Image Processing for Improving Coagulation and Flocculation
US-2017152153-A1 · Jun 1, 2017 · US
US11286181B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11286181-B2 |
| Application number | US-201716347431-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 12, 2017 |
| Priority date | Nov 17, 2016 |
| Publication date | Mar 29, 2022 |
| Grant date | Mar 29, 2022 |
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A calcium fluoride precipitation inhibitor is added to waste water containing sulfuric acid, fluorine (fluoride ions and hydrogen fluoride) and heavy metal ions to generate pretreated water. A calcium compound is added to the pretreated water to generate a first insolubilized product at a pH of less than 5, followed by solid-liquid separation. A calcium compound is added to a first separated water after the solid-liquid separation to generate a second insolubilized product at a pH of 3 to 7 (provided that the pH is a pH higher than in the first reaction step), followed by solid-liquid separation. An alkali is added to a second separated water after the solid-liquid separation to give a pH of 8 or more, thereby generating a third insolubilized product, followed by solid-liquid separation.
Opening claim text (preview).
The invention claimed is: 1. A method for treating waste water containing sulfuric acid, fluorine and heavy metal ions, the method comprising: a pretreatment step of adding a calcium fluoride precipitation inhibitor to the waste water to react with fluoride ions, thereby producing pretreated water; a first reaction step of adding at least one calcium compound selected from the group consisting of a calcium salt and calcium hydroxide to the pretreated water to generate a first insolubilized product at a pH of less than 5; a first solid-liquid separation step of subjecting the first insolubilized product to solid- liquid separation; a second reaction step of adding at least one calcium compound selected from the group consisting of a calcium salt and calcium hydroxide to a first separated water obtained in the first solid-liquid separation step to generate a second insolubilized product at a pH of 3 to 7 (provided that the pH is a pH higher than in the first reaction step); a second solid-liquid separation step of subjecting the second insolubilized product to solid-liquid separation; a third reaction step of adding an alkali to a second separated water obtained in the second solid-liquid separation step to give a pH of 8 or more, thereby generating a third insolubilized product; and a third solid-liquid separation step of subjecting the third insolubilized product to solid-liquid separation. 2. The method for treating waste water containing sulfuric acid, fluorine and heavy metal ions according to claim 1 , wherein the calcium fluoride precipitation inhibitor reacts with fluoride ions to generate a water-soluble fluorine-containing compound. 3. The method for treating waste water containing sulfuric acid, fluorine and heavy metal ions according to claim 1 , wherein the amount of the calcium fluoride precipitation inhibitor added in the pretreatment step is 0.5 to 5 times the equivalent weight of fluorine (a fluoride and hydrogen fluoride) in the waste water. 4. The method for treating waste water containing sulfuric acid, fluorine and heavy metal ions according to claim 1 , further comprising a first insolubilized product-reforming/returning step of adding at least part of the calcium compound added in the first reaction step to at least part of the first insolubilized product, followed by mixing, to supply a first mixture to the first reaction step. 5. The method for treating waste water containing sulfuric acid, fluorine and heavy metal ions according to claim 4 , further comprising at least one insolubilized product- reforming/returning step of: a second insolubilized product-reforming/returning step of adding at least part of the calcium compound added in the second reaction step to at least part of the second insolubilized product, followed by mixing, to supply a second mixture to the second reaction step; and a third insolubilized product-reforming/returning step of adding at least part of the calcium compound added in the third reaction step to at least part of the third insolubilized product, followed by mixing, to supply a third mixture to the third reaction step. 6. The method for treating waste water containing sulfuric acid, fluorine and heavy metal ions according to claim 1 , further comprising at least one dehydration/recovery step of: a first dehydration/recovery step of subjecting the first insolubilized product separated in the first solid-liquid separation step to dehydration treatment to recover a material containing calcium sulfate; a second dehydration/recovery step of subjecting the second insolubilized product separated in the second solid-liquid separation step to dehydration treatment to recover a material containing calcium fluoride; and a third dehydration/recovery step of subjecting the third insolubilized product separated in the third solid-liquid separation step to dehydration treatment to recover a material containing heavy metals. 7. A treatment apparatus for waste water containing sulfuric acid, fluorine and heavy metal ions, comprising: a pretreatment tank that comprises a calcium fluoride precipitation inhibitor-adding device and produces pretreated water by adding a calcium fluoride precipitation inhibitor to the waste water to react with fluoride ions; a first reaction tank that adds at least one calcium compound selected from the group consisting of a calcium salt and calcium hydroxide to the pretreated water to generate a first insolubilized product at a pH of less than 5; a first solid-liquid separation device that subjects the first insolubilized product to solid-liquid separation; a second reaction tank that adds at least one calcium compound selected from the group consisting of a calcium salt and calcium hydroxide to a first separated water obtained in the first solid-liquid separation device to generate a second insolubilized product at a pH of 3 to 7 (provided that the pH is a pH higher than in the first reaction tank); a second solid-liquid separation device that subjects the second insolubilized product to solid-liquid separation; a third reaction tank that adds an alkali to a second separated water obtained in the second solid-liquid separation device to give a pH of 8 or more, thereby generating a third insolubilized product; and a third solid-liquid separation device that subjects the third insolubilized product to solid- liquid separation, wherein the treatment apparatus further comprises a first insolubilized product-reforming/returning device that adds at least part of the calcium compound added in the first reaction tank to at least part of the first insolubilized product, followed by mixing, to supply a first mixture to the first reaction tank. 8. The treatment apparatus for waste water containing sulfuric acid, fluorine and heavy metal ions according to claim 7 , wherein the calcium fluoride precipitation inhibitor-adding device is configured to add an amount of the calcium fluoride precipitation inhibitor 0.5 to 5 times the equivalent weight of fluorine (a fluoride and hydrogen fluoride) in the waste water. 9. The treatment apparatus for waste water containing sulfuric acid, fluorine and heavy metal ions according to claim 7 , further comprising at least one insolubilized product-reforming/returning device of: a second insolubilized product-reforming/returning device that adds at least part of the calcium compound added in the second reaction tank to at least part of the second insolubilized product, followed by mixing, to supply a second mixture to the second reaction tank; and a third insolubilized product-reforming/returning device that adds at least part of the calcium compound added in the third reaction tank to at least part of the third insolubilized product, followed by mixing, to supply a third mixture to the third reaction tank. 10. The treatment apparatus for waste water containing sulfuric acid, fluorine and heavy metal ions according to claim 7 , further comprising at least one dehydration/recovery device of: a first dehydration/recovery device that subjects the first insolubilized product separated in the first solid-liquid separation device to dehydration treatment to recover a material containing calcium sulfate; a second dehydration/recovery device that subjects the second insolubilized product separated in the second solid-liquid separation step to dehydration treatment to recover a material containing calcium fluoride; and a third dehydration/recovery device that subjects the third insolubilized product separated in the third solid-liquid separation step to dehydration treatment to recover a material containing heavy metals.
by removing fluoride or fluorine compounds · CPC title
Regulation methods for flocculation or precipitation · CPC title
Multistage treatments, e.g. repetition of the same process step under different conditions · CPC title
by removing specified dissolved compounds (using ion-exchange C02F1/42; softening water C02F5/00) · CPC title
using filter presses (C02F11/123 takes precedence) · CPC title
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