def Sun_Mishima(m, D, rhol, rhog, mul, kl, Hvap, sigma, q=None, Te=None):
    r'''Calculates heat transfer coefficient for film boiling of saturated
    fluid in any orientation of flow. Correlation
    is as shown in [1]_, and also reviewed in [2]_ and [3]_.
    
    Either the heat flux or excess temperature is required for the calculation
    of heat transfer coefficient. Uses liquid-only Reynolds number, Weber
    number, and Boiling number. Weber number is defined in terms of the velocity
    if all fluid were liquid.

    .. math::
        h_{tp} = \frac{ 6 Re_{lo}^{1.05} Bg^{0.54}}
        {We_l^{0.191}(\rho_l/\rho_g)^{0.142}}\frac{k_l}{D}
        
        Re_{lo} = \frac{G_{tp}D}{\mu_l}
    
    Parameters
    ----------
    m : float
        Mass flow rate [kg/s]
    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]
    mul : float
        Viscosity of liquid [Pa*s]
    kl : float
        Thermal conductivity of liquid [W/m/K]
    Hvap : float
        Heat of vaporization of liquid [J/kg]
    sigma : float
        Surface tension of liquid [N/m]
    q : float, optional
        Heat flux to wall [W/m^2]
    Te : float, optional
        Excess temperature of wall, [K]

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

    Notes
    -----
    [1]_ has been reviewed. 
    
    [1]_ used 2501 data points to derive the results, covering 
    hydraulic diameters from 0.21 to 6.05 mm and 11 different fluids.
    

    Examples
    --------
    >>> Sun_Mishima(m=1, D=0.3, rhol=567., rhog=18.09, kl=0.086, mul=156E-6, sigma=0.02, Hvap=9E5, Te=10)
    507.6709168372167

    References
    ----------
    .. [1] Sun, Licheng, and Kaichiro Mishima. "An Evaluation of Prediction 
       Methods for Saturated Flow Boiling Heat Transfer in Mini-Channels." 
       International Journal of Heat and Mass Transfer 52, no. 23-24 (November 
       2009): 5323-29. doi:10.1016/j.ijheatmasstransfer.2009.06.041.
    .. [2] Fang, Xiande, Zhanru Zhou, and Dingkun Li. "Review of Correlations 
       of Flow Boiling Heat Transfer Coefficients for Carbon Dioxide."
       International Journal of Refrigeration 36, no. 8 (December 2013): 
       2017-39. doi:10.1016/j.ijrefrig.2013.05.015.
    '''
    G = m/(pi/4*D**2)
    V = G/rhol
    Relo = G*D/mul
    We = Weber(V=V, L=D, rho=rhol, sigma=sigma)
    if q:
        Bg = Boiling(G=G, q=q, Hvap=Hvap)
        return 6*Relo**1.05*Bg**0.54/(We**0.191*(rhol/rhog)**0.142)*kl/D
    elif Te:
        A = 6*Relo**1.05/(We**0.191*(rhol/rhog)**0.142)*kl/D
        return A**(50/23.)*Te**(27/23.)/(G**(27/23.)*Hvap**(27/23.))
    else:
        raise Exception('Either q or Te is needed for this correlation')