def McNelly(rhol, rhog, kl, Cpl, Hvap, sigma, P, Te=None, q=None):
    r'''Calculates heat transfer coefficient for a evaporator operating
    in the nucleate boiling regime according to [2]_ as presented in [1]_.

    Either heat flux or excess temperature is required.

    With `Te` specified:
    
    .. math::
        h = \left(0.225\left(\frac{\Delta T_e C_{p,l}}{H_{vap}}\right)^{0.69}
        \left(\frac{P k_L}{\sigma}\right)^{0.31}
        \left(\frac{\rho_L}{\rho_V}-1\right)^{0.33}\right)^{1/0.31}

    With `q` specified:
    
    .. math::
        h = 0.225\left(\frac{q C_{p,l}}{H_{vap}}\right)^{0.69} \left(\frac{P 
        k_L}{\sigma}\right)^{0.31}\left(\frac{\rho_L}{\rho_V}-1\right)^{0.33}

    Parameters
    ----------
    rhol : float
        Density of the liquid [kg/m^3]
    rhog : float
        Density of the produced gas [kg/m^3]
    kl : float
        Thermal conductivity of liquid [W/m/K]
    Cpl : float
        Heat capacity of liquid [J/kg/K]
    Hvap : float
        Heat of vaporization of the fluid at P, [J/kg]
    sigma : float
        Surface tension of liquid [N/m]
    P : float
        Saturation pressure of fluid, [Pa]
    Te : float, optional
        Excess wall temperature, [K]
    q : float, optional
        Heat flux, [W/m^2]
    
    Returns
    -------
    h : float
        Heat transfer coefficient [W/m^2/K]

    Notes
    -----
    Further examples for this function are desired.

    Examples
    --------
    Water boiling, with excess temperature of 4.3 K.

    >>> McNelly(Te=4.3, P=101325, Cpl=4180., kl=0.688, sigma=0.0588,
    ... Hvap=2.25E6, rhol=958., rhog=0.597)
    533.8056972951352

    References
    ----------
    .. [1] Cao, Eduardo. Heat Transfer in Process Engineering.
       McGraw Hill Professional, 2009.
    .. [2] McNelly M. J.: "A correlation of the rates of heat transfer to n
       ucleate boiling liquids," J. Imp Coll. Chem Eng Soc 7:18, 1953.
    '''
    if Te:
        return (0.225*(Te*Cpl/Hvap)**0.69*(P*kl/sigma)**0.31*(rhol/rhog-1.)**0.33
            )**(1./0.31)
    elif q:
        return 0.225*(q*Cpl/Hvap)**0.69*(P*kl/sigma)**0.31*(rhol/rhog-1.)**0.33
    else:
        raise Exception('Either q or Te is needed for this correlation')
def McNelly ( rhol , rhog , kl , Cpl , Hvap , sigma , P , Te = None , q = None ) : if Te : return ( 0.225 * ( Te * Cpl / Hvap ) ** 0.69 * ( P * kl / sigma ) ** 0.31 * ( rhol / rhog - 1. ) ** 0.33 ) ** ( 1. / 0.31 ) elif q : return 0.225 * ( q * Cpl / Hvap ) ** 0.69 * ( P * kl / sigma ) ** 0.31 * ( rhol / rhog - 1. ) ** 0.33 else : raise Exception ( 'Either q or Te is needed for this correlation' )
r'''Calculates heat transfer coefficient for a evaporator operating
    in the nucleate boiling regime according to [2]_ as presented in [1]_.

    Either heat flux or excess temperature is required.

    With `Te` specified:
    
    .. math::
        h = \left(0.225\left(\frac{\Delta T_e C_{p,l}}{H_{vap}}\right)^{0.69}
        \left(\frac{P k_L}{\sigma}\right)^{0.31}
        \left(\frac{\rho_L}{\rho_V}-1\right)^{0.33}\right)^{1/0.31}

    With `q` specified:
    
    .. math::
        h = 0.225\left(\frac{q C_{p,l}}{H_{vap}}\right)^{0.69} \left(\frac{P 
        k_L}{\sigma}\right)^{0.31}\left(\frac{\rho_L}{\rho_V}-1\right)^{0.33}

    Parameters
    ----------
    rhol : float
        Density of the liquid [kg/m^3]
    rhog : float
        Density of the produced gas [kg/m^3]
    kl : float
        Thermal conductivity of liquid [W/m/K]
    Cpl : float
        Heat capacity of liquid [J/kg/K]
    Hvap : float
        Heat of vaporization of the fluid at P, [J/kg]
    sigma : float
        Surface tension of liquid [N/m]
    P : float
        Saturation pressure of fluid, [Pa]
    Te : float, optional
        Excess wall temperature, [K]
    q : float, optional
        Heat flux, [W/m^2]
    
    Returns
    -------
    h : float
        Heat transfer coefficient [W/m^2/K]

    Notes
    -----
    Further examples for this function are desired.

    Examples
    --------
    Water boiling, with excess temperature of 4.3 K.

    >>> McNelly(Te=4.3, P=101325, Cpl=4180., kl=0.688, sigma=0.0588,
    ... Hvap=2.25E6, rhol=958., rhog=0.597)
    533.8056972951352

    References
    ----------
    .. [1] Cao, Eduardo. Heat Transfer in Process Engineering.
       McGraw Hill Professional, 2009.
    .. [2] McNelly M. J.: "A correlation of the rates of heat transfer to n
       ucleate boiling liquids," J. Imp Coll. Chem Eng Soc 7:18, 1953.