THE VARIATION OF FRICTIONAL AND SEPARATION LOSSES WITH SYSTEM COMPLEXITY IN WATER DISTRIBUTION TO A GROUP OF BUILDINGS

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International Journal of Science, Environment and Technology, Vol. 2, No 5, 2013, 847 862 ISSN 2278-3687 (O) THE VARIATION OF FRICTIONAL AND SEPARATION LOSSES WITH SYSTEM COMPLEXITY IN WATER DISTRIBUTION TO A GROUP OF BUILDINGS 1 J. I. Sodiki and 2 S. Orupabo 1 Department of Mechanical Engineering Rivers State University of Science and Technology P.M.B. 5080, Port Harcourt, Nigeria 2 Department of Civil Engineering University of Port Harcourt P.M.B. 5323, Port Harcourt, Nigeria Emails: 1 jisodiki_partners@yahoo.com / 2 sikaorupabo@yahoo.com Abstract: By progressively increasing the number of buildings supplied from a water reservoir at a fixed elevation, fractions of the total head loss which account for the loss due to friction and through fittings are derived for the varying system complexity. The fractions due to friction vary from 0.807 to 0.686 with a corresponding variation from 0.193 to 0.314 of the fractions due to fittings, as the length of the first index pipe run increases from 68.0m to 122.9m with corresponding increases in the number of appliances supplied from 17 to 68 and in the total water flow rate from 0.88L/s to 2.35L/s. The component fractions are useful for estimating head losses in water distribution networks for groups of buildings. Keywords: Head loss fractions, friction and fittings, groups of buildings. 1. INTRODUCTION The total head loss in gravity-flow water distribution systems comprises of frictional losses and losses through pipe fittings such as elbows, tees, reducers and s. The frictional head loss per metre run of pipe has been derived from the Hazen-Williams formula (utilizing a Hazen-Williams Coefficient C = 140, for plastic pipe material) as (Sodiki, 2002) 4.867 3d 1.85 h = 1.1374 x 10 q (1) f where and d = pipe diameter q = flow rate m s 3 ( / ) Thus, the selection of a suitable pipe diameter depends on the frictional loss per metre run and the flow rate; and graphical presentations of the form of Equation 1 abound in the literature (Institute of Plumbing, 1977 and Barry, 1984). Received August 20, 2013 * Published October 2, 2013 * www.ijset.net

848 J. I. Sodiki and S. Orupabo Furthermore, the head loss through pipe fittings is usually expressed in terms of a loss coefficient k of the fitting as (Sodiki, 2004) h kd q 4 2 p = 0.08256 (2) Values of k for common pipe fittings are given as (Giles, 1977) 0.75 for elbows, 2.0 for tees and 0.25 for gate s. Values for reducers are usually given in terms of the ratio of upstream diameter d 1 to downstream diameter d 2, as in Table 1 (Giles, 1977). The values of k, so obtained, are referred to the downstream diameter to obtain h p from Equation 2. In an earlier paper (Sodiki and Orupabo, 2011), fractions of the total loss which account for the loss due to friction, and through fittings, were derived for varying complexities of pipe work in water distribution to a range of sanitary appliances within a building. The present paper intends to derive fractions for water distribution to a group of buildings. work complexity is expressed, in turn, in terms of length of first index pipe run, number of appliances supplied, and total water discharge from the reservoir. 2. SYSTEM DESCRIPTION The selected water distribution system is gravity-fed from an elevated storage which supplies four bungalows in a residential estate. Each bungalow contains 17 sanitary appliances, made up of 5 water closets, 5 wash basins, 2 bath tubs, 3 water heaters, 1 shower tray and 1 kitchen sink. The site layout is shown in Figure 1. In order to understand the variation of the frictional loss and the loss through pipe fittings, with the varying complexity of pipe work, the distribution system is conceptualized into the four independent forms shown in Figures 1 to 4. The pipe work complexity is found to decrease in the order of Figure 1, 2, 3 to 4. Analyses are carried out on the first index pipe run from the elevated storage, for each form, and comparisons are made. The first index pipe run is the farthest run from the storage and is that which is most likely to be starved of water at its end, due to low system pressure. The distribution system of Figure 4 (which is the least complex) is utilized to illustrate the analysis by which the results for the other forms were also obtained. An isometric sketch of the pipe work of Figure 4 is given in Figure 5 in which the parameters of the different pipe sections are given using boxes placed near the sections. The number to the top of the box is the measured pipe length (in metres), while that to the bottom is the flow rate through the section (in litres per second).

