Non-Darcy flow of oil above bubble point

In blowout simulations of proposed (not yet drilled) oil wells  in the Gulf of Mexico (Worst Case Discharge, aka WCD) a simple radial reservoir simulation model is assumed and flowing pressure bottom hole pressures  are calculated.  The rates often are very large (<200,000 BOPD).  All commercial  reservoir simulators are formulated using Darcy's Law which is limited to laminar flow.  The problem with using these simulators is that a significant error in flowing bottom-hole pressure is realized due to the simulator not being able to model turbulent flow in the porous media in the near wellbore vicinity.  Estimates of the Reynold's number in this near wellbore region indicate turbulent flow is occurring.  As a result of errors in estimating bottom-hole pressure, inaccurate flowing pressure gradients result.  These flowing pressure gradients are used as input in determine collapse of proposed casing strings.  

Can Tough2 model turbulent flow in porous media for a liquid (e.g. oil above bubble point)?