Water treatment system using mechanical vapour compression
A water treatment system comprising a mechanical vapour compression apparatus ( 11 ), the mechanical vapour apparatus having a evaporation/condensation vessel ( 11 a ) and a recirculation circuit ( 20 ) whereby recirculated water is pumped from an outlet ( 18 a ) of the evaporation/condensation vessel ( 11 A) to an inlet ( 18 B) of the evaporation/condensation vessel ( 11 A), wherein the recirculation circuit ( 20 ) comprises a fluidized bed crystallizer ( 22 ), and at least part of the recirculated brine is passed through the fluidized bed crystallizer ( 22 ) to remove dissolved minerals therefrom.
1. A method of treating water, comprising:
supplying feed water to a mechanical vapour compression apparatus having an evaporation/condensation vessel,
receiving recirculation water from an outlet of the evaporation/condensation vessel,
passing at least part of the recirculation water through a fluidized bed crystallizer to remove dissolved minerals from the at least part of the recirculation water, thereby enabling higher operating temperatures in the evaporation/condensation vessel, and
supplying the recirculation water to an inlet of the evaporation/condensation vessel.
2. The method of claim 1 wherein the dissolved minerals comprise one or more of magnesium compounds and calcium compounds.
3. The method of claim 1 further comprising receiving removed dissolved minerals from the fluidized bed crystallizer.
4. The method according to claim 1 further comprising receiving feed water, supplying the feed water to a deaerator, and passing at least some of the feed water from the deaerator to the fluidized bed crystallizer.
5. The method according to claim 1 further comprising post-treating product water from the mechanical vapour compression apparatus, receiving product water from the mechanical vapour compression apparatus, and reintroducing dissolved minerals from the fluidized bed crystallizer to the product water.
6. The method according to claim 1 wherein the higher operating temperatures comprise temperatures that would precipitate at least one of the dissolved minerals from the at least part of the recirculation water.
7. The method according to claim 1 wherein the dissolved minerals comprise calcium carbonate, and wherein the higher operating temperatures comprise temperatures that would precipitate the calcium carbonate.