I think the author of this problem forgot to add units to $K_c$ since it's not a dimensionless entity:
$$K_c = \frac{[\ce{NO}]^2}{[\ce{N2O}][\ce{O2}]^{0.5}}$$
and should be $K_c = \pu{1.7e-13 mol^{0.5} L^{-0.5}}$. In general
$$[K_c] = \mathrm{dim}(c)^{Δn}$$
where square brackets denote the dimensions of the quantity $K_c$, $c$ is concentration and $Δn$ is the difference in the amounts between gaseous products and reactants, e.g. here
$$Δn = 2 - (1 + 0.5) = 0.5$$
On the other hand, the equilibrium constant $K$ you use for determining the standard Gibbs energy, must be dimensionless. Since we are dealing with gases only, the easiest way is to use $K_p$, which is dimensionless as required (when normalized to the standard state of pressure $p^\circ = \pu{1 bar}$):
$$K_p = \frac{\left(\frac{p(\ce{NO})}{p^\circ}\right)^2}{\left(\frac{p(\ce{N2O})}{p^\circ}\right) \left(\frac{p(\ce{O2})}{p^\circ}\right)^{0.5}}$$
so that in general
$$[K_p] = \mathrm{dim}(p)^{Δn}\cdot \mathrm{dim}(p^\circ)^{-Δn}$$
$K_p$ and $K_c$ are related (via the ideal gas law):
$$K_p = K_c (RT)^{Δn}$$
So, the equilibrium constant is
$$
\begin{align}
K &= K_p(p^\circ)^{-Δn}\\
&= K_c(RT)^{Δn}(p^\circ)^{-Δn} \\
&= \pu{1.7e-13 mol^{0.5} L^{-0.5}}\cdot(\pu{8.314e-2 L bar K−1 mol−1}\cdot\pu{298 K})^{0.5}(\pu{1 bar})^{-0.5} \\
&= \pu{8.5e-13}
\end{align}
$$
Note that here I used gas constant expressed as $\pu{8.314e-2 L bar K−1 mol−1}$ since in this case all dimensions are cancelled out and $K$ is left dimensionless. Now we can finally find the standard Gibbs energy:
$$
\begin{align}
Δ G^\circ &= -RT\ln K\\
&= -\pu{8.314 J mol-1 K-1}\cdot\pu{298 K}\cdot\ln\left(\pu{8.5e-13}\right)\\
&= \pu{68.9 kJ mol-1}
\end{align}
$$
Here the product before the logarithm includes $R = \pu{8.314 J mol-1 K-1}$ to get answer in $\pu{kJ mol-1}$ straight away.