A generic reagent A is considered. The behavior equations of a CSTR reactor is the following:
$$ \tau = c_\mathrm{A,0} \intop_0^{X_\mathrm{A,final}} \dfrac{1}{-r_\mathrm{A}} dX_\mathrm{A} $$
where $\tau$ where it is the filling time, understood as the time required to make a fluid flow rate react whose volume is equal to the reactor volume
$$ \tau = \dfrac{V_\mathrm{reactor}}{\dot{V_\mathrm{A}}} $$
$c_\mathrm{A,0}$ is the initial concentration of A, and $X_\mathrm{A}$ and it is the conversion of A that we want to obtain
From Octave Levenspiel, Chemical Engineering Reaction, John Wiley & Sons, Third Edition, page 103, you can see how the graph $-\dfrac{1}{r_\mathrm{A}} = f(X_\mathrm{A})$ has the shape of a crescent curve
I tried to reproduce this graph, using the formula
$$ -\dfrac{1}{r_\mathrm{A}} = \dfrac{\tau}{c_\mathrm{A,0} X_\mathrm{A}} $$
and what I get is a decreasing curve
My question is: to be able to reproduce the graphic in the text, which formula should I use?