Page 126 - Pipeline Rules of Thumb Handbook
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Pipe Design  113

                                Figure 5                                              Figure 6
                      Recommended Liquid Velocities                                 ID to OD Ratio

                                        Pipe Size-Inches         SDR            F              SDR             F
                                 3–10        10–28     28–48      7             0.706          13.5            0.852
           Water and Similar                                      7.3           0.719          15.5            0.873
           Viscosity Fluids                                       9             0.774          17              0.884
                                          Velocity, fps           9.3           0.781          21              0.909
           Pump suction*         1 to 4      3 to 6    5 to 8    11             0.817          26              0.928
           Pump discharge        3 to 5      4 to 8    6 to 12                                 32.5            0.944
           Gravity drain system  3 to 5      4 to 8    6 to 10
                                                                                   Pressure drop
           Viscous liquids
           Pump suction*         0.5 to 2    1 to 4    2 to 5
                                                                   Refer to Section 13: Liquids—Hydraulics and use the
           Pump discharge        3 to 5      4 to 6    5 to 7
                                                                 Hazen-Williams equation. Use a C of 150.
           * It is important in the selection of the pipe size that the
           designated pump suction velocity be lower than the
           discharge velocity.                                                Fitting equivalent length

                                                                   The exact pressure loss through fittings cannot readily be
                                                                 calculated because of the geometry of the fitting. The
                                                                 values shown in Figure 7 are the result of general industry
                                                                 consensus.
                             Pipe diameter
             Volumetric flow, Q, can be determined from the continu-                   Figure 7
           ity equation Q = A ¥ V by selecting a suitable velocity from      Equivalent Length of Fittings
           Figure 5 for a given pipe size. When modified for flow in
           gallons per minute, the equation becomes:             Fitting Type              Equivalent length of pipe
                                                                 90deg.elbow                          30D
           Q = 2 449  ¥  V ¥  d 2                                60deg.elbow                          25D
               .
                                                                 45deg.elbow                          16D
           where                                                 45deg.wye                            60D
           Q = flow rate in gpm                                   Running tee                          20D
           V = velocity if feet per second                       Branch tee                           50D
           d = inside diameter, inches                           Gate valve, full open                 8D
                                                                 Butterfly valve (3≤ to 14≤)           40D
           or d = ( Q ∏ 2 449  ¥  V) 12  for pipe size determination .  Butterfly valve ≥14≤           30D
                     .
                                                                 Swing check valve                   100D
           Example: If the required water flow rate for a system is   Ball valve full bore full open    3D
           2,000gpm and the flow velocity is to be maintained below
           8fps, the pipe diameter can be found as follows:      Example: A running tee has an equivalent length of 20D. For
                                                                 an 18≤ SDR 11 line, this represents 20 ¥ ID. From Figure 6,
           d = ( Q ∏ 2 449  ¥  V) 12                             ID = OD ¥ F = 18 ¥ 0.817 = 14.7≤¥ 20 = 294 ∏ 12 and is
                   .
                                                                 equal to 24.5 feet. In calculating the total pressure drop in
                             12
                     .
           d = (2000 2 449  ¥ ) 8                                the system, 24.5 feet of 18 inch pipe should be added to the
                   ∏
                                                                 total line length to account for the increased pressure loss due
           d = 10.1 inches inside diameter                       to the presence of the tee.
                   ∏ (
           OD ID F F from Figure ) 6                             Published with permission—CSR TM  PolyPipe
              =
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