Electrolytic method of generating chloride dioxide with improved theoretical yield

Patent metadata

Field	Value
Publication number	US-10046990-B2
Application number	US-201113153656-A
Country	US
Kind code	B2
Filing date	Jun 6, 2011
Priority date	Jun 6, 2011
Publication date	Aug 14, 2018
Grant date	Aug 14, 2018

Abstract

The invention is directed to an apparatus and methods of its use to generate chlorine dioxide. The apparatus comprises three cation exchange resin chambers in fluidic communication to convert chlorite salt into chlorine dioxide. Unlike previous converters, the invention utilizes an novel method of acidifying some of the chlorite to produce a more effective process. The invention can achieve a 100% theoretical yield which is s significant improvement over the 80% theoretical yield in previous attempts using non-acidifying chemistry. The method also avoids the need for expensive catalysts.

First claim

What is claimed is:

1. A method of generating a disinfectant, the method comprising:
feeding sodium chlorite and sodium hypochlorite into a central chamber of an apparatus, the apparatus comprising:
three chambers consisting of a first chamber, a second chamber, and a third chamber, the second chamber being the central chamber positioned between the first and third chambers and in fluid communication with the first and third chambers through water-permeable membranes, and each of the three chambers being filled with cation exchange resin; and
an anode disposed in the first chamber and a cathode disposed in the third chamber in electrical communication with the anode,

feeding water into at least one of the chambers of the apparatus, and
feeding a current into the apparatus to produce an output of chlorine dioxide from the central chamber, and
periodically decreasing or turning off a flow of the sodium chlorite into the apparatus to produce an output of elemental chlorine or a combination of elemental chlorine and chlorine dioxide in the absence of a catalyst,
wherein the chlorine dioxide is produced by a reaction where only water reacts at the anode and cathode, and the sodium chlorite and sodium hypochlorite are converted first into chlorous acid and hypochlorous acid and then into chlorine dioxide in the central chamber and the reaction takes place without the addition of an inorganic acid.

2. The method of claim 1 wherein when sodium chlorite and sodium hypochlorite are both fed, the sodium chlorite and sodium hypochlorite are fed at a ratio of 2:1.

3. The method of claim 1 further comprising buffering at least one of the chlorite salts in caustic prior to its entry into the apparatus.

4. The method of claim 1 further comprising sequentially adding the output of chlorine dioxide and the output of elemental chlorine or combination of elemental chlorine and chlorine dioxide into an aqueous stream for disinfecting.

5. The method of claim 4 in which the chlorine dioxide and elemental chlorine are added according to an interactive disinfection regimen.

6. The method of claim 5 in which the chlorine dioxide is added to a system which is subject to spray or agitation.

7. The method of claim 5 in which the elemental chlorine increases the amount of chlorine dioxide according to a recycle effect.

8. The method of claim 5 in which the chlorine dioxide is added at night and the elemental chlorine is added during the day.

9. The method of claim 1 comprising periodically turning off the flow of sodium chlorite.

10. The method of claim 1 further comprising increasing or turning on the flow of sodium chlorite after a period of time of having been decreased or turned off.

11. The method of claim 1 further comprising controlling the turning off and thereafter turning on of the flow of sodium chlorite into the apparatus to alternate production of elemental chlorine or chlorine dioxide.

12. The method of claim 1 further comprising controlling the decreasing and thereafter increasing the flow of sodium chlorite into the apparatus to increase and decrease production of elemental chlorine.

13. The method of claim 12 , wherein the controlling is done by controlling pumps governed by control logic.

14. The method of claim 1 , wherein the chlorine dioxide is produced by a reaction where:
the anode oxidizes water to produce H + ions and oxygen gas, H+ ions migrate into the central chamber;
sodium chlorite and sodium hypochlorite exchange sodium ions for H + ions at the cation exchange resin in the central chamber to produce chlorous acid and hypochlorous acid;
the cathode reduces water to produce hydroxide ions and hydrogen gas;
sodium ions migrate into the chamber comprising the cathode and combine with the hydroxide ions to produce sodium hydroxide; and
the chlorous acid and hypochlorous acid are converted into chlorine dioxide, water, and hydrochloric acid.

Assignees

• Dimascio Felice
• Ecolab Usa Inc

Inventors

• Dimascio Felice

Classifications

• C02F1/4695 Primary

  electrodeionisation · CPC title

• C25B1/26

  Chlorine; Compounds thereof (by simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine C25B1/34) · CPC title

• C02F1/4678

  of metals · CPC title

• Y02W10/37

  using solar energy · CPC title