Controlled precipitation of struvite from postdigestion, sludge lagoon supe
rnatant was studied using a pilot scale fluidized bed reactor (FBR). The pr
ocess effectively and rapidly removed struvite constituents from the supern
atant and produced effluent significantly undersaturated for struvite. Rece
ntly published information on struvite thermodynamic and kinetic properties
was incorporated into the FBR system design and selection of components. S
truvite crystals were selected as seed media, which enabled precipitation o
f nearly pure crystals and allowed nucleation, with its associated lag time
, to be bypassed. Mixing energy in the FBR was demonstrated to be sufficien
t to overcome transport limitations to struvite growth, allowing growth kin
etics to be governed by the surface integration rate of constituent ions in
to the growing crystal lattice structure. Struvite removal was optimized by
incorporating pH elevation into the FBR system. Process fluid was circulat
ed in the pH adjustment tank/FBR system, which was configured as a continuo
us feed stirred-tank reactor. Struvite removal efficiency exceeded 80% in c
ontinuous feed experiments where the hydraulic detention time exceeded 1 h.