The Variation of Frictional and Separation Losses With.. 849 3. ANALYSIS OF HEAD LOSS COMPONENTS Rather than using complicated mathematical analyses, a more practical graphical method of pipe sizing and determining frictional losses is utilized. Losses through pipe fittings are determined from Equation 2. By the graphical method, loading units (Institute of Plumbing, 1977 and Barry, 1984) for each sanitary appliance (which are taken as 2 for a water closet, 1.5 for a wash basin, 10 for a bath tub, 2 for a water heater, 3 for a shower and 3 for a kitchen sink) are utilized, to account for the non-simultaneous discharge from all the installed appliances. The cumulative discharge units for the different pipe sections are entered in the graph of loading units versus flow rates of Figure 6 (Institute of Plumbing, 1977) to obtain the respective flow rates. For loading units below 10 with corresponding flow rates less than 0.34L/s (for which Figure 6 cannot be used) linear extrapolations are utilized by the equation Design flow = 0.34 10 X loading unit (3) The elevation difference between the distribution pipe outlet at the water reservoir and the highest sanitary appliance supplied is the available static head and is maintained at 3.2m for all the distribution configurations considered. Measured length of the first index run for Figures 4 and 5 = 68.0m Therefore, permissible maximum frictional head loss per metre run (H/L) that must not be 3.2 exceeded in selecting any pipe size = = 0. 047 68.0 Utilizing this H/L value and the sectional flow rates, pipe sizes are selected from the graph of Figure 7 (Institute of Plumbing, 1977). For instance, for the main supply section A to B which has a flow rate of 0.88L/s, a 40mm pipe is selected; at point A in Figure 7, where the actual H/L value obtained at the intersection of the lines of flow rate and pipe diameter is 0.024. Multiplying this value by the measured length of the pipe section (which is 24.0m) gives the frictional head loss of this section as 0.576. The pipe section designations, loading units, design flow rates, pipe lengths, permissible maximum H/L value, pipe sizes, actual H/L values and frictional losses, obtained in a similar manner for all pipe sections, are entered, respectively, in Columns 1 to 8 of Table 2. Having obtained the pipe sizes, locations of reducers are indicated. These are entered in Column 9. Other types of pipe fitting (i.e. elbows, tees and s) in the first index run which are specified in consideration of system functionality are listed in Column 10.

850 J. I. Sodiki and S. Orupabo Now, in pipe section G to I, for instance, there are 1 number 25mm x 20mm reducer (which has d I /d 2 = 1.25), 4 elbows,1 gate and. By interpolation in Table 1, k for the reducer is 0.1025. Then, from Equation 2, for pipe section G to I = (0.1025 + 4 x 0.75 + 0.25 + 2) x 0.08256 x 0.02 x (0.12 x 10 ) 4 3 2 = 0.04m The head loss through fittings, so obtained for the different pipe sections, are entered in Column 11 of Table 2. It is thus observed that the total head loss through friction and that due to fittings for the first index pipe run of the system of Figures 4 and 5 are, respectively, l.657m and 0.397m. By carrying out the foregoing analysis for the other systems (Figure 3, 2 and 1), the results in Tables 3 to 5 are, respectively, obtained. 4. DISCUSSION OF RESULTS The losses due to friction and fittings for all the analyzed systems are summarized in Table 6 which also shows the fractions of these losses that constitute the total loss, for the varying system complexities. Graphical presentations (using Excel ) are given in Figures 8 to 10 to show the variation of the head loss components with system complexity. Within the limits of the utilized values of the variables, the graphs show a decrease of the frictional loss fraction and an increase of the fraction of loss through fittings, with increasing system complexity. Furthermore, second order relationships are depicted for the variations of the ratio of loss through fittings to the total loss, and the different measures of system complexity. Within the limits of system complexity utilized in the analyses, the frictional loss fraction varies from 0.807 to 0.686 with a corresponding variation from 0.193 to 0.314 of the fraction of head loss due to fittings. These fractions are useful in estimating the different head loss components. For instance, for a given length of index pipe length, number of appliances served, or total discharge from the reservoir; and for a given storage elevation, the total head loss can quickly be estimated by adding the relevant fraction due to fittings to the frictional head loss.

