Electrodeionization device and pure-water production system

Patent metadata

Field	Value
Publication number	US-10252218-B2
Application number	US-201615540198-A
Country	US
Kind code	B2
Filing date	Feb 15, 2016
Priority date	Feb 17, 2015
Publication date	Apr 9, 2019
Grant date	Apr 9, 2019

Abstract

An electrodeionization device having an improved boron rejection capability compared with high-performance electrodeionization devices proposed in the related art is provided. An electrodeionization device comprising a cathode; an anode; and a plurality of cation-exchange membranes and a plurality of anion-exchange membranes, the plurality of cation-exchange membranes and the plurality of anion-exchange membranes being arranged between the cathode and the anode so as to form concentrating compartments and desalting compartments, the concentrating compartments and desalting compartments being arranged alternately, the desalting compartments being filled with an ion-exchange resin, wherein the ion-exchange resin has an average particle size of 100 to 300 μm. Preferably, the ion-exchange resin has a uniformity coefficient of 1.1 or less.

First claim

The invention claimed is:

1. An electrodeionization device, comprising:
a cathode;
an anode; and
a plurality of cation-exchange membranes and a plurality of anion-exchange membranes, the plurality of cation-exchange membranes and the plurality of anion-exchange membranes being arranged between the cathode and the anode so as to form concentrating compartments and desalting compartments, the concentrating compartments and desalting compartments being arranged alternately, the desalting compartments being filled with an ion-exchange resin,
wherein the ion-exchange resin has an average particle size of 150 to 250 μm,
the ion-exchange resin has a uniformity coefficient of 1.1 or less,
the ion-exchange resin is a resin mixture of an anion-exchange resin and a cation-exchange resin,
the ion-exchange resin on an entry side of the desalting compartments in a water-flow direction is a resin mixture of an anion-exchange resin and a cation-exchange resin at a ratio of Anion-exchange resin:Cation-exchange resin=60 to 90:40 to 10 (dry weight ratio), and
the ion-exchange resin on an exit side of the desalting compartments is a resin mixture of an anion-exchange resin and a cation-exchange resin at a ratio of Anion-exchange resin:Cation-exchange resin=40 to 60:60 to 40 (dry weight ratio).

2. The electrodeionization device according to claim 1 , wherein the concentrating compartments are filled with an ion-exchange resin having an average particle size of 100 to 300 μm.

3. The electrodeionization device according to claim 2 , wherein the ion-exchange resin filled in the concentrating compartments has a uniformity coefficient of 1.1 or less.

4. The electrodeionization device according to claim 2 , wherein the ion-exchange resin filled in the concentrating compartments is a resin mixture of an anion-exchange resin and a cation-exchange resin.

5. The electrodeionization device according to claim 4 , wherein the ion-exchange resin filled in the concentrating compartments is a resin mixture of an anion-exchange resin and a cation-exchange resin at a ratio of Anion-exchange resin:Cation-exchange resin=40 to 70:60 to 30 (dry weight ratio).

6. A method for producing deionized water using the electrodeionization device according to claim 1 , the method comprising:
passing water to be treated through the desalting compartments of the electrodeionization device;
passing part of water discharged from the desalting compartments through the concentrating compartments in a direction opposite to a direction in which the water-to-be-treated is passed through the desalting compartments; and
discharging the remainder of the water discharged from the desalting compartments as treated water.

7. A pure-water production system comprising the electrodeionization device according to claim 1 , and a reverse-osmosis membrane separation device disposed upstream of the electrodeionization device.

8. The electrodeionization device according to claim 1 , wherein each of the desalting compartments is defined between an adjacent pair of the anion-exchange membrane and the cation-exchange membrane, and each of a thickness of the desalting compartments and the concentrating compartments is 2.0 to 8.0 mm.

9. The method according to claim 6 , wherein the water to be treated contains boron,
a boron concentration in the water to be treated is 10-20 ppb, and
a boron concentration in the treated water is 1 ppt or less.

Assignees

• Kurita Water Ind Ltd

Inventors

• Sato Shin
• Miyazaki Yoichi

Classifications

• C02F1/52

  by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} · CPC title

• C02F1/283

  using coal, charred products, or inorganic mixtures containing them · CPC title

• B01D61/025

  Reverse osmosis; Hyperfiltration · CPC title

• B01D61/485

  Specific features relating to the ion-exchange material · CPC title

• C02F1/42

  by ion-exchange (ion-exchange in general B01J) · CPC title