Page 163 - Shale Shakers Drilling Fluid Systems
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146   SHALE SHAKERS AND DRILLING FLUID SYSTEMS



                                      TABLE 7-3. Flow Rates through Hydrocyclones

                                            Cone Diameter       Flow Rate through Each Cone
                          Designation            (in.)                     (gpm)
                          Desilter                 2                        1O-30
                         Desilter                  4                        50-65
                         Desilter                  5                        75-85
                         Desander                  6                       100-120
                         Desander                  8                       20O-240
                         Desander                 10                       400-500
                         Desander                 12                       5OO-600
                         Note: Numbers in bold indicate the most common flow rate.




           The D 50 cut point of a solids separation de-      over the lip of the apex as an annular ring. The
        vice is usually defined as the particle size at which  apex is actually a weir or dam, not a choke or valve.
        one-half of the weight of those particles go to the     The high-velocity return stream spinning upward
        underflow and one-half of the weight of those par-    near the center of the cone into the vortex finder
        ticles go to the overflow. The cut point is related   generates a column of lower pressure, which sucks
        to the inside diameter of the hydrocyclone. For       air inward through the center of the apex opening.
        example, a 12-inch cone is capable of a D 50 cut        To set a cone to balance, slowly open the apex
        point around 60 to 80 microns, a 6-inch cone is       discharge while circulating water through the cone.
        capable of around 40 to 60 microns, and a 4-inch      When a small amount of water is discharged and
        cone is capable of around 20 to 40 microns. These     the center air core is almost the same diameter as
        cut points are representative for a fluid that        the opening, the cone is "balanced."
        contains a low solids content. The cut point will       With spray discharge, the device removes the
        vary according to the size and quantity of solids     maximum amount of solids and discarding of whole
        in the feed and the flow properties of the fluid. Cut  mud is minimized. The umbrella-shaped spray dis-
        point determination procedures are explained in       charge indicates that a uniform solids loading is
        Chapter 9.                                            presenting to the cone, with proper separation
          When hydrocyclones are mounted above the            occurring. The pattern of the apex discharge pro-
        liquid level in the mud tanks, a siphon breaker       vides a good indication of cone operation. The
        should be installed in the overflow manifold from     discharge should have a hollow center and appear
        the cones.                                            as a cone spray. A wide cone spray may indicate
                                                              the apex orifice is too large. When the apex ori-
                                                              fice is larger than required, an excess amount
        Discharge                                             of liquid will exit, carrying with it finer feed sol-
                                                              ids, thereby reducing sharpness of separation and
          Most hydrocyclones are designed to be balanced.     underflow density.
        A properly adjusted, balanced hydrocyclone has          Several conditions restrict separations and ex-
        a spray discharge at the underflow outlet and         iting of solids that have spiraled along the cone
        exhibits a central air suction core. A balanced       wall. These include:
        cyclone can be adjusted so that when water is fed
        under pressure, nothing discharges at the apex.         • Excessive solids concentration
        Conversely, when coarse solids are added to the         • Excessive volumetric feed rate per cone
        feed slurry, wet solids are discharged at the apex.     • Excessive fluid viscosity
        Even with this adjustment, there still should be a      • Restricted (too small) apex
        large opening in the bottom of the cyclone. This        • Inadequate feed pressure
        will confirm that the cyclone is hydraulically bal-
        anced and discharges at the bottom (apex) only          A greater number of larger solids are entrained
        when solids, which the cyclone can separate, are      within the central vortex stream to exit with the
        in the feed slurry (drilling fluid).                  overflow. The discharge pattern changes from spray
          A balanced cyclone should be operated with          to "rope discharge"—characterized by a cylindri-
        "spray discharge." Here, coarser solids separate      cal or "ropy" appearance. With the rope discharge,
        to the outside in the downward spiral and pass        no air core occurs through the center of the cone.
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