I don't how what your vacuum column is going to look like, what product specs you put on LVGO and HVGO.
If there is no fractionation between LVGO and HVGO, which is usually the case, then you can use 2 theoretical stages for the LVGO pumparound, 2 theoretical stages for the HVGO pumparound, 2 or 3 theoretical stages for the wash section (between HVGO draw and column feed) and 1 or 2 theoretical stages for the stripping section (below column feed).
If you want to improve (for whatever reason) the separation between LVGO and HVGO then you add 1 or 2 or even 3 theoretical stages between the LVGO PA and HVGO PA stages.
To recover some gasoil that was left in the topped crude you could add a section above the LVGO PA consisting of a Top PA (2 theoretical stages) and a fractionation section of 2 or 3 theoretical stages between TPA and LVGO PA.
It is your design so you can play with the number of theoretical stages to achieve what you consider to be the optimum design.