Page 246 - Shale Shakers Drilling Fluid Systems
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228  SHALE SHAKERS AND DRILLING FLUID SYSTEMS



            impeller blades in a centrifugal pump, which          See item 12.
            propel the fluid outward. Both types are de-
            signed to move all of the fluid within a certain  16. Mud guns can be used in the Addition and Check/
            volume. The turnover rate (TOR) depends on           Suction Sections of the surface system and pro-
            how much fluid is moving. The TOR must                vide the benefits of shear and dividing and re-
            be large enough to adequately blend the fluid         blending newly added mud materials.
            within the compartment. TOR is calculated as          Mud guns do an excellent job of shearing new
            60 times the tank volume divided by displace-         material enabling it to disperse, and are effec-
            ment. Displacement or flow rate associated            tive at blending new material into the surface
            with each type of blade, based on projected           system. Agitators may aid and assist mud guns
            area of blade, are presented in Table B-l.            in these capacities. The flow rate through a
                                                                  mud gun can be calculated from the follow-
        14. Baffles may be installed around each mechani-         ing equation:
            cal stirrer to prevent air vortices and settling in                         2
            corners. A typical baffle can be 1 inch thick by      Flow rate, gpm = 19.4(D) VH
            12 inches wide and extends from the tank bot-         where D = Nozzle diameter, in.
            tom to 6 inches above the top agitator blade.               H = Head, ft
            Four baffles are installed around each agitator.
            They are installed 6 inches past the tips of the  17. The sand trap is the only settling compartment
            agitator blades, along lines connecting the cen-     in the surface mud system. It should not be
            ter of the agitator blade with the four actual cor-  stirred nor should any pump take its suction
           ners of a square pit or compartment. For a long       from the sand trap.
           rectangular pit, with two or more agitators, the       Sand traps are becoming obsolete except for
            tank is divided into imaginary square compart-        fast drilling surface holes where seawater is
           ments and a baffle is pointed at each corner          used as a drilling fluid and coarse mesh screens
            (either actual or imaginary).                         are used on the shale shakers.
            The purpose of installing baffles is to prevent
            the drilling fluid from swirling in a manner      18. If a sand trap is used, the bottom should slope
            that creates a vortex, which pulls air into the       to its outlet at 45 degrees or steeper. The outlet
            drilling fluid. The baffles can be created in a      valve should be large, non-plugging, and quick
            variety of shapes and positions and still func-      opening and closing.
            tion properly.                                       The bottom slope is needed so that the settled
                                                                 solids can be easily removed from the com-
        15. Mud guns should not be used in the removal           partment. The quick opening and closing valve
           section except where the feed mud to the mud          is needed to reduce drilling fluid loss. The
           gun(s) comes from the compartment being stirred       valve is normally shaped like a plate or rect-
            by the mud gun(s).                                   angular piece of metal.




                                                     TABLE B-1
                       Four 6O° Canted Blade Impeller,            Four Flat Blade Impeller,
                                  57.5 rpm                               57.5 rpm
                      Impeller Diameter      Flow Rate       Impeller Diameter       Flow Rate
                           (inches)            (gpm)              (inches)             (gpm)

                              20                  910                20                 1,100
                              24                 1,600               24                 1,900
                              28                2,500                28                 2,800
                              32                 3,800               32                 4,400
                              36                 5,400               36                 6,300
                              40                 7,300               40                 8,400
                              44                 9,900               44                11,300
                              48                12,500               48                14,400
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