Pure chlorine dioxide generation system with reduced acid usage

Patent metadata

Field	Value
Publication number	US-12098070-B2
Application number	US-202318336411-A
Country	US
Kind code	B2
Filing date	Jun 16, 2023
Priority date	Apr 2, 2019
Publication date	Sep 24, 2024
Grant date	Sep 24, 2024

Abstract

A method of producing chlorine dioxide is disclosed. The method may include feeding a reaction mixture into a separator. The reaction mixture may follow a helical path through the separator and produce gaseous chlorine dioxide within the separator. Gaseous chlorine dioxide may be withdrawn from the separator and used to disinfect process water.

First claim

What is claimed is:

1. A method of producing chlorine dioxide, comprising:
mixing a first solution and a second solution in a mixing device to form a reaction mixture;
feeding the reaction mixture into a separator;
directing the reaction mixture in a helical path through the separator;
reacting the first solution with the second solution to produce gaseous chlorine dioxide within the separator; and
withdrawing the gaseous chlorine dioxide from the separator;
wherein the helical path is defined by a plurality of plates disposed within the separator, and wherein the helical path is defined by a tube having a coiled configuration having a coil plane angle of about 1 degree to about 60 degrees.

2. The method of claim 1 , further comprising:
feeding the first solution comprising an acid through a first feed line into the mixing device; and
feeding the second solution comprising chlorite or chlorate through a second feed line into the mixing device;
wherein the mixing device is in fluid communication with the separator.

3. The method of claim 2 , wherein the acid is hydrochloric acid, phosphoric acid, sulfuric acid, hypochlorous acid, or any combination thereof.

4. The method of claim 2 , wherein the acid comprises sulfuric acid and the second solution comprises chlorate and hydrogen peroxide.

5. The method of claim 2 , wherein the acid comprises hydrochloric acid and the second solution comprises chlorite.

6. The method of claim 2 , wherein the first feed line and the second feed line are opposite to and directed against each other.

7. The method of claim 1 , wherein the separator is operated at a pressure about equal to or less than atmospheric pressure.

8. The method of claim 1 , wherein the reaction mixture has a residence time in the separator of about 0.1 minute to about 1 hour.

9. The method of claim 1 , further comprising producing the chlorine dioxide at a rate ranging from about 0.001 lb/hour to about 200 lb/hour.

10. The method of claim 1 , further comprising operating the separator at a temperature ranging from about 2° C. to about 80° C.

11. The method of claim 1 , wherein the reaction mixture is fed into a top portion of the separator.

12. The method of claim 1 , wherein the reaction mixture is fed into a bottom portion of the separator.

13. The method of claim 1 , wherein the reaction mixture is fed into a middle portion of the separator.

14. The method of claim 1 , further comprising withdrawing liquid from the separator and recycling the liquid to the separator.

15. The method of claim 1 , wherein the plurality of plates comprises a plate having perforations.

16. The method of claim 1 , wherein an average conversion efficiency is at least about 90%.

17. A method of producing chlorine dioxide, comprising:
mixing a first solution and a second solution in a mixing device to form a reaction mixture;
feeding the reaction mixture into a separator;
directing the reaction mixture in a helical path through the separator;
reacting the first solution with the second solution to produce gaseous chlorine dioxide within the separator; and
withdrawing the gaseous chlorine dioxide from the separator;
wherein the helical path is defined by a plurality of plates disposed within the separator, and wherein the plurality of plates comprises a plate having perforations.

Assignees

• Ecolab Usa Inc

Inventors

• Xiong Kun
• Denny Nicholas R
• Dalke Shawn

Classifications

• C02F1/68

  by addition of specified substances, e.g. trace elements, for ameliorating potable water (medicinal water A61K) · CPC title

• C01B11/026 Primary

  from chlorate ions in the presence of a peroxidic compound, e.g. hydrogen peroxide, ozone, peroxysulfates · CPC title

• C02F1/76

  with halogens or compounds of halogens {(C02F1/4674 takes precedence)} · CPC title

• C01B11/023

  Preparation from chlorites or chlorates · CPC title

• C01B11/024 Primary

  from chlorites · CPC title