Reduction of Order
Starting from the FSC ODEs :
\[(Cf'')' + ff'' + \beta_H(\tau - f'^2) = 0\]
\[(Cg')' + fg' = 0\]
\[\begin{aligned}
&\left(\frac{C}{\mathrm{Pr}}\tau'\right)'
+ (S-1)\left(C(f'^2)'\right)'
+ (K-1)S\left(C(g^2)'\right)' \\
&\quad + f\!\left[\tau' + (S-1)(f'^2)' + (K-1)S(g^2)'\right] = 0
\end{aligned}\]
where \(C = \rho\mu/(\rho_e\mu_e)\) , \(f' = u/u_e\) , \(g = w/w_e\) , \(\tau = T/T_e\) , and all
primes denote differentiation with respect to \(\eta\) .
Chapman–Rubesin factor
For a perfect gas \(\rho/\rho_e = 1/\tau\) , so the Chapman–Rubesin factor simplifies to:
\[C = \frac{\rho\mu}{\rho_e\mu_e} = \frac{\mu}{\mu_e\tau}\]
Differentiating with respect to \(\eta\) via the quotient rule:
\[C' = \frac{d}{d\eta}\!\left(\frac{\mu}{\mu_e\tau}\right)
= \frac{1}{\mu_e}\frac{\mu'\tau - \mu\tau'}{\tau^2}\]
and therefore:
\[\frac{C'}{C} = \frac{\mu'}{\mu} - \frac{\tau'}{\tau}\]
Expanding the compound derivatives
Applying the product rule to each term:
\[(Cf'')' = C'f'' + Cf'''\]
\[(Cg')' = C'g' + Cg''\]
\[\left(\frac{C}{\mathrm{Pr}}\tau'\right)' = \frac{C'}{\mathrm{Pr}}\tau' + \frac{C}{\mathrm{Pr}}\tau''\]
\[\left(C(f'^2)'\right)' = \left(2Cf'f''\right)' = 2\!\left(C'f'f'' + Cf''^2 + Cf'f'''\right)\]
\[\left(C(g^2)'\right)' = \left(2Cgg'\right)' = 2\!\left(C'gg' + Cg'^2 + Cgg''\right)\]
Substituting into the three ODEs:
x-momentum:
\[C'f'' + Cf''' + ff'' + \beta_H(\tau - f'^2) = 0\]
z-momentum:
\[C'g' + Cg'' + fg' = 0\]
Energy:
\[\frac{C'}{\mathrm{Pr}}\tau' + \frac{C}{\mathrm{Pr}}\tau''
+ 2(S-1)\!\left(C'f'f'' + Cf''^2 + Cf'f'''\right)
+ 2(K-1)S\!\left(C'gg' + Cg'^2 + Cgg''\right)
+ f\!\left[\tau' + 2(S-1)f'f'' + 2(K-1)Sgg'\right] = 0\]
Isolating the highest derivatives
x-momentum → \(f'''\)
Divide by \(C\) and rearrange, using \(C'/C = \mu'/\mu - \tau'/\tau\) :
\[\boxed{f''' = \frac{\tau'}{\tau}\,f'' - \frac{\mu'}{\mu}\,f''
- \frac{ff''}{C} - \frac{\beta_H(\tau - f'^2)}{C}}\]
z-momentum → \(g''\)
Divide by \(C\) and rearrange, using \(C'/C = \mu'/\mu - \tau'/\tau\) :
\[\boxed{g'' = \frac{\tau'}{\tau}\,g' - \frac{\mu'}{\mu}\,g' - \frac{fg'}{C}}\]
Energy → \(\tau''\)
Solve for \(\tau''\) , multiply by \(\mathrm{Pr}/C\) , and substitute \(C'/C = \mu'/\mu - \tau'/\tau\) :
\[\boxed{\begin{aligned}
\tau'' &= \frac{\tau'^2}{\tau} - \frac{\mu'\tau'}{\mu} - \frac{\mathrm{Pr}\,f\tau'}{C} \\
&\quad - 2\mathrm{Pr}(S-1)\!\left[\left(\frac{\mu'}{\mu} - \frac{\tau'}{\tau}\right)f'f'' + f''^2 + f'f'''\right] \\
&\quad - 2\mathrm{Pr}(K-1)S\!\left[\left(\frac{\mu'}{\mu} - \frac{\tau'}{\tau}\right)gg' + g'^2 + gg''\right] \\
&\quad - \frac{2\mathrm{Pr}\,f}{C}\!\left[(S-1)f'f'' + (K-1)Sgg'\right]
\end{aligned}}\]
Viscosity derivatives
The \(\mu'/\mu\) term requires the derivative of viscosity with respect to \(\eta\) .
