Water treatment method
View Patent ↗A water treatment system for removing hard ions from source water. The water treatment system is of the type that includes a pair of ion-exchange water softener tanks connectable to a source of pressurized water and with a water system to supply softened water to the water system, the tanks each being capable of regeneration by flushing with a regeneration solution to replenish depleted ions. A process for preventing system failure due to salt crystallization includes flowing water during brine replenishment from a second nozzle and a first nozzle at a defined ratio. The first nozzle diluted the brine in a reservoir after regeneration cycle is complete. The second nozzle replenishes brine by flowing water directly onto a salt material.
1. A method of operating a water treatment system that includes a pair of ion-exchange water softener tanks connectable to a source of pressurized water and with a water system to supply softened water to the water system, the tanks each being capable of regeneration by flushing with a regeneration solution to replenish depleted ions, the method of operating the water treatment system, comprising:
a) regenerating a selected one of the tanks with a brine solution wherein hard ions are removed from a resin in the tank and exchanged with soft ions, the brine solution being contained in a container in communication with the selected tank wherein the container includes a salt material disposed on a screen above a brine reservoir and further includes a brine well in communication with the brine reservoir, the brine reservoir defining the brine solution;
b) replenishing brine after the tank regeneration cycle is complete wherein the step of replenishing the brine includes;
(i) flowing water from a first nozzle directly into a brine well of the system for initially diluting the brine in the reservoir, and
(ii) flowing water from a second nozzle directly onto a salt material for generating additional brine solution in the reservoir.
2. The method according to claim 1 , wherein the water flow rate through the second nozzle is in the range of about four times to about eight times the water flow rate through the first nozzle.
3. The method according to claim 1 , wherein the flow rate of water through the second nozzle is about six times greater than the flow rate of water flowing through the first nozzle.