I suggest you remove as much ...

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I suggest you remove as much P as possible biologically and then trim with ferric downstream. If you dose ferric upstream at the headworks a significant proportion will react with sulphide and form insoluble iron sulphide, which may block your MBR. Any ferric consumed reacting with sulphide will be also be lost to phosphate removal and cost you more money. With a conventional SBR system I normally achieve 80% phosphate removal biologically.

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I don't have a lot of experience in this area but we took this approach when implementing this in an SBR. The idea was that biological P removal was 'free' and that we didn't want to remove too much P too early on as we could run the risk of the biomass growth being limited by P.

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