IPC분류정보
| 국가/구분 |
United States(US) Patent
등록
|
| 국제특허분류(IPC7판) |
|
| 출원번호 |
US-0623435
(2009-11-22)
|
| 등록번호 |
US-8419948
(2013-04-16)
|
|
발명자
/ 주소 |
|
| 출원인 / 주소 |
- United Laboratories International, LLC
|
| 대리인 / 주소 |
|
| 인용정보 |
피인용 횟수 :
0 인용 특허 :
50 |
초록
▼
A method for treating wastewater treats wastewater. In an embodiment, the method for treating wastewater includes treating wastewater comprising a chemical oxygen demand. The method includes dissolving an iron compound in the wastewater. The method also includes adjusting the pH of the wastewater to
A method for treating wastewater treats wastewater. In an embodiment, the method for treating wastewater includes treating wastewater comprising a chemical oxygen demand. The method includes dissolving an iron compound in the wastewater. The method also includes adjusting the pH of the wastewater to reduce the chemical oxygen demand of the wastewater.
대표청구항
▼
1. A method for treating wastewater, wherein the wastewater comprises a chemical oxygen demand, comprising: (A) dissolving an iron compound in the wastewater, the wastewater comprising dimethylalkylamine-N-oxide;(B) adjusting the pH of the wastewater to precipitate an insoluble iron composition comp
1. A method for treating wastewater, wherein the wastewater comprises a chemical oxygen demand, comprising: (A) dissolving an iron compound in the wastewater, the wastewater comprising dimethylalkylamine-N-oxide;(B) adjusting the pH of the wastewater to precipitate an insoluble iron composition comprising hydrated iron oxides; and(C) reacting the iron composition with the dimethylalkylamine-N-oxide in the wastewater to reduce the chemical oxygen demand of the wastewater and provide a reduced chemical oxygen demand wastewater. 2. The method of claim 1, further comprising reducing the chemical oxygen demand of the reduced chemical oxygen wastewater to less than about 300 milligrams/liter. 3. The method of claim 1, further comprising reducing the chemical oxygen demand of the reduced chemical oxygen wastewater to less than about 100 milligrams/liter. 4. The method of claim 1, further comprising reducing the chemical oxygen demand of the reduced chemical oxygen demand wastewater to less than about 50 milligrams/liter. 5. The method of claim 1, wherein the dimethylalkylamine-N-oxide comprises an alkyl component, and wherein the alkyl component comprises C6 to C18. 6. The method of claim 1, wherein the iron compound comprises a soluble iron salt. 7. The method of claim 1, wherein the iron compound comprises ferrous sulfate, ferric ammonium sulfate, ferrous ammonium sulfate, ferric chloride, ferric sulfate, a soluble ferrous salt, a soluble ferric salt, or any combinations thereof. 8. The method of claim 1, wherein the iron compound comprises ferric ammonium sulfate. 9. The method of claim 1, further comprising adding from about 1 gram/liter to about 5 grams/liter of the iron compound to the wastewater. 10. The method of claim 1, wherein the iron compound comprises a soluble ferrous salt, a soluble ferric salt, or any combinations thereof. 11. The method of claim 1, wherein adjusting the pH comprises increasing the pH of the wastewater to a pH from about 5 to about 9. 12. The method of claim 1, wherein adjusting the pH comprises increasing the pH of the wastewater to a pH from about 7 to about 9. 13. The method of claim 1, wherein adjusting the pH comprises adding trisodium phosphate, ammonia, sodium bicarbonate, borax, sodium carbonate, or any combination thereof to the wastewater. 14. The method of claim 1, wherein adjusting the pH comprises adding sodium bicarbonate to the wastewater. 15. The method of claim 1, further comprising heating the wastewater. 16. The method of claim 15, wherein heating the wastewater comprises heating the wastewater to temperatures from about 50° C. to about 100° C. 17. The method of claim 15, wherein heating the wastewater comprises heating the wastewater to temperatures from about 50° C. to about 60° C. 18. The method of claim 15, wherein heating the wastewater comprises adding heat for about 3 hours to about 6 hours.
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