UNIVERSITY OF DAR ES SALAAM DEPARTMENT OF WATER RESOURCES ENGINEERING FLUID MECHANICS FOR CIVIL ENGINEERS WR 211 PRACTICAL No: 1 HEAD LOSSES IN SMALL BORE PIPE SYSTEMS NAME: BILALI AHMAD REGISTRATION NO: 2020-04-00746 DEGREE PROGRAMME: BSc. IN MINING ENGINEERING DEPARTMENT: WATER RESOURCES ENGINEERING DATE OF SUBMISSION: 23 DECEMBER 2022 INTRODUCTION The minor losses are those which are caused by change in pipe cross section, presence of bends, valves and fittings. Although in long pipelines the losses due to the local disturbances caused by these fittings are of minor importance and often can be neglected, they may however outweigh the friction losses in short pipe. The source of losses is usually confined to every short length of the pipe. A theoretical determination of the minor losses is seldom possible except for the loss due to sudden enlargement. Since the losses have been experimentally found to vary approximately as the square of the mean velocity, they are normally expressed in the form HL =KL V2/ 2g In which KLis known as the loss coefficient. For geometry, the value if KL is practically constant at high Reynolds number, the magnitude of the loss coefficient is experimentally determined and is governed primarily by the shape of the obstruction or pipe fitting. OBJECTIVES Part 1: To examine the minor energy head losses(i.e shock losses) for; 1. 900 elbow bend (small radius) 2. 900 mitre bend 3. 900 large radius bend Verify that; hshock ∆h =∆h =K Part 2: To show that shock losses due to sudden contraction are also proportional to the velocity head and to calculate the coefficient of contraction. hL=K.V2/2g= (1/CC-1)2.V2/2g where CC is the coefficient of contraction. The graph of hfvs v2/2g would be drawn to verify the value of K. Part 3: To confirm the Borda –Carnot equation for head loss in a sudden expansion from the experimental results. Note:Borda-Carnot equations is obtained by using 3-equations.These equations are: Continuity equation Momentum equation Energy equation. The Borda-Carnot equations for Head losses is given by: HL = ( ) APPARATUS Hydraulic circuit: It consists of Piezometer tappings and thus pressure changes across each of the components are measured by a pair of pressurized piezometer tubes. Hydraulic bench: Used to circulate and measure volume of water in litres. Stop watch:Was used to record the time taken to measure a particular volume Piezometric apparatus and its block diagram PROCEDURE The pump was started and the bench supply and apparatus valves were opened. Water was allowed to flow for some 2 minutes. The apparatus control valve was then partially closed and the manometer was purged in using the vent valve. The apparatus control valve was then closed. Air was then pumped into the manometer to obtain zero pressure differences in the piezometer tubes at the convenient level. And six readings for Q (discharge) and H diff (pressure head difference) was recorded,Hdiff being reduced in equal decrements. DATA COLLECTION Given the following; Pipe Diameter D1 = 22.5mm Pipe Diameter D 2 = 29.6mm A1 = 3.98 X 10-4m2 A 2= 6.88 X 10-4m2 PIPE SYSTEM: PIEZOMETRIC HEAD LOSSES AT VARIOUS RATES OF FLOW Pipe diameter D1= 22.5mm Pipe diameter D2= 29.6mm Data Sheet VOLUME TIME MITRE ELBOW SUDDEN SUDDEN V (T) BEND BEND (L) (sec) Hdiff Hdiff Hdiff Hdiff BEND 1-2 3-4 5-6 7-8 Hdiff (m) (m) (m) (m) 9-10 