In vacuum crystallization
process, raw salt is dissolved in water to make a saturated
solution and sent to clarifier wherein bulk of insoluble
impurities settles down and is removed from the bottom.
Solution transferred from the clarifier is filtered and pumped
to treatment vessels for precipitation to the extent
required by means of chemical reaction. Precipitated mass is
filtered out and the solution thus purified is pre-heated
and subjected to continuous evaporation on being heated with
steam. For economizing the steam consumption, multiple units
are used in series, so that the steam coming out from one
unit, be used in the next effect, thus eliminating the need
for application of fresh steam at each stage. Vapour from
the last effect is condensed in a condenser using water from
cooling tower. The entire plant initially is under vacuum,
and thereafter the pressure in the system is
thermodynamically stabilized. Vacuum is generated by using a
suitable Vacuum Pump. The number
of effects depends upon the capacity of the plant, so that
optimized economy is achieved at minimum investment.
Depending upon the requirement, the system can be of forced
circulation type or falling film type. Each effect consists
of an External Calendria,
circulation pump, Vapour Separator
(Flash Chamber) and entrainment separator. The salt
solution is continuously circulated through external
calendria and the superheated liquid is flashed in flash
chambers for separating vapour. The vapour is freed from
entrainment in the separator and then fed to next effect
which serves as heating medium. The vapour from last effect
is sent to a direct contact Steam
Condenser where it gets mixed up with water from
cooling tower, and serves as make up water. Vapour from
earlier effects are condensed, and collected as pure water.
Hence, a properly designed vacuum
crystallizer is capable of simultaneously producing pure
vacuum salt and pure water. This makes the whole process
much more economically viable.
As the evaporation proceeds, salt starts crystallizing, and
the slurry formation takes place. Slurry is continuously
withdrawn from the evaporators and fed to centrifuge through
a thickener.
Mother liquor from centrifuge is recycled to evaporator, and
centrifuged salt is blended with crystal habitat modifiers,
dried, graded, blended with additives including
suitable quantity of a free flowing agent, and then finally
packed.














