 6.0 Result and Calculation 14-19 7.0 Discussion 20-26 8.0 Conclusion 27 9.0 Reference 28 4 1.0 OBJECTIVE 1. To To study the trajectory of a water jet issuing from an orifice. 2. To determine the flow characteristics through a small orifice. 3. To calculate the coefficient of discharge (CdC dCd) of the orifice. 4. To compare theoretical and actual discharges. 2. 0 LEARNING OUTCOMES At the end of the course, students should be able to apply the knowledge and skills they have learned to: 1. Understand the characteristics of different orifices. 2. Understand the concept of contraction of the stream and energy loss. 3. Understand the factors which influence the flow through orifice. 3. 0 THEORY An orifice is an opening, of any size or shape, in a pipe or at the bottom or side wall of a container (water tank, reservoir, etc.), through which fluid is discharged. If the geometric properties of the orifice and the inherent properties of the fluid are known, the orifice can be used to measure flow rates. Flow measurement by an orifice is based on the application of Bernoulli’s equation, which states that a relationship exists between the pressure of the fluid and its velocity. The flow velocity and discharge calculated based on the Bernoulli’s equation should be corrected to include the effects of energy loss and viscosity. Therefore, for accurate results, the coefficient of velocity (Cv) and the coefficient of discharge (Cd) should be calculated for an orifice. This experiment is being conducted to calibrate the coefficients of the given orifices in the lab. Bernoulli's Theorem applied between the water surface and orifice yields the theoretical velocity: Vth 2gh Where: Vth = theoretical velocity g = 9.81 m/s 5 h = head of water above the orifice centre Theoretical Discharge: Qth A 2gh Where is the area of the orifice. Actual Discharge: Qact v Where V is the volume of water collected and t is the time. t Coefficient of Discharge (Cd): Cd Qact Qth Cd accounts for energy losses due to viscosity, friction, and contraction. Flow Through Orifices and Nozzles Drawing (a) shows fluid streaming through a smoothly contracting nozzle, making a parallel jet. The overall increase in speed through the contraction reduces non uniformity in the approaching flow, so the fluid velocity should be uniform across the emerging jet. The cross-sectional area of the jet is the same as that of the nozzle, so the flow rate is the product of the jet velocity and the nozzle area. In drawings (b) and (c) however, the fluid does not emerge as a convergent stream, so the cross-sectional area of the jet reduces to a contracted section or ‘vena contracta’. Over this section the streamlines are parallel and velocity is effectively uniform. The flow rate is the product of the jet velocity and area of the contracted section. Figure 3.1: Examples of jet flows from nozzles and orifices Jet Trajectory: Water issuing horizontally from an orifice under pressure forms a parabolic trajectory. The horizontal range x and vertical drop y relate to velocity v and height h by: v 2 gh 6 t Time of flight t is: 2y g Horizontal distance x : x vt v 2y g Flow Through an Orifice: Theoretical discharge: Qtheoretical A 2gH Actual discharge Qactual measured by collecting volume over time. Coefficient of discharge: Qd Qactual Qtheoretical 7 4.0 EQUIPMENT EQUIPMENT PICTURES Orifice apparatus with hydraulic bench Stop watch 8 Orifice 1 : Length 15mm, with 60° contraction and 60° diverging section Orifice Vernier Clipper 9 5.0 PROCEDURE 1. The water was filled into the three sump tanks to 3/4 height. Figure 5.1: Filling Water into the Sump Tank 2. All the valves were opened before starting the experiment. 