def Martin_Sims(m, x, D, rhol, rhog, hl):
    r'''Calculates the two-phase non-boiling heat transfer coefficient of a 
    liquid and gas flowing inside a tube of any inclination, as in [1]_ and 
    reviewed in [2]_.

    .. math::
        \frac{h_{TP}}{h_l} = 1 + 0.64\sqrt{\frac{V_{gs}}{V_{ls}}}
            
    Parameters
    ----------
    m : float
        Mass flow rate [kg/s]
    x : float
        Quality at the specific tube interval []
    D : float
        Diameter of the tube [m]
    rhol : float
        Density of the liquid [kg/m^3]
    rhog : float
        Density of the gas [kg/m^3]
    hl : float
        Liquid-phase heat transfer coefficient as described below, [W/m^2/K]

    Returns
    -------
    h : float
        Heat transfer coefficient [W/m^2/K]

    Notes
    -----
    No suggestion for how to calculate the liquid-phase heat transfer
    coefficient is given in [1]_; [2]_ suggests to use the same procedure as
    in `Knott`, but this has not been implemented.
    
    Examples
    --------
    >>> Martin_Sims(m=1, x=.9, D=.3, rhol=1000, rhog=2.5, hl=141.2)
    5563.280000000001

    References
    ----------
    .. [1] Martin, B. W, and G. E Sims. "Forced Convection Heat Transfer to 
       Water with Air Injection in a Rectangular Duct." International Journal 
       of Heat and Mass Transfer 14, no. 8 (August 1, 1971): 1115-34. 
       doi:10.1016/0017-9310(71)90208-0.
    .. [2] Dongwoo Kim, Venkata K. Ryali, Afshin J. Ghajar, Ronald L. 
       Dougherty. "Comparison of 20 Two-Phase Heat Transfer Correlations with 
       Seven Sets of Experimental Data, Including Flow Pattern and Tube 
       Inclination Effects." Heat Transfer Engineering 20, no. 1 (February 1, 
       1999): 15-40. doi:10.1080/014576399271691.
    '''
    Vgs = m*x/(rhog*pi/4*D**2)
    Vls = m*(1-x)/(rhol*pi/4*D**2)
    return hl*(1 + 0.64*(Vgs/Vls)**0.5)
r'''Calculates the two-phase non-boiling heat transfer coefficient of a 
    liquid and gas flowing inside a tube of any inclination, as in [1]_ and 
    reviewed in [2]_.

    .. math::
        \frac{h_{TP}}{h_l} = 1 + 0.64\sqrt{\frac{V_{gs}}{V_{ls}}}
            
    Parameters
    ----------
    m : float
        Mass flow rate [kg/s]
    x : float
        Quality at the specific tube interval []
    D : float
        Diameter of the tube [m]
    rhol : float
        Density of the liquid [kg/m^3]
    rhog : float
        Density of the gas [kg/m^3]
    hl : float
        Liquid-phase heat transfer coefficient as described below, [W/m^2/K]

    Returns
    -------
    h : float
        Heat transfer coefficient [W/m^2/K]

    Notes
    -----
    No suggestion for how to calculate the liquid-phase heat transfer
    coefficient is given in [1]_; [2]_ suggests to use the same procedure as
    in `Knott`, but this has not been implemented.
    
    Examples
    --------
    >>> Martin_Sims(m=1, x=.9, D=.3, rhol=1000, rhog=2.5, hl=141.2)
    5563.280000000001

    References
    ----------
    .. [1] Martin, B. W, and G. E Sims. "Forced Convection Heat Transfer to 
       Water with Air Injection in a Rectangular Duct." International Journal 
       of Heat and Mass Transfer 14, no. 8 (August 1, 1971): 1115-34. 
       doi:10.1016/0017-9310(71)90208-0.
    .. [2] Dongwoo Kim, Venkata K. Ryali, Afshin J. Ghajar, Ronald L. 
       Dougherty. "Comparison of 20 Two-Phase Heat Transfer Correlations with 
       Seven Sets of Experimental Data, Including Flow Pattern and Tube 
       Inclination Effects." Heat Transfer Engineering 20, no. 1 (February 1, 
       1999): 15-40. doi:10.1080/014576399271691.