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                    258  Chapter 7  Water Distribution Systems: Modeling and Computer Applications
                          Table 7.13  Pipe Information for Problem 7.2  highest node), and the top is approximately 20 ft (6.1 m) higher.
                                                                    To avoid the cost of an elevated tank, this 80-ft-diameter (24.4-
                          Pipe     Diameter (mm)    Length (m)
                                                                    m-diameter) tank is located on a hillside, 2,000 ft (610 m) away
                          P-1          250           1,525          from the main system. Assume that the tank starts with a water
                          P-2          150             300          surface elevation of 380 ft (115.8 m). The pump was originally
                          P-3          150             240          sized to deliver 300 gpm (1,135 L/min) with enough head to
                          P-4          150             275          pump against the tank when it is full. Three defining points on
                          P-5          150             245          the pump curve are as follows: 0 gpm at 200 ft of head; 300 gpm
                          P-6          200             230          at 180 ft of head; and 600 gpm at 150 ft of head (0 L/min at 610 m
                                                                    of head; 1,135 L/min at 54.9 m of head; and 2,271 L/min at 45.7 m
                                                                    of head). The pump elevation is assumed to be the same as the
                        Table 7.14  Junction Information for Problem 7.2
                                                                    elevation at J-1, although the precise pump elevation is not cru-
                        Junction   Elevation (m)  Demand (L/min)    cial to the analysis.
                                                                       The system is to be analyzed under several demand condi-
                          J-1          55             950           tions with minimum and maximum pressure constraints.
                          J-2          49            1,060          During normal operations, the junction pressures should be be-
                          J-3          58            1,440          tween 35 psi and 80 psi (243 kPa and 555 kPa). Under fire flow
                          J-4          46            1,175          conditions, however, the minimum pressure is allowed to drop
                          J-5          44             980
                                                                    to 20 psi (139 kPa). Fire protection is being considered both
                                                                    with and without a sprinkler system.
                                                                       Demand Alternatives: WaterGEMS enables you to store
                    7.3  A distribution system is needed to supply water to a resort  multiple demand alternatives corresponding to various condi-
                    development for normal usage and emergency purposes (such as  tions (such as average day, peak hour, etc.). This feature allows
                    fighting a fire). The proposed system layout is shown in Fig. 7.14.  you run different scenarios that incorporate various demand
                    The source of water for the system is a pumped well. The water is  conditions within a single project file without losing any input
                    treated and placed in a ground-level tank (shown in the figure as  data. For an introduction and more information about scenarios
                    a reservoir because of its plentiful supply), which is maintained at  and alternatives, see WaterGEMS’s online help system.
                    a water surface elevation of 210 ft (64 m). The water is then  Pipe Network: The pipe network consists of the pipes
                    pumped from this tank into the rest of the system.  listed in Table 7.15. The diameters shown are based on the pre-
                        The well system alone cannot efficiently provide the  liminary design, and may not be adequate for the final design.
                    amount of water needed for fire protection, so an elevated stor-  For all pipes, use ductile iron as the material and a Hazen-
                    age tank is also needed. The bottom of the tank is at 376 ft  Williams C factor of 130. The junction information for this
                    (114.6 m) (high enough to produce 35 psi or 243 kPa at the  problem is given in Table 7.16.


                                       Well and tank
                                    R-1                            T-1
                                                                                        Pro shop
                                         P-1
                                      PMP-1     P-2                 P-15
                                                     J-1    P-3      J-2    P-4     J-3

                                                                          Hotel
                                                                    P-12   J-11     P-5
                                                       P-11
                                                    P-10  J-9
                                                J-8                        P-14
                                                                       P-7     P-6
                                                               P-8  J-6      J-5    J-4
                                                       P-9
                                                                           P-13
                                                                        J-10
                                                           J-7                        Administration
                                                                         Entrance    and maintenance
                                    Figure 7.14 Schematic for Problem 7.3
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