The best way to acheive your goal of <0.3 mg/L iron at 50 gpm is to use a pressure vessel filled with 24" of silica sand and a 6" anthracite cap.
Inject chlorine ahead of the filter(s)in a dosage sufficient to carry a residual of free chlorine after the filter(s).
Backwash the filter(s) whenever the pressure loss exeeds 25 psid or sooner if necessary.
If you have at least 238 gpm (15 gpm/sf loading rate) available for backwash, then a single 54" diameter by 60" side shell vessel should be adequate. If you only have the 50 gpm available for backwash from the well, then use five 24" diameter by 60" side shell vessels in parallel. Backwash each filter sequentially for 10 minutes each.
Manganese Greensand has a typical life of 5 - 7 years where as silica sand will last indefinitely in your application. Greensand media is fragile and cannot be operated in excess of 12 psid max. Greensand requires potassium permanganate feed, in addition to chlorine for disinfection residual, where as silica sand only requires chlorine. Manganese Greensand costs 8 times more than silica sand and costs more to operate.
Water softeners should not be used for iron removal. Ten States Standards and most health departments and regulatory agencies specifically exclude ion exchange softeners from consideration for iron removal. Ion exchange resin manufacturers typically require the feedwater to be virtually free of iron for warranty purposes. Using an ion exchange softener for iron removal would require that the total flow be passed through the treatment system without any bypass blending. This would result in very low hardness water in the distribution system that could result in problems with lead and copper leaching as well as corrosion of piping.
In addition, you should consult with your local regulatory agency for further advice and/or seek professioal assistance from a registered professional engineer with municipal water experience.
S. Bush