Granted Patent B2

US 12,521,677 · App. 17/639,493 · Granted Jan 13, 2026

Inventors: Peter Sendelius (Staffanstorp, SE); Henrik Lindgren (Genarp, SE); Carl-Henry Örndal (Eslöv, SE)

Assignees: Baxter International Inc.; Baxter Healthcare SA

B01D61/12C02F1/441B01D2311/246B01D2311/2512B01D2313/18B01D2313/243C02F2209/001C02F2209/005C02F2209/05C02F2209/40C02F2301/046

Abstract

Claims (32)

1 . A water purification apparatus configured to provide a stable permeate conductivity, the apparatus comprising:

a fluid path;

a feed pump configured to receive inlet water, and to provide feed water;

a reverse osmosis membrane, wherein the reverse osmosis membrane is configured to receive feed water from the feed pump, and to produce permeate water and reject water;

a quality sensor configured to measure an inlet water conductivity;

a flow rate sensor configured to measure a product water flow rate, wherein the product water is permeate water that is delivered for consumption;

a recirculation path configured to recirculate a first portion of the reject water to an inlet path or to a feed path;

a drain valve configured to regulate a drain flow rate to a drain, from a second portion of the reject water; and

a control arrangement configured to:

receive, from the quality sensor, the inlet water conductivity;

determine a target recovery for water purification based on the inlet water conductivity, wherein the target recovery defines a target ratio for product water flow rate to inlet water flow rate, wherein the inlet water flow rate is determined as the sum of product water flow rate and drain flow rate;

control, based on the inlet water conductivity, a feed pump speed of the feed pump to either (i) a predetermined speed at which the feed pump works most efficiently, or (ii) a speed determined based on a relation between the feed pump speed, the inlet water conductivity and a target permeate water conductivity, and wherein the feed pump speed is controlled such that the target permeate water conductivity is achieved for the determined target recovery; and

control the drain flow rate of the drain valve to drain, such that the target recovery is achieved based on the product water flow rate.

2 . The water purification apparatus according to claim 1 , wherein the control arrangement is configured to determine a drain flow rate needed to accomplish the target recovery, based on the product water flow rate, and to control the drain flow rate to be the determined drain flow rate.

3 . The water purification apparatus according to claim 1 , wherein the control arrangement is configured to determine the target recovery with a limitation that a permeate water conductivity is maintained at a predetermined permeate water conductivity, or within a predetermined permeate water conductivity interval.

4 . The water purification apparatus according to claim 1 , comprising a permeate recirculation path arranged between a recirculation point in the permeate path and the inlet path, such that the permeate recirculation path recirculates a portion of the permeate water from the recirculation point to the inlet path.

5 . The water purification apparatus according to claim 4 , wherein the control arrangement is configured to control recirculation so as to meet a product water flow rate criterion including that the product water flow rate is equal to, or close to equal to, a predetermined product water flow rate, based on the property indicative of a flow rate of a product water.

6 . The water purification apparatus according to claim 1 , wherein the relation between the feed pump speed, the inlet water conductivity and the target permeate water conductivity is a predetermined relation, and wherein an output of the predetermined relation is a feed pump speed needed to produce permeate water with the target permeate conductivity at the inlet water conductivity and the target recovery.

7 . The water purification apparatus according to claim 1 , wherein the control arrangement is configured to determine a target recovery,

wherein the target recovery is determined to be a constant first value while the inlet water conductivity C inlet is in a lower interval,

wherein the target recovery is determined according to a linear relationship between the target recovery and the inlet water conductivity while the inlet water conductivity C inlet is within a middle interval, and

wherein the target recovery is determined to be a constant second value while the inlet water conductivity C inlet is in an upper interval, wherein the second value is lower than the first value, and wherein the target recovery in the middle interval is between the first value and the second value.

8 . The water purification apparatus according to claim 1 , wherein the quality sensor is a conductivity cell, and the conductivity indicative of an inlet water conductivity is a conductivity of the inlet water, conductivity of the feed water, or conductivity of the permeate water.

9 . The water purification apparatus according to claim 1 , wherein the control arrangement is configured to:

determine an initial drain flow rate through the drain valve when the drain valve is fully open towards drain;

determine a proportion the drain valve should be open towards drain, based on the initial drain flow rate and a determined flow rate; and

control the drain valve based on the determined proportion.

10 . A non-transitory, computer-readable medium storing instructions, which when executed by a processor of the control arrangement according to claim 1 , cause the processor to:

receive, from the quality sensor, the inlet water conductivity;

determine a target recovery for the water purification based on the inlet water conductivity, wherein the target recovery defines a target ratio for product water flow rate to inlet water flow rate, wherein the inlet water flow rate is determined as the sum of product water flow rate and drain flow rate;

control, based on the inlet water conductivity, the feed pump speed of the feed pump to either (i) a predetermined speed at which the feed pump works most efficiently, or (ii) a speed determined based on a relation between the feed pump speed, the inlet water conductivity and the target permeate water conductivity, and wherein the feed pump speed is controlled such that the target permeate water conductivity is achieved for the determined target recovery; and

control the drain flow rate of the drain valve to drain, such that the target recovery is achieved based on the product water flow rate.

Assignments (5)

Priority Claims (1)

Continuity (1)

References Cited (13)