def volume_solutions(T, P, b, delta, epsilon, a_alpha, quick=True):
        r'''Solution of this form of the cubic EOS in terms of volumes. Returns
        three values, all with some complex part.  

        Parameters
        ----------
        T : float
            Temperature, [K]
        P : float
            Pressure, [Pa]
        b : float
            Coefficient calculated by EOS-specific method, [m^3/mol]
        delta : float
            Coefficient calculated by EOS-specific method, [m^3/mol]
        epsilon : float
            Coefficient calculated by EOS-specific method, [m^6/mol^2]
        a_alpha : float
            Coefficient calculated by EOS-specific method, [J^2/mol^2/Pa]
        quick : bool, optional
            Whether to use a SymPy cse-derived expression (3x faster) or 
            individual formulas

        Returns
        -------
        Vs : list[float]
            Three possible molar volumes, [m^3/mol]
            
        Notes
        -----
        Using explicit formulas, as can be derived in the following example,
        is faster than most numeric root finding techniques, and
        finds all values explicitly. It takes several seconds.
        
        >>> from sympy import *
        >>> P, T, V, R, b, a, delta, epsilon, alpha = symbols('P, T, V, R, b, a, delta, epsilon, alpha')
        >>> Tc, Pc, omega = symbols('Tc, Pc, omega')
        >>> CUBIC = R*T/(V-b) - a*alpha/(V*V + delta*V + epsilon) - P
        >>> #solve(CUBIC, V)
        '''
        if quick:
            x0 = 1./P
            x1 = P*b
            x2 = R*T
            x3 = P*delta
            x4 = x1 + x2 - x3
            x5 = x0*x4
            x6 = a_alpha*b
            x7 = epsilon*x1
            x8 = epsilon*x2
            x9 = x0*x0
            x10 = P*epsilon
            x11 = delta*x1
            x12 = delta*x2
            x13 = 3.*a_alpha
            x14 = 3.*x10
            x15 = 3.*x11
            x16 = 3.*x12
            x17 = -x1 - x2 + x3
            x18 = x0*x17*x17
            x19 = ((-13.5*x0*(x6 + x7 + x8) - 4.5*x4*x9*(-a_alpha - x10 + x11 + x12) + ((x9*(-4.*x0*(-x13 - x14 + x15 + x16 + x18)**3 + (-9.*x0*x17*(a_alpha + x10 - x11 - x12) + 2.*x17*x17*x17*x9 - 27.*(x6 + x7 + x8))**2))+0j)**0.5*0.5 - x4**3*x9*x0)+0j)**(1./3.)
            x20 = x13 + x14 - x15 - x16 - x18
            x22 = 2.*x5
            x24 = 1.7320508075688772j + 1.
            x25 = 4.*x0*x20/x19
            x26 = -1.7320508075688772j + 1.
            return [(x0*x20/x19 - x19 + x5)/3.,
                    (x19*x24 + x22 - x25/x24)/6.,
                    (x19*x26 + x22 - x25/x26)/6.]
        else:
            return [-(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)/(3*(sqrt(-4*(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)**3 + (27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/P - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P**2 + 2*(-P*b + P*delta - R*T)**3/P**3)**2)/2 + 27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/(2*P) - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/(2*P**2) + (-P*b + P*delta - R*T)**3/P**3)**(1/3)) - (sqrt(-4*(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)**3 + (27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/P - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P**2 + 2*(-P*b + P*delta - R*T)**3/P**3)**2)/2 + 27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/(2*P) - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/(2*P**2) + (-P*b + P*delta - R*T)**3/P**3)**(1/3)/3 - (-P*b + P*delta - R*T)/(3*P),
                     -(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)/(3*(-1/2 - sqrt(3)*1j/2)*(sqrt(-4*(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)**3 + (27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/P - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P**2 + 2*(-P*b + P*delta - R*T)**3/P**3)**2)/2 + 27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/(2*P) - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/(2*P**2) + (-P*b + P*delta - R*T)**3/P**3)**(1/3)) - (-1/2 - sqrt(3)*1j/2)*(sqrt(-4*(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)**3 + (27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/P - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P**2 + 2*(-P*b + P*delta - R*T)**3/P**3)**2)/2 + 27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/(2*P) - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/(2*P**2) + (-P*b + P*delta - R*T)**3/P**3)**(1/3)/3 - (-P*b + P*delta - R*T)/(3*P),
                     -(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)/(3*(-1/2 + sqrt(3)*1j/2)*(sqrt(-4*(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)**3 + (27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/P - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P**2 + 2*(-P*b + P*delta - R*T)**3/P**3)**2)/2 + 27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/(2*P) - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/(2*P**2) + (-P*b + P*delta - R*T)**3/P**3)**(1/3)) - (-1/2 + sqrt(3)*1j/2)*(sqrt(-4*(-3*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P + (-P*b + P*delta - R*T)**2/P**2)**3 + (27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/P - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/P**2 + 2*(-P*b + P*delta - R*T)**3/P**3)**2)/2 + 27*(-P*b*epsilon - R*T*epsilon - a_alpha*b)/(2*P) - 9*(-P*b + P*delta - R*T)*(-P*b*delta + P*epsilon - R*T*delta + a_alpha)/(2*P**2) + (-P*b + P*delta - R*T)**3/P**3)**(1/3)/3 - (-P*b + P*delta - R*T)/(3*P)]
r'''Solution of this form of the cubic EOS in terms of volumes. Returns
        three values, all with some complex part.  

        Parameters
        ----------
        T : float
            Temperature, [K]
        P : float
            Pressure, [Pa]
        b : float
            Coefficient calculated by EOS-specific method, [m^3/mol]
        delta : float
            Coefficient calculated by EOS-specific method, [m^3/mol]
        epsilon : float
            Coefficient calculated by EOS-specific method, [m^6/mol^2]
        a_alpha : float
            Coefficient calculated by EOS-specific method, [J^2/mol^2/Pa]
        quick : bool, optional
            Whether to use a SymPy cse-derived expression (3x faster) or 
            individual formulas

        Returns
        -------
        Vs : list[float]
            Three possible molar volumes, [m^3/mol]
            
        Notes
        -----
        Using explicit formulas, as can be derived in the following example,
        is faster than most numeric root finding techniques, and
        finds all values explicitly. It takes several seconds.
        
        >>> from sympy import *
        >>> P, T, V, R, b, a, delta, epsilon, alpha = symbols('P, T, V, R, b, a, delta, epsilon, alpha')
        >>> Tc, Pc, omega = symbols('Tc, Pc, omega')
        >>> CUBIC = R*T/(V-b) - a*alpha/(V*V + delta*V + epsilon) - P
        >>> #solve(CUBIC, V)