Treatment method and treatment apparatus for waste water containing sulfuric acid, fluorine and heavy metal ions
US-2019276342-A1 · Sep 12, 2019 · US
US11479490B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11479490-B2 |
| Application number | US-201816957464-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 27, 2018 |
| Priority date | Dec 27, 2017 |
| Publication date | Oct 25, 2022 |
| Grant date | Oct 25, 2022 |
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A method of treating a waste liquid: an aluminum dissolution step of dissolving aluminum in an acidic waste liquid and performing separation into a first treated water and a reduced heavy metal precipitate; a gypsum recovery step of adding a calcium compound to the first treated water at a pH of 4 or less, and performing separation into a second treated water and gypsum; a heavy metal coprecipitation step of adding a ferric compound to the second treated water and performing separation into a third treated water and a heavy metal coprecipitate; an aluminum and fluorine removal step of adding an alkali to the third treated water and performing separation into a fourth treated water and a precipitate containing aluminum and fluorine; and a neutralization step of adding an alkali to the fourth treated water and performing separation into an alkali neutralization treated water and a neutralized heavy metal hydroxide.
Opening claim text (preview).
What is claimed is: 1. A method of treating a waste liquid for recovering gypsum having a small amount of fluorine from an acidic waste liquid containing fluorine and a heavy metal and removing the heavy metal, the method comprising: an aluminum dissolution step of dissolving aluminum in the acidic waste liquid to stably dissolve fluorine in the liquid as a fluoroaluminate ion and produce a reduced heavy metal precipitate and performing separation into a first treated water and the reduced heavy metal precipitate; a gypsum recovery step of, after removing the reduced heavy metal precipitate, adding a calcium compound to the first treated water at a liquid property of a pH of 4 or less to produce gypsum, and performing separation into a second treated water and the gypsum; a heavy metal coprecipitation step of, after removing the gypsum, adding a ferric compound to the second treated water to produce a ferric hydroxide precipitate, causing the heavy metal in the liquid to be coprecipitated with the precipitate, and performing separation into a third treated water and a heavy metal coprecipitate; an aluminum and fluorine removal step of, after removing the heavy metal coprecipitate, adding an alkali to the third treated water to adjust a pH to 5.5 to 9.5 and produce a precipitate containing aluminum and fluorine while suppressing an amount of the precipitate, and performing separation into a fourth treated water and the precipitate containing aluminum and fluorine; and a neutralization step of, after removing the precipitate containing aluminum and fluorine, further adding an alkali to the fourth treated water to adjust the pH to 9.5 to 11.8 and produce a neutralized precipitate of a heavy metal hydroxide, and performing separation into an alkali neutralization treated water and the neutralized precipitate of a heavy metal hydroxide, wherein a reduction reaction occurs by dissolving the aluminum in the acidic waste liquid in the aluminum dissolution step, and an oxidation-reduction potential in the reduction reaction is +400 mV or less. 2. The method of treating a waste liquid according to claim 1 , wherein, in the aluminum and fluorine removal step, a liquid property of the third treated water is adjusted to a pH of 5.5 to 7.0 to suppress the amount of the precipitate and suppress precipitation of arsenic and zinc, thereby fluorine and aluminum are precipitated. 3. The method of treating a waste liquid according to claim 1 , wherein the acidic waste liquid containing fluorine and a heavy metal is wastewater from a non-ferrous metal smelter. 4. The method of treating a waste liquid according to claim 2 , wherein the acidic waste liquid containing fluorine and a heavy metal is wastewater from a non-ferrous metal smelter. 5. The method of treating a waste liquid according to claim 1 , wherein an amount of aluminum dissolved in the acidic waste liquid with respect to fluorine is 0.4 mol or more in the aluminum dissolution step. 6. The method of treating a waste liquid according to claim 2 , wherein an amount of aluminum dissolved in the acidic waste liquid with respect to fluorine is 0.4 mol or more in the aluminum dissolution step. 7. The method of treating a waste liquid according to claim 3 , wherein an amount of aluminum dissolved in the acidic waste liquid with respect to fluorine is 0.4 mol or more in the aluminum dissolution step. 8. The method of treating a waste liquid according to claim 4 , wherein an amount of aluminum dissolved in the acidic waste liquid with respect to fluorine is 0.4 mol or more in the aluminum dissolution step.
Processes for facilitating the dissolution of solid flocculants in water · CPC title
Fluorides · CPC title
Oxides; Hydroxides {(C01G49/0018 takes precedence)} · CPC title
Fluorides · CPC title
Sulfates (dehydration of gypsum {for the production of calcium sulfate cements} C04B11/02) · CPC title
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