Beside the already mentioned criteria the design of the crystallization processes is influenced by several additional factors. These are:

SURFACE-COOLING CRYSTALLIZATION


The surface-cooling produces supersaturations directly on the heat exchanger surface. This supersaturation is the highest in the entire crystallizer. Incrustations of the cooling surface and a limitation of the plant operation are the normal consequences. That can be accepted for discontinuous operation, because with the next batch all the incrustations get dissolved again. For continuous processes the surface cooling is only decided for, if too low operating pressures make vacuum cooling crystallization uneconomically. One reason could be a high boiling point elevation. In that cases especial large heat exchanger surface are chosen.

VACUUM-COOLING CRYSTALLIZATION


Vacuum-cooling crystallization is the preferred cooling crystallization method under continuous operation. Because cooling is generated by adiabatic expansion of the solvent no cooling surfaces can be incrusted. Vacuum-cooling becomes uneconomical only if cooling has to be effected at very low temperatures.

EVAPORATION CRYSTALLIZATION


The evaporation crystallization is a vacuum process as well as the vacuum-cooling crystallization. Differing from the vacuum-cooling this process method is independently from the concentration and temperature of the feed solution. External heat can be added to the system and the concentration of mother liquor can be adjusted independently. Like vacuum-cooling crystallization there are no special incrustation problems in evaporation crystallization if boiling on the heater surface is prevented. Some difficulties may arise for inverse soluble substances, like the hardeners. In those cases it has to be taken care as explained for the surface-cooling crystallization. High velocities of the suspension flow and a high suspension density can be helpful by erosion and faster desupersaturation behaviour. For a better process economy the units are constructed as multiple-effect evaporation plants.