Right well in the case of Stokes flow, the velocity is so low that it is assumed that all drag is viscous in nature, which means that the density has no part in it. It only affects the terminal velocity. With such a low flow velocity, viscous effects are much, much more significant than pressure and density effects.
Consider the nondimensional Navier-Stokes equations:
[tex]\frac{\partial u_i^{*}}{\partial t^{*}} + u_j^{*}\frac{\partial u_i^{*}}{\partial x_j^{*}} = -\frac{\partial p^{*}}{\partial x_i^{*}} + \frac{1}{\textrm{Re}}\frac{\partial^2 u_i^{*}}{\partial x_j^{*} \partial x_j^{*}}[/tex]
Stokes flow assumes that [itex]\textrm{Re} \ll 1[/itex], so the dissipation term, [itex]\frac{\partial^2 u_i^{*}}{\partial x_j^{*} \partial x_j^{*}}[/itex], will be an order of magnitude greater than the pressure term. In other words, the forces on the object in question are going to be dominated by viscosity with negligible contribution by pressure/density effects.