Low risk chlorine dioxide onsite generation system

Patent metadata

Field	Value
Publication number	US-11130677-B2
Application number	US-201815928435-A
Country	US
Kind code	B2
Filing date	Mar 22, 2018
Priority date	Mar 24, 2017
Publication date	Sep 28, 2021
Grant date	Sep 28, 2021

Abstract

The present disclosure generally relates to producing chloride dioxide. A chlorine dioxide reactor, methods for producing chlorine dioxide, and treating aqueous systems are disclosed. The reactor may include a mixing device, a first feed line in fluid communication with the mixing device, and a second feed line in fluid communication with the mixing device. The reactor may include a proximal portion in fluid communication with the mixing device and a distal portion in fluid communication with a motive water line. The mixing device, the reactor, a portion of the first feed line, and a portion of the second feed line may be positioned within the motive water line.

First claim

What is claimed is:

1. A method of producing chlorine dioxide, comprising:
feeding a first solution comprising an acid through a first feed line into a mixing device;
feeding a second solution comprising chlorite through a second feed line into the mixing device;
mixing the first solution and the second solution in the mixing device to form a reaction mixture, wherein the mixing device is in fluid communication with a reactor;
feeding the reaction mixture into the reactor;
reacting the acid and the chlorite in the reactor, wherein the reactor comprises a proximal portion in fluid communication with the mixing device and a distal portion in fluid communication with a motive water line, wherein the mixing device, the reactor, a portion of the first feed line, and a portion of the second feed line are positioned within the motive water line; and
mixing chlorine dioxide with motive water in the motive water line at the distal portion of the reactor,
wherein the motive water line is a double containment pipe having an inner channel separated from an outer channel, wherein the reactor is disposed within the inner channel and the motive water flows through the inner and outer channel and the chlorine dioxide mixes with the motive water flowing through the inner channel and outer channel at the distal portion of the reactor.

2. The method of claim 1 , wherein the acid is hydrochloric acid, phosphoric acid, sulfuric acid, hypochlorous acid, or any combination thereof.

3. A method of treating process water, comprising: producing chlorine dioxide according to claim 1 ; and injecting the mixture of the chlorine dioxide and the motive water into the process water.

4. The method of claim 1 , further comprising cooling the mixing device and the reactor with the motive water.

5. The method of claim 1 , wherein the reactor comprises a coiled configuration having a coil plane angle of about 1 degree to about 60 degrees.

6. The method of claim 1 , 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 reactor is operated at a pressure about equal to or greater than atmospheric pressure.

8. The method of claim 1 , wherein the reaction mixture has a residence time in the reactor of at least about 0.1 minute, and a precursor velocity is at least about 25 cm/min, wherein the precursor velocity is a velocity of the first and second solutions.

9. The method of claim 1 , further comprising producing the chlorine dioxide at a rate ranging from about 0.001 lb/hour to about 20 lb/hour.

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

11. The method of claim 3 , wherein injecting the mixture of chlorine dioxide and motive water into the process water of a cooling tower.

12. A method of producing chlorine dioxide, comprising:
feeding a first solution comprising an acid through a first feed line into a mixing device;
feeding a second solution comprising chlorite through a second feed line into the mixing device;
mixing the first solution and the second solution in the mixing device to form a reaction mixture, wherein the mixing device is in fluid communication with a reactor;
feeding the reaction mixture into the reactor;
reacting the acid and the chlorite in the reactor, wherein the reactor comprises a proximal portion in fluid communication with the mixing device and a distal portion in fluid communication with a motive water line, wherein the mixing device, the reactor, a portion of the first feed line, and a portion of the second feed line are positioned within the motive water line; and
mixing chlorine dioxide with motive water in the motive water line at the distal portion of the reactor,
wherein the acid is phosphoric acid, sulfuric acid, hypochlorous acid, or any combination thereof,
wherein the motive water line is a double containment pipe having an inner channel separated from an outer channel, wherein the reactor is disposed within the inner channel and the motive water flows through the inner and outer channel and the chlorine dioxide mixes with the motive water flowing through the inner channel and outer channel at the distal portion of the reactor.

13. The method of claim 1 , wherein the reactor has an inner diameter ranging from about 0.1 inches to about 4 inches.

Assignees

• Ecolab Usa Inc

Inventors

• Xiong Kun
• Dimascio Felice
• Denny Nicholas Ryan
• Dalke Shawn

Classifications

• C01B11/026

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

• C01B11/024 Primary

  from chlorites · CPC title

• B01J14/00

  Chemical processes in general for reacting liquids with liquids; Apparatus specially adapted therefor (B01J8/00, B01J19/08 take precedence) · CPC title