Strategy for on-site in situ generation of oxidizing compounds and application of the oxidizing compound for microbial control

Patent metadata

Field	Value
Publication number	US-9242880-B2
Application number	US-97980610-A
Country	US
Kind code	B2
Filing date	Dec 28, 2010
Priority date	Dec 28, 2010
Publication date	Jan 26, 2016
Grant date	Jan 26, 2016

Abstract

The invention provides a method of controlling biological fouling of water containing items. The method involves combining at least two reactants, a peroxygen source and an acyl group donor to form peracetic acid. Because the peracetic acid can be made in situ, the entire sum of its short lifespan can be used controlling biocidal fouling and storage and transport is simplified. The invention further facilitates the ease of controlling biocidal fouling by allowing the injection of the biocidal agent in liquid form, in a non-acidic environment, and without the need for any halogen. This allows the inventive biocide to be used with chemistries for which prior art biocides are inapplicable.

First claim

The invention claimed is:

1. A method of microbial fouling control of a liquid system susceptible to biological fouling, wherein the liquid system comprises an industrial process water stream the method comprising generating a biocidal agent comprising peracetic acid by reacting a peroxygen source and triacetylethanolamine in the presence of 1-acetyl imidazole at a pH of from about 5 to about 8;
wherein the peroxygen source is selected from the group consisting of: hydrogen peroxide, a percarbonate salt, a perborate salt, a permanganate salt, a peroxysilicate, carbamide peroxide, urea hydrogen peroxide, an organic peroxide, tert-butyl hydroperoxide, and combinations thereof wherein the reaction occurs within the industrial process water stream.

2. The method of claim 1 , wherein the reaction occurs at a pH of from about 5 to about 6.

3. The method of claim 1 , wherein the biocidal agent is within the industrial process water stream for the entire lifespan of the peracetic acid.

4. The method of claim 1 , wherein the industrial process water stream comprises a component selected from the group consisting of: flume water; shower water;
thermal processing water; a brewing liquid; a fermentation liquid; a clean in place liquid; a hard surface sanitization liquid; ethanol/bio-fuel process water; pretreatment water; utility water; a membrane system liquid; an ion-exchange bed liquid; water used to manufacture paper, ceiling tiles, fiber board, or microelectronics; an E-coat liquid; an electrodeposition liquid; a process cleaning liquid; an oil exploration services liquid; an oil well completion fluid; an oil well workover fluid; a drilling additive fluid; an oil fracturing fluid; an oil well flowline water system; a gas well flowline water system; a natural gas water system; and combinations thereof.

5. The method of claim 1 , wherein the biocidal agent further comprises at least one item selected from the group consisting of: a surfactant, a chelant, a dispersant, an emulsifier, a salt, a freezing point depressant, and combinations thereof.

6. The method of claim 1 , wherein the industrial process water stream comprises a main stream and a side stream through which a portion of the industrial process water is diverted and then returned to the main stream, wherein the biocidal agent is added to the side stream.

7. The method of claim 6 , wherein, prior to the addition of the biocidal agent, the side stream passes through an apparatus selected from the group consisting of: a water clarifier, a water softener, an on-line centrifuge, a water filter, and combinations thereof.

8. The method of claim 1 , further comprising monitoring the industrial process water stream to control the generation of the biocidal agent.

9. The method of claim 1 , wherein the liquid system comprises process equipment constructed of a material that is less compatible with halogenated biocides than with non-halogenated biocides.

10. The method of claim 1 , wherein the generated peracetic acid remains stable for about two to about ten hours.

11. The method of claim 1 , wherein the peroxygen source, triacetylethanolamine, and the 1-acetyl imidazole are liquids prior to being reacted.

12. A method of microbial fouling control of a liquid system susceptible to biological fouling, wherein the liquid system comprises an industrial process water stream the method consisting essentially of generating a biocidal agent by reacting a peroxygen source and triacetylethanolamine in the presence of 1-acetyl imidazole at a pH of from about 5 to about 8, and introducing the biocidal agent into the liquid system;
wherein the peroxygen source is selected from the group consisting of: hydrogen peroxide, a percarbonate salt, a perborate salt, a permanganate salt, a peroxysilicate, carbamide peroxide, urea hydrogen peroxide, an organic peroxide, tert-butyl hydroperoxide, and combinations thereof wherein the reaction occurs within the industrial process water stream.

13. The method of claim 12 , wherein the reaction occurs at a pH of from about 5 to about 6.

14. The method of claim 12 , wherein the reaction occurs at a pH of from about 5 to 6.

15. The method of claim 1 , wherein the reaction occurs at a pH of from about 5 to 6.

16. The method of claim 1 , wherein the peroxygen source is hydrogen peroxide.

17. The method of claim 12 , wherein the peroxygen source is hydrogen peroxide.

18. The method of claim 14 , wherein the peroxygen source is hydrogen peroxide.

19. The method of claim 15 , wherein the peroxygen source is hydrogen peroxide.

Assignees

• Gupta Amit
• Reedy Charles J
• Moriarty Barbara E
• Atkins Jeffery M
• Nalco Co

Inventors

• Gupta Amit
• Reedy Charles J
• Moriarty Barbara E
• Atkins Jeffery M

Classifications

• C02F2303/20

  Prevention of biofouling · CPC title

• C02F1/722 Primary

  Oxidation by peroxides · CPC title