Preparation of concentrated aqueous bromine solutions and biocidal applications thereof
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
A01N-041/06
A61K-031/18
출원번호
US-0451319
(1999-11-30)
등록번호
US-8293795
(2012-10-23)
발명자
/ 주소
Moore, Jr., Robert M.
Nalepa, Christopher J.
출원인 / 주소
Albemarle Corporation
대리인 / 주소
Hoefling, Marcy M.
인용정보
피인용 횟수 :
0인용 특허 :
79
초록▼
A process of producing a concentrated liquid biocide formulation is described. Mixed together are (a) bromine and (b) an aqueous solution of alkali metal salt of sulfamic acid having a pH of at least about 12, in amounts such that (i) the active bromine content of the solution is at least about 100,
A process of producing a concentrated liquid biocide formulation is described. Mixed together are (a) bromine and (b) an aqueous solution of alkali metal salt of sulfamic acid having a pH of at least about 12, in amounts such that (i) the active bromine content of the solution is at least about 100,000 ppm (wt/wt), and (ii) the atom ratio of nitrogen to active bromine from (a) and (b) is greater than 1. A continuous process for producing the concentrated liquid biocide composition is provided. This process comprises continuously feeding into mixing apparatus (i) bromine and (ii) an aqueous solution of alkali metal salt of sulfamic acid; the desired product is withdrawn from the mixing apparatus at a rate sufficient to enable the continuous feeding to be maintained. Also described are methods for disinfecting surfaces and for sanitizing bodies of water using a single-feed, bromine-based biocide. These methods use concentrated liquid biocide compositions comprising biocidally active bromine as the biocide.
대표청구항▼
1. A process of producing a concentrated, stabilized liquid biocide formulation, which process consists of cofeeding to an aqueous solution formed from components consisting of water, sulfamic acid and alkali metal base, feed components consisting of (i) bromine and (ii) a solution of alkali metal b
1. A process of producing a concentrated, stabilized liquid biocide formulation, which process consists of cofeeding to an aqueous solution formed from components consisting of water, sulfamic acid and alkali metal base, feed components consisting of (i) bromine and (ii) a solution of alkali metal base that maintains, while cofeeding, the pH of said concentrated, stabilized liquid biocide formulation produced in the range of from about 12 to about 14. 2. A process according to claim 1 wherein said concentrated, stabilized liquid biocide formulation contains an amount of bromine that is no more than 26% of active bromine. 3. A process according to claim 1 wherein said biocide formulation has an active bromine content of about 100,000 ppm (wt/wt) or more and an atom ratio of nitrogen to active bromine greater than 1. 4. A process according to claim 1, wherein the pH is up to about 13.5. 5. A process of producing a concentrated liquid biocide composition, which process consists of A) continuously feeding into mixing apparatus components consisting of (i) bromine and (ii) an aqueous solution of alkali metal salt of sulfamic acid having a pH of about 1 or more, proportioned to produce an aqueous product (a) having an active bromine content of at least 100,000 ppm (wt/wt), and an atom ratio of nitrogen to active bromine from (i) and (ii) greater than 1, and (b) maintaining the pH of said product in the range of from about 12 to about 14; andB) withdrawing said product from said mixing apparatus at a rate sufficient to enable the continuous feeding in A) to be maintained. 6. A process according to claim 5 wherein (ii) in A) is an aqueous solution of the sodium salt of sulfamic acid. 7. A process according to claim 6 wherein said atom ratio is in the range of about 1.1 to about 1.5. 8. A process according to claim 5 wherein said mixing apparatus comprises a static mixer. 9. A process according to claim 5 wherein said mixing apparatus comprises a vessel equipped with a mechanical stirrer. 10. A process according to claim 9 wherein said product is intermittently withdrawn from said vessel. 11. A process according to claim 9 wherein said product is continuously withdrawn from said vessel. 12. A process of producing a concentrated liquid biocide composition, which process consists of A) continuously feeding into mixing apparatus components consisting of (i) a bromine stream and (ii) a separate feed stream of an aqueous solution of alkali metal salt of sulfamic acid having a pH of about 12 or more, in proportions that produce an aqueous product (a) having an active bromine content of at least 100,000 ppm (wt/wt), and an atom ratio of nitrogen to active bromine from (i) and (ii) greater than 1, and (b) maintaining the pH of said product in the range of from about 12 to about 14; andB) withdrawing said product from said mixing apparatus at a rate sufficient to enable the continuous feeding in A) to be maintained; andC) continuously, but alternately, withdrawing from at least one and then from at least one other of at least two reaction vessels, an aqueous solution of alkali metal salt of sulfamic acid at a rate that maintains said stream of (ii) in A), and during the time the solution is being withdrawn from said at least one of at least two reaction vessels, forming additional aqueous solution of alkali metal salt of sulfamic acid in said at least one other of at least two reaction vessels from which solution is not then being withdrawn. 13. A process according to claim 12 wherein said aqueous solution of alkali metal salt of sulfamic acid is an aqueous solution of the sodium salt of sulfamic acid. 14. A process according to claim 12 wherein said aqueous solution of alkali metal wherein said atom ratio is in the range of about 1.1 to about 1.5. 15. A process according to claim 12 wherein said mixing apparatus comprises a static mixer. 16. A process according to any of claim 12 wherein said mixing apparatus comprises a vessel equipped with a mechanical stirrer. 17. A process according to claim 16 wherein in B) said aqueous product is intermittently withdrawn from said vessel. 18. A process according to claim 16 wherein in B) said aqueous product is continuously withdrawn from said vessel. 19. A process according to claim 12 wherein said mixing apparatus comprises a static mixer, and wherein said additional aqueous solution of alkali metal salt of sulfamic acid is formed from an alkali metal base, sulfamic acid, and water. 20. A process according to claim 12 wherein said mixing apparatus comprises a static mixer, wherein said aqueous solution of alkali metal salt of sulfamic acid is an aqueous solution of sodium sulfamate, and wherein said additional aqueous solution of alkali metal salt of sulfamic acid is formed from a water-soluble sodium base, sulfamic acid, and water. 21. A process according to claim 20 wherein said sodium base is an aqueous solution of sodium hydroxide, and wherein the sodium sulfamate is formed as an aqueous solution by charging to a reactor (i) an aqueous solution of sodium hydroxide, and (ii) a slurry of sulfamic acid in water, or (iii) separate charges of sulfamic acid and water, or (iv) both of (ii) and (iii).
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