Read your pump curve, and see what HP is required at the flows you are running, and then compare your electrical data, as recommended above, to what the pump should be using at that operating point.
If for nothing else, it should serve as a check and balance on your electrical work.
Part of your evaluation regarding whether or not you want to sell the power vs run plant equipment has to do with whether or not the same steam that the BFPT's would use to do this work is best used in the BFPT, or the main turbine.
In some cases the steam not extracted messes up the volumetric efficiency of the main steam turbine stages down stream of the extraction point, and contributes to exit losses at the hoods into the condenser. In other cases, it is actually beneficial. Depends upon your particular turbine.
Bottom line, if your BFPT efficiency is at all near the efficiency of the lower stages of the main turbine, ignoring things like exit losses, etc., it is more efficient to do the work with extracted steam, since to make this into electricity and run the motor adds all the electrical losses to the system before the work is applied to the pump. On the other hand, BFPT's are seldom as efficient as MST's. So, get out the Mollier Dia.
rmw