The Variation of Frictional and Separation Losses With.. 851 5. CONCLUSIONS Within the limits of pipe work complexity used in the analyses, the fraction of head loss due to friction decreases with a corresponding increase of the fraction due to fittings, for water distribution to a group of buildings. The fractions are useful in the analysis of system pressures, in such situations as in determining storage elevations and pump head requirements. Water distribution systems for larger groups of buildings, such as are utilized in town distribution networks could also be analyzed by the same method. REFERENCES 1. Barry, R. (1984), The Construction of Buildings Vol. 5: Supply and Discharge Services, Granada Publishing Ltd., London. 2. Giles, R. V. (1977), Fluid Mechanics and Hydraulics, McGraw-Hill Book Co., New York 3. Institute of Plumbing (IOP) (1977), Plumbing Services Design Guide, IOP, Essex. 4. Sodiki, J. I. (2002), A Representative Expression for Swimming Pool Circulator Pump Selection, Nigerian Journal of Engineering Research and Development, Vol. 1, No. 4, Pp. 24-35. 5. Sodiki, J. 1. (2004), Computer Generation of Total System Heads for Submersible Pumps in Boreholes, Compendium of Engineering Monographs, Vol. 1, No. 1, Pp. 1-12. 6. Sodiki, J. 1. and Orupabo, S. (2011), Estimating Head and Frictional Losses Through Fittings in Building Water Distribution Systems, Journal of Applied Science and Technology, Vol. 16, Nos 1 & 2, 2011, 67-74.

852 J. I. Sodiki and S. Orupabo Table 1: Values of K for Reducers (Giles, 1977) d 1 /d 2 * 1.2 0.08 1.4 0.17 1.6 0.26 1.8 0.34 2.0 0.37 2.5 0.41 3.0 0.43 4.0 0.45 5.0 0.46 * d 1 = upstream diameter, d 2 = downstream diameter Table 2: Calculations for Sizing and Head Loss Components for Water Distribution to One Bungalow 1 2 3 4 5 6 7 8 9 10 11 Section No Loading Units Design Flow (L/s) length Permissible maximum H/L Diameter (mm) Actual H/L k Frictional head loss, h friction Reducers (mm x mm) Fittings (other than reducers) A to B 49.5 0.88 24.0 0.047 40 0.024 0.576-3elbows 2 gate s Loss through fittings, h fittings 0.119 B to C 46.0 0.85 3.6 0.047 40 0.023 0.083-0.047 C to D 41.0 0.80 3.4 0.047 40 0.020 0.068-0.041 D to F 25.5 0.50 12.4 0.047 32 0.023 0.285 40 X 32 1 elbow F to G 19.0 0.43 5.6 0.047 25 0.045 0.252 32 X 25 0.083 G to I 3.5 0.12 17.0 0.047 20 0.019 0.323 25 X 20 4 elbows 1 gate I to J 1.5 0.05 2.0 0.047 15 0.035 0.070 20 X 15 3 elbows 1 gate 0.056 0.040 0.011 68.0 1.657 0.397

The Variation of Frictional and Separation Losses With.. 853 Table 3: Calculations for Sizing and Head Loss Components for Water Distribution to Two Bungalows 1 2 3 4 5 6 7 8 9 10 11 Section No Loading Units Design Flow (L/s) length Permissible maximum H/L Diameter (mm) Actual H/L Frictional head loss, h friction Reducers (mm x mm) Fittings (other than reducers) A to B 99.0 1.35 24.0 0.035 50 0.013 0.312-3elbows 2 gate s Loss through fittings, B to C 95.5 1.30 3.6 0.035 50 0.012 0.043-0.045 C to D 90.5 1.25 3.4 0.035 50 0.011 0.037-0.041 D to F 75.0 1.10 12.4 0.035 50 0.010 0.124-1 elbow F to G 68.5 0.98 5.6 0.035 40 0.030 0.168 50 x 40 0.065 G to H 53.0 0.90 4.0 0.035 40 0.025 0.100-0.052 H to K 49.5 0.88 8.0 0.035 40 0.024 0.192-1 gate K to L 25.5 0.50 7.0 0.035 32 0.023 0.161 40 x 32 0.041 L to M 19.0 0.43 5.6 0.035 32 0.017 0.095-0.029 M to N 3.5 0.12 17.0 0.035 20 0.019 0.323 32 x 20 4 elbows 1 gate s N to O 1.5 0.05 2.0 0.035 15 0.035 0.070 20 x 15 3 elbows 1 gate h fittings 0.114 0.044 0.056 0.041 0.011 92.6 1.625 0.539