3. The main switch on the control box was switched on. Figure 5.2: Switching on the Control Box 4. The water supply hose was connected to the Flow Through Orifice Tank inlet port. 5. It was ensured that the overflow port was connected with a hose and the hose was placed in the volumetric tank. 10 6. The orifice plate to be tested was placed at the base of the apparatus tank. 7. The pump was switched on and water was allowed to flow into the orifice tank. Figure 5.5: Adjusting Flow and Overflow 8. The flow was adjusted and allowed to pass over the overflow pipe. 9. The Pitot tube was adjusted and placed at the center of the outlet flow from the orifice plate. 10. Water was allowed to flow for around 3 to 4 minutes. It was ensured that no bubbles were present in the manometer tubing. Figure 5.6: Positioning the Pitot Tube 11. The water level of the tank height was recorded as Ho. 11 Figuire 5.5 : Recording tank levels Ho 12. The water level of the Pitot tube was recorded as Hc. Figure 5.6 : Recording pilot tube lebel Hc 13. The diameter of the existing water jet (dc) was measured using the provided caliper. Figure 5.8: Measuring Water Jet Diameter 12 14. All the recorded data was filled into the table below. 15. The experiment was repeated with different flow rates. 16. The experiment was also conducted with different orifice plates. 13 6.0 RESULTS, CALCULATION AND DATA COLLECTION CALCULATION 14 15 16 RESULT ORIFICE 1 Volu me (liters ) Tim e (sec ) Tank Heig ht, 𝐻𝑜 (mm) Pitot Tube Heig ht, 𝐻𝑐 (mm) Orifice Diamet er, 𝐷𝑜 (mm) Existin g Water Diamet er, 𝐷𝑐 (mm) 10 46.2 4 40.7 6 23.9 2 110 116 29.7 14.0 Experim Theoreti Coeffici ent cal ent of Flowrate Flowrate Velocity, , , 𝐶𝑣 𝑄𝑒𝑥𝑝 𝑄𝑡ℎ𝑒𝑜 (𝑚3 /𝑠) (𝑚3 /𝑠) (𝑥10−4 ) (𝑥10−4 ) 2.163 2.351 1.027 154 156 29.7 14.2 2.453 2.635 230 230 29.7 14.8 4.181 2.825 10 10 17 Coefficie nt of Contracti on, 𝐶𝑐 Discharg e Coefficie nt, 𝐶𝑑 0.896 0.920 1.006 0.925 0.931 1.000 1.480 1.480 ORIFICE 2 Volu me (liters ) Tim e (se c) Tank Heig ht, 𝐻𝑜 (mm) Pitot Tube Heig ht, 𝐻𝑐 (mm) Orifice Diame ter, 𝐷𝑜 (mm) 10 46. 59 41. 00 19. 01 160 162 201 231 10 10 Experim ent Flowrat e, 𝑄𝑒𝑥𝑝 (𝑚3 /𝑠) (𝑥10−4 ) 2.146 Theoret ical Flowrat e, 𝑄𝑡ℎ𝑒𝑜 (𝑚3 /𝑠) (𝑥10−4 ) 2.351 Coeffici ent of Velocity , 𝐶𝑣 Coefficie nt of Contract ion, 𝐶𝑐 Dischar ge Coeffici ent, 𝐶𝑑 30.0 Existin g Water Diame ter, 𝐷𝑐 (mm) 11.3 1.006 0.908 0.913 210 30.0 12.0 2.439 2.635 1.022 0.906 0.926 231 30.0 12.4 5.260 2.825 1.024 1.818 1.862 Calculation Example: 1. Experimental Flowrate, 𝑄𝑒𝑥𝑝 = Volume= 10ℓ x 𝑉𝑜𝑙𝑢𝑚𝑒,𝑚 3 𝑇𝑖𝑚𝑒,𝑠 0.001𝑚 3 1ℓ Volume= 0.01𝑚3 0.01𝑚 3 𝑄𝑒𝑥𝑝 = 46.24𝑠 𝑄𝑒𝑥𝑝 =2.163𝑥10−4 𝐴 2. Theoretical Flowrate,𝑄𝑡ℎ𝑒𝑜 = 𝑜√2𝑔ℎ 𝜋(13𝑥10−3 )2 𝐴𝑜 = 4 𝐴𝑜 = 1.327𝑥10−4 𝑚2 𝑄𝑡ℎ𝑒𝑜= 1.327𝑥10 −4𝑚2 √(2)(9.81)(0.11) 𝑄𝑡ℎ𝑒𝑜= 1.949𝑥10−4 𝑚3 /𝑠 18 𝐻 3. Coefficient of Velocity, 𝐶𝑣 =√𝐻𝑐 𝑜 116 𝐶𝑣 =√110 𝐶𝑣 =√1.055 5. Coefficient of Contraction,𝐶𝑐 𝐶𝑣 =1.006 𝑄 4. Discharge Coefficient,𝐶𝑑 = 𝑄 𝑒𝑥𝑝 𝑡ℎ𝑒𝑜 2.163𝑥10−4 𝐶𝑑 =2.351𝑥10−4 𝐶𝑑 =0.920 𝐶 = 𝐶𝑑 𝑣 0.920 