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IntroductionAlthough industrial applications of precipitation have a long history and precipitation has been studied scientifically since the 1930s, understanding of this operation is still ver y limited 1) . Industrially, precipitation reactions are generally carried out in ver y simple reactor systems. Probably over 90% of industrial precipitation processes are carried out in ordinary stirred tank reactors operated either batchwise or continuously 2) . Major problems, however, often occur in control of precipitation processes, specifically in understanding the effect of processing conditions on reactor performance and product characteristics such as precipitate morphology, purity and particle size distribution 3,4,1) . In addition, the design of industrial crystallisers is still experience-based 5) , and geometric and time-dependent variations are not taken into account. It is therefore hardly surprising that these strategies fail almost without exception 6) .The problem is even more challenging in the field of industrial precipitation, where the default reactor design is a simple stirred tank, invariably quite inadequate for product control. A significant amount of research has been conducted into the development of more efficient precipitation processes. The development of the seeded fluidised bed, or pellet reactor, offers a number of potential advantages over conventional precipitation options. The technology was initially employed for the softening of drinking water by calcium carbonate precipitation 7) and the removal of phosphates from waste water, producing calcium phosphate 8) . More recently, fluidised bed reactors have been used for the removal of metals (nickel, copper and zinc) from solution 9, 10, 11, 12) as carbonates or as sulphides. Kaksonen and co-workers 13) used biologically generated sulphide and alkalinity as the reagents to precipitate zinc and iron from acidic waste water in a fluidised bed reactor, whilst Esposito and co-workers 14) used the same sulphide source but precipitated only zinc from acidic waste water. ), the fines formed immediately but never aggregated onto the seed material and it was not possible to control the supersaturation levels to the extent that fines formation was avoided.
Fines Formation (and Prevention) in Seeded Precipitation Processes Abstract