By the chain rule:
\[\mu' = \frac{d\mu}{d\eta} = \frac{d\mu}{dT}\frac{dT}{d\eta}\]
Since \(T = T_e\tau(\eta)\) :
\[\frac{dT}{d\eta} = T_e\frac{d\tau}{d\eta} = T_e\tau'\]
Therefore:
\[\mu' = \frac{d\mu}{dT}\,T_e\tau'\]
Substituting \(\mu'/\mu = (T_e/\mu)(d\mu/dT)\,\tau'\) into the intermediate expressions gives the final forms:
\[f''' = \frac{\tau'}{\tau}\,f''
- \frac{T_e}{\mu}\frac{d\mu}{dT}\,\tau'f''
- \frac{ff''}{C}
- \frac{\beta_H(\tau - f'^2)}{C}\]
\[g'' = \frac{\tau'}{\tau}\,g'
- \frac{T_e}{\mu}\frac{d\mu}{dT}\,\tau'g'
- \frac{fg'}{C}\]
\[\begin{aligned}
\tau'' &= \frac{\tau'^2}{\tau} - \frac{T_e}{\mu}\frac{d\mu}{dT}\,\tau'^2 - \frac{\mathrm{Pr}\,f\tau'}{C} \\
&\quad - 2\mathrm{Pr}(S-1)\!\left[\left(\frac{T_e}{\mu}\frac{d\mu}{dT} - \frac{1}{\tau}\right)\tau'f'f'' + f''^2 + f'f'''\right] \\
&\quad - 2\mathrm{Pr}(K-1)S\!\left[\left(\frac{T_e}{\mu}\frac{d\mu}{dT} - \frac{1}{\tau}\right)\tau'gg' + g'^2 + gg''\right] \\
&\quad - \frac{2\mathrm{Pr}\,f}{C}\!\left[(S-1)f'f'' + (K-1)Sgg'\right]
\end{aligned}\]
where \(\mu = \mu(T_e\tau)\) and \(C = \mu/(\mu_e\tau)\) are evaluated locally at each \(\eta\) ,
and \(f'''\) and \(g''\) are computed first.
State variables
The third-order equation in \(f\) , the second-order equation in \(g\) , and the second-order equation in
\(\tau\) yield a seventh-order system. Define:
\[y_1 = f, \quad y_2 = f', \quad y_3 = f'', \quad y_4 = \tau, \quad y_5 = \tau', \quad y_6 = g, \quad y_7 = g'\]
First-order ODE system
\[y_1' = y_2\]
\[y_2' = y_3\]
\[y_3' = \frac{y_5}{y_4}\,y_3
- \frac{T_e}{\mu}\frac{d\mu}{dT}\,y_5 y_3
- \frac{y_1 y_3 + \beta_H(y_4 - y_2^2)}{C}\]
\[y_4' = y_5\]
\[\begin{aligned}
y_5' &= \frac{y_5^2}{y_4} - \frac{T_e}{\mu}\frac{d\mu}{dT}\,y_5^2 - \frac{\mathrm{Pr}\,y_1 y_5}{C} \\
&\quad - 2\mathrm{Pr}(S-1)\!\left[\left(\frac{T_e}{\mu}\frac{d\mu}{dT} - \frac{1}{y_4}\right)y_5 y_2 y_3 + y_3^2 + y_2 y_3'\right] \\
&\quad - 2\mathrm{Pr}(K-1)S\!\left[\left(\frac{T_e}{\mu}\frac{d\mu}{dT} - \frac{1}{y_4}\right)y_5 y_6 y_7 + y_7^2 + y_6 y_7'\right] \\
&\quad - \frac{2\mathrm{Pr}\,y_1}{C}\!\left[(S-1)y_2 y_3 + (K-1)S\,y_6 y_7\right]
\end{aligned}\]
\[y_6' = y_7\]
\[y_7' = \frac{y_5}{y_4}\,y_7
- \frac{T_e}{\mu}\frac{d\mu}{dT}\,y_5 y_7
- \frac{y_1 y_7}{C}\]
where \(C = \mu(T_e y_4)/(\mu_e y_4)\) , \(T = T_e y_4\) , and \(y_3'\) , \(y_7'\) are computed before \(y_5'\) .
Boundary conditions
Wall (\(\eta = 0\) ):
\[y_1 = 0, \qquad y_2 = 0, \qquad y_6 = 0\]
Isothermal : \(y_4 = T_w/T_e\)
Adiabatic : \(y_5 = 0\)
Edge (\(\eta \to \infty\) ):
\[y_2 = 1, \qquad y_4 = 1, \qquad y_6 = 1\]
The unknown wall values \(y_3(0) = f''(0)\) , \(y_7(0) = g'(0)\) , and (for isothermal walls)
\(y_5(0) = \tau'(0)\) are determined by shooting to match the edge conditions.