Page 205 - Shale Shakers Drilling Fluid Systems
P. 205

188   SHALE SHAKERS AND DRILLING FLUID SYSTEMS




            Sample Calculation:

            For 800 gpm of a 12.0 ppg drilling fluid flowing through a 6-inch diameter. Schedule 80 pipe, the fluid has a PV = 20 cp.
                              2
            and a YP = 18 lb/100 ft . Find the Reynold's number.
            The pipe data in Table 11-2 shows that the pipe's inside diameter is 5.76 inches.
            The velocity of the fluid in the pipe would be:






            The 600-rpm Fann reading would be 58 (the 300 rpm reading would be 38). The apparent viscosity would be 29 cp.






            This value is larger than 4000, so this flow is turbulent.






            This equation is correct for either laminar or     where d = Pipe inside diameter, in.
         turbulent flow.' It calculates the head loss of a            v = Velocity of liquid, ft/sec
         constant-density fluid flowing in a straight, constant-    MW = Fluid density, pounds per gallon
         diameter pipe.                                               p = Viscosity of the fluid, centipoise
            For laminar flow conditions, or Reynold's num-
         ber (R e) less than 2000, the friction factor (f) is:    For laminar flow, R e < 2000; and for turbuler
                                                               flow, R e > 4000.
                                                                  Viscosity for Newtonian fluids can be easil
                                                               defined if the pressure and temperatures are knowr
            For turbulent flow conditions, or Reynold's num    Drilling fluids, however, are usually shear-thinninj
         ber (R e) greater than 4000, the friction factor is:  and the viscosity decreases as the shear rate ir
                                                               creases. Drilling fluid viscosity also depends on th
                                                               pressure and temperature. If the flow properties c
                                                               a drilling fluid are known as a function of shea
                                                               rate, the viscosity for the appropriate shear rat
            The head loss (H) for fluid with a viscosity, p,   can be used to calculate head loss in a pipe systerr
         and a flow rate, Q, gpm, in a pipe with a diam-       In lieu of this, the apparent viscosity can be usec
         eter of D, inches, would be:                          This value, in centipoise, is calculated by dividin
                                                               the 600-rpm Fann reading by two. This is the vis
                                                               cosity of the drilling fluid at 1022 sec~' shear rat<
                                                                  After determining the Reynold's number an
                                                               flow regime, the head loss per unit length of pip
         where L e = Equivalent length of pipe, ft             may be calculated from the equation:

         Elbows, valves, swedges, and changes in direction
         of piping can be expressed in equivalent lengths
         of straight, smooth pipe (Table 11-I). Reynold's
         number may be calculated from the equation:
                                                                  To calculate velocity, v in ft/sec, the following
                                                               equation can be used instead of using the conver-
                                                               sion factors. Here, Q is in gpm and d is the inside
                                                               pipe diameter in inches:

         1
           The velocity head is the vV2g part of this equation. This should
         be recognizable from the kinetic energy equation: KE = m(vV2g).
   200   201   202   203   204   205   206   207   208   209   210