def Barr_1981(Re, eD):
    r'''Calculates Darcy friction factor using the method in Barr (1981) [2]_
    as shown in [1]_.

    .. math::
        \frac{1}{\sqrt{f_d}} = -2\log\left\{\frac{\epsilon}{3.7D} +
        \frac{4.518\log(\frac{Re}{7})}{Re\left[1+\frac{Re^{0.52}}{29}
        \left(\frac{\epsilon}{D}\right)^{0.7}\right]}\right\}

    Parameters
    ----------
    Re : float
        Reynolds number, [-]
    eD : float
        Relative roughness, [-]

    Returns
    -------
    fd : float
        Darcy friction factor [-]

    Notes
    -----
    No range of validity specified for this equation.

    Examples
    --------
    >>> Barr_1981(1E5, 1E-4)
    0.01849836032779929

    References
    ----------
    .. [1] Winning, H. and T. Coole. "Explicit Friction Factor Accuracy and
       Computational Efficiency for Turbulent Flow in Pipes." Flow, Turbulence
       and Combustion 90, no. 1 (January 1, 2013): 1-27.
       doi:10.1007/s10494-012-9419-7
    .. [2]	Barr, Dih, and Colebrook White."Technical Note. Solutions Of The
       Colebrook-White Function For Resistance To Uniform Turbulent Flow."
       ICE Proceedings 71, no. 2 (January 6, 1981): 529-35.
       doi:10.1680/iicep.1981.1895.
    '''
    fd = (-2*log10(eD/3.7 + 4.518*log10(Re/7.)/(Re*(1+Re**0.52/29*eD**0.7))))**-2
    return fd
r'''Calculates Darcy friction factor using the method in Barr (1981) [2]_
    as shown in [1]_.

    .. math::
        \frac{1}{\sqrt{f_d}} = -2\log\left\{\frac{\epsilon}{3.7D} +
        \frac{4.518\log(\frac{Re}{7})}{Re\left[1+\frac{Re^{0.52}}{29}
        \left(\frac{\epsilon}{D}\right)^{0.7}\right]}\right\}

    Parameters
    ----------
    Re : float
        Reynolds number, [-]
    eD : float
        Relative roughness, [-]

    Returns
    -------
    fd : float
        Darcy friction factor [-]

    Notes
    -----
    No range of validity specified for this equation.

    Examples
    --------
    >>> Barr_1981(1E5, 1E-4)
    0.01849836032779929

    References
    ----------
    .. [1] Winning, H. and T. Coole. "Explicit Friction Factor Accuracy and
       Computational Efficiency for Turbulent Flow in Pipes." Flow, Turbulence
       and Combustion 90, no. 1 (January 1, 2013): 1-27.
       doi:10.1007/s10494-012-9419-7
    .. [2]	Barr, Dih, and Colebrook White."Technical Note. Solutions Of The
       Colebrook-White Function For Resistance To Uniform Turbulent Flow."
       ICE Proceedings 71, no. 2 (January 6, 1981): 529-35.
       doi:10.1680/iicep.1981.1895.