ENLARGEMENT CONTRACTION LARGE RADIUS (m) 5 10.59 0.14 0.095 -0.04 0.095 0.06 5 12.80 0.115 0.08 -0.035 0.08 0.05 5 15.21 0.095 0.066 -0.025 0.069 0.042 5 15.70 0.075 0.055 -0.020 0.060 0.032 5 20.81 0.055 0.045 -0.015 0.045 0.025 5 22.21 0.045 0.035 -0.010 0.030 0.020 5 31.63 0.03 0.025 -0.003 0.025 0.015 5 41.98 0.02 0.02 -0.001 0.015 0.010 Note The negative sign indicate that there is sudden enlargement Table of results Where; Velocity (Velocity in D1 pipe) V = Q/A1 Discharge Q X 10 -4 Velocity in D1 pipe 3 (m /s) Velocity Head 2 V /2g V (m) (m/s) Pressure Sudden Sudden Change Enlargement Contraction Hshock= Hshock= 0.034V2-Hdiff Hdiff-0.034V2 (m) (m) 0.034V (m) 2 4.72 1.19 0.072 0.048 0.008 0.047 3.91 0.99 0.050 0.033 -0.002 0.047 3.29 0.83 0.035 0.022 -0.003 0.047 3.19 0.80 0.033 0.022 0.002 0.038 2.40 0.60 0.018 0.012 -0.003 0.033 2.25 0.57 0.017 0.011 -0.001 0.02 1.58 0.40 0.008 0.005 0.002 0.02 1.19 0.30 0.004 0.003 0.002 0.012 GRAPHS AND ANALYSIS FROM THE GRAPHS THE GRAPH OF HSHOCK(M) AGAINST V2/2g(M) FOR THE METRE BEND, ELBOW AND LARGE RADIUS 0.16 y = 1.817x + 0.018 0.14 Hshock(m) 0.12 y = 1.138x + 0.018 0.1 0.08 METRE BEND y = 0.755x + 0.009 0.06 ELBOW LARGE RADIUS 0.04 0.02 0 0 0.01 0.02 V2/2g 0.03 The value of k for mitre bend is 1.817 The value ofk for elbow bend is 1.138 The value of k for large radius bend is 0.755 0.04 0.05 0.06 0.07 0.08 THE GRAPH OF HSHOCK(M) AGAINST V2/2g(M) FOR THE SUDDEN CONTRACTION 0.06 0.05 y = 0.532x + 0.017 Hshock(m) 0.04 0.03 Series1 Linear (Series1) 0.02 0.01 0 0 0.02 0.04 0.06 Axis Title From the graph the value of k=0.532 ANALYSIS AND CALCULATIONS From the graph above; K = 0.532 But K = Thus −1 =0.6984 where Cc = coefficient of contraction = √0.532 + 1 ∴ 𝐂𝐜 = 𝟎. 𝟓𝟕𝟖2 The coefficient of contraction,Cc is 0.531 0.08 THE GRAPH OF HSHOCK(M) AGAINST V2/2g (M) FOR THE SUDDEN ENLARGEMENT. 0.01 0.008 Hshock(m) 0.006 0.004 0.002 y = 0.065x - 0.001 0 0 0.01 0.02 0.03 0.04 0.05 0.06 0.07 0.08 -0.002 -0.004 V2/2g(m) From the graph the value of k=0.065 ANALYSIS AND CALCULATIONS To confirm the Borda –Carnot equation for head loss in sudden expansion from experimental results HL = (V1 – V2)2 2g From continuity equation V2 =A1V1/ A2 hL = (V1-{ A1V1/A2})2 2g hL= (1 - A1/A2)2V12 2g hL=kV2 2g But A2 = 688.1mm2, A1 = 398.mm2 k= (1 – (398mm2/688.1mm2)) 2 The theoretical value of k is 0.178 From the graph the value of k is 0.065 The value of k obtained from Borda – Carnot equation and that obtained from graph varies greatly due to error which was previously made by neglecting of frictional losses in the pipe. Since Head losses the pipe is caused by friction which is the major loss and suddenly enlargement and contraction which are the minor loss. SOURCES OF ERRORS Parallax Fluctuation of liquid level in manometer Timing error while recording the quantity of discharge Approximately of value in calculation CONCLUSION Generally change in direction of fluid flow have always brought loss, but the loss brought about by the bends varies from high head loss in sharply bend to minimum losses in slightly bent pipes.The loss is highly brought about by the reaction which is exerted by water flowing at the bend. Also verification of Borda-Carnot equation has proved some failure since the value are neither close nor the same. This was caused by assuming that losses due to friction were not present in the pipes.