Water treatment method and water treatment apparatus
US-2024383788-A1 · Nov 21, 2024 · US
US9593032B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9593032-B2 |
| Application number | US-201313802961-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 14, 2013 |
| Priority date | Nov 30, 2012 |
| Publication date | Mar 14, 2017 |
| Grant date | Mar 14, 2017 |
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Systems and methods for removing organic contaminants from water may be used, for example, to treat produced water from a steam assisted heavy oil recovery operation. The treated produced water may be re-used to create steam. Alternatively, the produced water may be a blowdown stream treated to facilitate further treatment in a thermal crystallizer. The treatments may include pH adjustment or separating de-solubilized organics or both. Other treatments may include one or more of oxidation, sorption and biological treatments. The treatments may be used alone or in various combinations. One exemplary combination includes reducing the pH of produced water, separating de-solubilized organics from the produced water, and oxidizing the produced water or contacting the produced water with activated carbon.
Opening claim text (preview).
What is claimed is: 1. A method for removing organics from aqueous media, said method comprising the steps of: (A) treating the aqueous media in a first phase by acidifying the aqueous media to de-solubilize dissolved organics and separating de-solubilized organics from the aqueous media by filtration; and (B) treating the aqueous media directly resulting from step (A) in a second phase by contacting the aqueous media with activated carbon having at least 50% of its pores by number with a pore diameter in a range of about 10 to about 20 Angstroms. 2. The method of claim 1 , wherein the activated carbon has at least 50% of its pores by number with a pore diameter in the range from about 12 to about 17 Angstroms or a high volume of pores in this range. 3. The method of claim 1 , wherein the activated carbon has a positively charged surface. 4. The method of claim 1 , wherein the aqueous media is acidified in the first phase to a pH value of from about 4 to about 6. 5. The method of claim 1 , wherein the de-solubilized organics are separated by filtration with a ceramic membrane. 6. The method of claim 1 comprising contacting the aqueous media with biological activated carbon. 7. The method of claim 6 comprising two stages of activated carbon treatment wherein one of the stages is a biological activated carbon. 8. The method of claim 7 , wherein the biological activated carbon stage is after the activated carbon stage. 9. The method of claim 7 , wherein the biological activated carbon stage is before the activated carbon stage. 10. The method of claim 1 wherein the aqueous media is treated via adsorption. 11. The method of claim 1 , wherein the aqueous media is acidified in the first phase to a pH of from about 3 to about 7. 12. The method of claim 1 wherein the aqueous media comprises produced water.
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