Water softener system and method of operating the same

Patent metadata

Field	Value
Publication number	US-12515214-B2
Application number	US-202217737274-A
Country	US
Kind code	B2
Filing date	May 5, 2022
Priority date	Jun 28, 2021
Publication date	Jan 6, 2026
Grant date	Jan 6, 2026

Abstract

A water softener system includes a brine tank, an ion-exchange resin and a softener control valve fluidly coupling the brine tank and the ion-exchange resin. The softener control valve has an inlet configured to receive a flow of feed-water and an outlet configured to deliver a flow of product water. A flow meter is configured to monitor a flow rate of water to or from the control valve, and a sensor is arranged upstream of the inlet of the softener control valve to measure a fluid property of the flow of feed-water. A controller is configured to calculate an available exchange capacity of the ion-exchange resin using flow rate data from the flow meter and a hardness value of the feed-water, which the controller calculates using a fluid property value from the sensor and a predetermined coefficient. The controller is also configured to initiate a regeneration of the ion-exchange resin using the brine tank and the softener control valve, and to update the predetermined coefficient based at least partially on the calculated available exchange capacity upon initiating the regeneration.

First claim

What is claimed is:

1 . A method of operating a water softener system, comprising:
passing feed-water received into the water softener system through an ion-exchange resin to produce product water; determining a hardness indication value of the product water; monitoring a cumulative amount of water that has been passed through the ion-exchange resin since a last regeneration of the ion-exchange resin; calculating an available exchange capacity of the ion-exchange resin based at least in part on the cumulative amount of water, wherein calculating an available exchange capacity of the ion-exchange resin includes measuring a feed-water conductivity value of the water prior to softening the water and calculating a feed-water hardness value using the feed-water conductivity value, and wherein calculating the feed-water hardness value comprises multiplying the feed-water conductivity value by a coefficient; regenerating the ion-exchange resin when either of a first criterion and a second criterion is met, wherein the first criterion is met when the hardness indication value of the product water exceeds a predetermined limit and wherein the second criterion is met when the available exchange capacity is less than a predetermined reserve capacity, and updating the coefficient when the first criterion or the second criterion is met.

2 . The method of claim 1 , wherein determining a hardness indication value of the product water comprises:
measuring a first conductivity value of the product water; passing a portion of the product water through a filtration membrane; measuring a second conductivity value of said portion of the product water after having been passed through the filtration membrane; and calculating the hardness indication value using the first and second conductivity values.

3 . The method of claim 1 , wherein updating the coefficient results in the calculated feed-water hardness value decreasing when the second criterion is met but the first criterion is not met, and results in the calculated feed-water hardness value increasing when the first criterion is met but the second criterion is not met.

4 . The method of claim 1 , wherein calculating the available exchange capacity of the ion-exchange resin further comprises:
calculating an estimated used exchange capacity using the feed-water hardness value and the cumulative amount of water; and subtracting the estimated used exchange capacity from a predetermined total exchange capacity of the ion-exchange resin.

5 . The method of claim 4 , further comprising:
comparing the estimated used exchange capacity to a stored value of a previous used exchange capacity, the stored value having been calculated prior to the last regeneration of the ion-exchange resin; determining whether the estimated used exchange capacity is less than the stored value by at least a threshold amount; and delivering an error message when the estimated used exchange capacity is less than the stored value by at least the threshold amount.

6 . The method of claim 1 , wherein the predetermined reserve capacity is greater than zero.

7 . The method of claim 5 , wherein the threshold amount is a first threshold amount, the method further comprising determining whether the estimated used exchange capacity is less than the stored value by at least a second threshold amount, the second threshold amount being greater than the first threshold amount.

8 . The method of claim 7 , wherein the error message is a message indicating that a brine tank of the water softener system needs to be refilled with salt when the estimated used exchange capacity is less than the stored value by at least the first threshold amount but is not less than the stored value by at least the second threshold amount.

9 . The method of claim 7 , wherein the error message is a message indicating that a faulty regeneration has occurred when the estimated used exchange capacity is less than the stored value by at least the second threshold amount.

Assignees

• Smith Corp A O

Inventors

• Averbeck David Jeffrey
• Zhou Guihua

Classifications

• C02F2303/16

  Regeneration of sorbents, filters · CPC title

• C02F2209/445

  Filter life · CPC title

• C02F2209/40

  Liquid flow rate · CPC title

• C02F2209/055

  Hardness · CPC title

• C02F2209/006

  comprising a software program or a logic diagram · CPC title