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Mud Hydraulics Fundamentals                                    55


        where
           ROP = rate of penetration, ft/hr or m/hr
           RPM = rotary speed of bit, rpm

        The constant 0.2 in U.S. units is 0.0167 in SI units.
           The particle friction factor f is a function of the Reynolds number
        N Re and particle sphericity ψ. The sphericity is defined as the surface area
        of a sphere containing the same volume as the particle divided by the
        surface area of the particle. A conservative value for cuttings sphericity is
        0.8. Engineering charts are available for finding the values of the friction
        factor (Bourgoyne et al., 1986). Fang et al. (2008) developed the follow-
        ing correlation to replace the charts:


                                                           2
                          ^                                         (2.92)
                    f p = 10 A′ + B′ logðN ReP Þ + C′½logðN ReP ފ
        where
                                                 2
                  A′ = 2:2954 − 2:2626 ψ + 4:4395 ψ − 2:9825 ψ 3    (2.93)
                  B′ = −0:4193 − 1:9014 ψ + 3:3416 ψ − 2:0409 ψ 3   (2.94)
                                                   2

                  C′ = 0:1117 + 0:0553 ψ − 0:1468 ψ + 0:1145 ψ 3    (2.95)
                                                 2
        where the particle Reynolds number is defined as

                                            f
                                 N ReP =  928ρ v sl d s             (2.96)
                                            μ
        where
           μ = viscosity of Newtonian fluid, cp or Pa-s

        The constant 928 in U.S. units is 1 in SI units.
           Because the slip velocity is implicitly involved in Eqs. (2.90) and
        (2.92), the slip velocity can only be solved numerically (trial and error).
        A computer program called Cuttings Slip Velocity.xls is attached to this
        book for easy calculations. To calculate the particle slip velocity using
        Table 2.4, (1) select a unit system, (2) update the data in the Input Data
        column, and (3) click the Solution button and obtain the result.
           In non-Newtonian fluids, an analytical solution for cuttings terminal
        slip velocity has not been developed. For Bingham plastic fluids, there is
        a critical (minimum) cuttings diameter for it to slip (Bourgoyne et al.,
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