854 J. I. Sodiki and S. Orupabo Table 4: Calculations for Sizing and Head Loss Components for Water Distribution to Three Bungalows 1 2 3 4 5 6 7 8 9 10 11 Section No Loading Units Design Flow (L/s) length Permissible maximum H/L Diameter (mm) Actual H/L Frictional head loss, h friction Reducers (mm x mm) Fittings (other than reducers) A to B 148.5 1.85 24.0 0.033 50 0.0200 0.480-3 elbows 2 gate s Loss through fittings, h fittings 0.215 B to C 145.0 1.80 3.6 0.033 50 0.0190 0.068-0.086 C to D 140.0 1.75 3.4 0.033 50 0.0180 0.061-0.081 D to E 124.5 1.70 6.1 0.033 50 0.0175 0.107-0.076 E to P 49.5 0.88 17.2 0.033 40 0.0240 0.413 50 x 40 1 gate P to Q 46.0 0.82 3.6 0.033 40 0.0220 0.079-0.043 Q to R 41.0 0.80 3.4 0.033 40 0.0200 0.068-0.041 R to S 25.5 0.50 12.4 0.033 32 0.0230 0.285 40 x 32 1 elbow S to T 19.0 0.43 5.6 0.033 32 0.0170 0.095-0.029 T to V 3.5 0.12 17.0 0.033 20 0.0190 0.323 32 x 20 4 elbows 1 gate V to R 1.5 0.05 2.0 0.033 20 0.0045 0.009-3 elbows 1 gate 0.028 0.056 0.041 0.003 98.3 1.988 0.699

The Variation of Frictional and Separation Losses With.. 855 Table 5: Calculations for Sizing and Head Loss Components for Water Distribution to Four Bungalows 1 2 3 4 5 6 7 8 9 10 11 Section No Loading Units Design Flow (L/s) length Permissible maximum H/L Diameter (mm) Actual H/L Frictional head loss, h friction Reducers (mm x mm) Fittings (other than reducers) A to B 198.0 2.35 24.0 0.026 65 0.0100 0.240-3 elbows 2 gate s Loss through fittings, h fittings 0.121 B to C 194.5 2.30 3.6 0.026 65 0.0090 0.032-0.049 C to D 189.5 2.25 3.4 0.026 65 0.0080 0.027-0.047 D to E 174.0 2.20 6.1 0.026 50 0.0250 0.153 65 x 50 0.136 E to P 99.0 1.35 17.2 0.026 50 0.0130 0.224-1 gate P to Q 95.5 1.30 3.6 0.026 50 0.0120 0.043-0.045 Q to R 90.5 1.25 3.4 0.026 50 0.0110 0.037-0.041 R to S 75.0 1.10 12.4 0.026 50 0.0100 0.124-1 elbow S to T 68.5 0.98 5.6 0.026 50 0.0090 0.050-0.025 T to U 53.0 0.90 4.0 0.026 40 0.0250 0.010 50 x 40 0.055 U to X 49.5 0.88 8.0 0.026 40 0.0240 0.192-1 gate X to Y 25.5 0.50 7.0 0.026 32 0.0230 0.161 40 x 32 0.041 Y to Z 19.0 0.43 5.6 0.026 32 0.0170 0.095-0.029 Z to Y 1 3.5 0.12 17.0 0.026 20 0.0190 0.323 32 x 20 4 elbows 1 gate Y 1 to 1.5 0.05 2.0 0.026 20 0.0045 0.009-3 elbows 0.003 Z 1 1 gate 122.9 1.720 0.787 0.054 0.044 0.056 0.041

856 J. I. Sodiki and S. Orupabo Table 6: Head Loss Components for Varying Complexities 1 2 3 4 5 6 7 8 Figure Number Length of 1 st Index Run No. of Appliances Served by Main Distribution Total Water Discharge from Reservoir (L/s) Frictional Loss in 1 st Index Run Loss through Fittings in 1 st Index Run Ratio of Frictional Loss to Total Loss Ratio of Loss through Fittings to Total Loss 4 and 5 68.0 17 0.88 1.657 0.397 0.807 0.193 3 92.6 34 1.35 1.625 0.539 0.751 0.249 2 98.3 51 1.85 1.988 0.699 0.740 0.260 1 122.9 68 2.35 1.720 0.787 0.686 0.314

The Variation of Frictional and Separation Losses With.. 857

858 J. I. Sodiki and S. Orupabo

The Variation of Frictional and Separation Losses With.. 859

860 J. I. Sodiki and S. Orupabo

The Variation of Frictional and Separation Losses With.. 861 0.4 0.3 0.2 0.1 0 0 20 40 60 80 100 120 140 Le ngt h o f 1s t Inde x P ipe R un ( m )

862 J. I. Sodiki and S. Orupabo Fig. 8: Length of Index Run Versus Fraction of Loss Through Fittings 0.4 0.3 0.2 0.1 0 0 20 40 60 80 N o. o f A pplia nc e s S e rv e d by M a in D is t ribut io n P ipe Fig. 9: No. of Appliances Served Versus Fraction of Loss Through Fittings 0.4 0.3 0.2 0.1 0 0 0.5 1 1.5 2 2.5 T o ta l D is cha rge f ro m R e s e rv o ir (L/ s ) Fig. 10: Total Water Discharge Versus Fraction of Loss Through Fittings