IP Library Granted Patent US 6,840,251
Granted Patent B2
US 6,840,251 · App. 10/409,220 · Granted Jan 11, 2005

Methods of simultaneously cleaning and disinfecting industrial water systems

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Quick Facts
Patent No.
US 6,840,251
App. No.
10/409,220
Granted
Jan 11, 2005
Kind
B2
Abstract

On-Line and Off-Line methods of simultaneously cleaning and disinfecting an industrial water system are described and claimed. The methods involve the addition to the water of the industrial water system of a Compound selected from the group consisting of the alkali salts of chlorite and chlorate and mixtures thereof; and an acid, followed by allowing the water in the industrial water system to circulate for several hours. The reaction of the alkali salts of chlorite and chlorate and acid produces chlorine dioxide in-situ in the water of the industrial water system. The chlorine dioxide kills microorganisms and the acid acts to remove deposits upon the water-contact surfaces of the equipment. An alternative method involves the use of a chelating agent and a biocide. Other possible cleaning and disinfection reagents may be added as needed including corrosion inhibitors, chelating agents, biocides, surfactants and reducing agents. These cleaning and disinfecting methods work in a variety of industrial water systems including cooling water and boiler water systems.

Claims (15)

1. An on-line method of simultaneously cleaning and disinfecting an industrial water system comprising the steps of:

a) providing an industrial water system; wherein said industrial water system is selected from the group consisting of cooling water systems and boiler water systems;

b) adding a Compound selected from the group consisting of the alkali salts of chlorite and chlorate, or a mixture thereof, and optionally adding a corrosion inhibitor and optionally adding a dispersant to the water of said industrial water system; wherein enough Compound is added to reach a concentration of from about 1 ppm to about 1000 ppm, wherein if a corrosion inhibitor is added enough corrosion inhibitor is added to reach a concentration of from about 50 ppm to about 500 ppm and wherein if a dispersant is added enough dispersant is added to reach a concentration of from about 1 ppm to about 500 ppm;

c) lowering the pH of the water in the industrial water system to about 4.0 by adding an acid selected from the group consisting of mineral acids and organic acids to the water of said industrial water system and maintaining the pH of the water in the industrial water system at about 4.0 for from about 1 to about 4 hours;

d) adding a chelating agent to the water of the industrial water system, wherein enough chelating agent is added to maintain the concentration of the chelating agent at from about 10 ppm to about 500 ppm in the water of the industrial water system; wherein said chelating agent is added either before or after the optional next step of raising the pH;

e) optionally raising the pH of the water in the industrial water system from about 5.5 to about 11;

f) adding a biocide to the water of the industrial water system; wherein if the chelating agent is added after the optional step of raising the pH, then the chelating agent and the biocide from step g) may be added simultaneously to the water or the chelating agent may be added first followed by the biocide or the biocide may be added first, followed by the chelating agent; wherein the amount of biocide added is that amount sufficient to have a concentration of from about 1 ppm to about 500 ppm in the water of the industrial water system; and

g) allowing the water in the industrial water system to circulate for an additional time period of from about 1 hour to about 120 hours.

2. The method of claim 1 further comprising: 1) modifying said industrial water system to a single cycle system after step a); 2) halting the feeding of chemical or biological treatment chemicals to the water of the industrial water system; and 3) adding said corrosion inhibitor and said dispersant to the industrial water system.

3. The method of claim 1 in which said corrosion inhibitor is benzotriazole.

4. The method of claim 1 in which said dispersant is a terpolymer comprising from about 30 to about 70 mol % acrylic acid, from about 10 to about 30 mol % acrylamide and from about 20 to about 40 mol % aminomethylsulfonic acid.

5. The method of claim 1 wherein the alkali salt of chlorite is sodium chlorite.

6. The method of claim 1 in which said acid is glycolic acid.

7. The method of claim 1 in which said chelating agent is sodium hexametaphosphate.

8. The method of claim 1 in which said biocide is 2,2-dibromo-3-nitrilopropionamide.

Assignments (10)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 4, 2017
From: NALCO COMPANY
To: ECOLAB USA INC.
Reel/Frame 042147/0420 →
RELEASE OF SECURITY INTEREST Recorded Feb 28, 2017
From: CITICORP NORTH AMERICA, INC.
To: NALCO COMPANY
Reel/Frame 041832/0826 →
CHANGE OF NAME Recorded Feb 28, 2017
From: NALCO COMPANY
To: NALCO COMPANY LLC
Reel/Frame 041835/0903 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2017
From: NALCO COMPANY LLC; CALGON CORPORATION; CALGON LLC; ONDEO NALCO ENERGY SERVICES, L.P.
To: ECOLAB USA INC.
Reel/Frame 041836/0437 →
RELEASE OF SECURITY INTEREST Recorded Feb 24, 2017
From: BANK OF AMERICA, N.A.
To: NALCO COMPANY
Reel/Frame 041808/0713 →
SECURITY AGREEMENT Recorded May 18, 2009
From: NALCO COMPANY; CALGON LLC; NALCO ONE SOURCE LLC; NALCO CROSSBOW WATER LLC
To: BANK OF AMERICA, N.A., AS COLLATERAL AGENT
Reel/Frame 022703/0001 →
CHANGE OF NAME Recorded Dec 3, 2004
From: ONDEO NALCO COPANY
To: NALCO COMPANY
Reel/Frame 016046/0310 →
GRANT OF SECURITY INTEREST Recorded Dec 8, 2003
From: NALCO COMPANY
To: CITICORP NORTH AMERICA, INC., AS ADMINISTRATIVE AGENT
Reel/Frame 014805/0132 →
GRANT OF SECURITY INTEREST Recorded Dec 2, 2003
From: ONDEO NALCO COMPANY
To: NALCO COMPANY
Reel/Frame 014822/0305 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 8, 2003
From: GILL, JASBIR S.; GUPTA, AMIT
To: ONDEO NALCO COMPANY
Reel/Frame 013954/0304 →