𝐶𝑐 =1.027 𝐶𝑐 =0.896 19 7.0 DISCUSSION 1. Compare the calculated result between theoretical flow rate and the experimental flow rate In the experiment conducted using the hydraulic bench a clear comparison was made between theoretical and experimental flow rates for different tank heights and orifice configurations. For example, in one trial using Orifice 1 with a tank height of 110 mm the experimental flow rate was 2.163 L/min while the theoretical flow rate was 2.351 L/min. Similarly for a tank height of 154 mm the experimental flow rate was 2.453 L/min compared to a theoretical rate of 2.635 L/min. These results consistently show that the experimental discharge is lower than the theoretical prediction. The deviation can be attributed to real-world losses such as fluid viscosity, frictional resistance at the orifice edges, turbulence during flow and imperfect stream contraction. These effects are not accounted for in Bernoulli’s idealized assumptions which explains why the experimental values tend to fall short of the calculated theoretical flow. This comparison not only confirms the necessity of correction factors such as the discharge coefficient (Cd) but also highlights the practical importance of considering energy losses in real engineering applications. 2. Calculate the Coefficient of Velocity, Cv, Coefficient of Contraction, Cc, and Discharge Coefficient, Cd 20 . 21 22 23 24 25 26 8.0 CONCLUSION The experiment was performed to examine water flow through different orifices by finding the coefficients of velocity (CV), contraction (Cc), and discharge (Cd). Relevant measurements taken in the experiment included the flow rate of water, height of the tank, and the diameter of the jet. The values of these coefficients were determined and shown to be dependent on the type of orifice and experimental conditions being considered. Unlike the ideal values of discharge coefficient, the experimental discharge coefficient is a bit different. This is because some of the energy in the fluids is usually lost due to viscosity, turbulence, minor imperfections of the orifice, which are not considered in the theory. It is very important to consider these vital factors of conditions in fluid. Moreover, the study disclosed that the nature of the orifice matters quite much as it influences the flow of the liquid. Varying the orifice geometry also influences jet contraction, flow rate, and hence the total discharge of the liquid, necessitating the need for care when designing a liquid flow system. 27 REFERENCE AE547-EN. (n.d.). Lab 9: Experimental Aerodynamics – Flow Visualization. Middle East Technical University. Retrieved May 28, 2025, from http://www.ae.metu.edu.tr/~ae547/lab13/Lab9_manual.pdf TecQuipment Ltd. (2022). H4 Flow Through an Orifice datasheet. https://www.tecquipment.com/assets/documents/datasheets/H4-Flow-Through-Orifice-Datasheet.pdf Hilado, C. (2020). Flow through an orifice: Experiment No. 05. School of Civil, Environmental, and Geological Engineering, Mechanics of https://www.scribd.com/document/470984231/Experiment-5 28 Fluids Laboratory Report.
0
You can add this document to your study collection(s)
Sign in Available only to authorized usersYou can add this document to your saved list
Sign in Available only to authorized users(For complaints, use another form )