Water treatment method and water treatment apparatus
US-2024383788-A1 · Nov 21, 2024 · US
US2016251241A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016251241-A1 |
| Application number | US-201415026448-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 6, 2014 |
| Priority date | Oct 16, 2013 |
| Publication date | Sep 1, 2016 |
| Grant date | — |
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A wastewater treatment method and a wastewater treatment apparatus securely and readily remove selenium, which is considered harmful, by removing not only 0-valent selenium, 4-valent selenium, and 6-valent selenium, but also -2-valent selenium. In the wastewater treatment method and the wastewater treatment apparatus for treating wastewater including selenium, -2-valent selenium included in the wastewater is oxidated by using an oxidant, or -2-valent selenium included in the water is removed by using a remover.
Opening claim text (preview).
1 - 8 . (canceled) 9 . A wastewater treatment method for treating wastewater including selenium, wherein -2-valent selenium included in the wastewater is oxidated by using an oxidant or -2-valent selenium included in the wastewater is removed by using a remover, and wherein a silver chloride is used as the remover which is generated by reacting hydrochloric acid with a silver nitrate. 10 . The wastewater treatment method according to claim 9 , wherein an aqueous solution of hydrogen peroxide is used as the oxidant. 11 . The wastewater treatment method according to claim 10 , comprising a coprecipitation treatment step of separating 0-valent selenium and/or 4-valent selenium from the wastewater including oxidated selenium by coprecipitation with iron hydroxide by oxidating the -2-valent selenium with the aqueous solution of aqueous solution of hydrogen peroxide. 12 . The wastewater treatment method according to claim 9 , comprising a coprecipitation treatment step of separating 0-valent selenium and/or 4-valent selenium from the wastewater by coprecipitation with iron hydroxide after the silver chloride has adsorbed the -2-valent selenium for separation. 13 . A wastewater treatment apparatus configured to remove selenium included in wastewater drained from a coal gasification compound power generation facility, the apparatus comprising: a receiving tank into which the wastewater including -2-valent selenium, 0-valent selenium, 4-valent selenium, and 6-valent selenium flows; an oxidation tank configured to oxidate the -2-valent selenium by using an aqueous solution of hydrogen peroxide or a removal tank configured to adsorb the -2-valent selenium and allow the -2-valent selenium to precipitate by using silver chloride generated by a reaction between silver nitrate and hydrochloric acid; a reduction tank configured to reduce the 6-valent selenium into 0-valent selenium and/or 4-valent selenium by using a reductant; and a precipitation tank configured to allow the 0-valent selenium and the 4-valent selenium in the water that has flowed in from the reduction tank to precipitate and separate by iron coprecipitation. 14 . The wastewater treatment apparatus according to claim 13 , wherein the oxidation tank or the removal tank is an aeration tank configured to remove volatile substances in the wastewater that has flowed in from the receiving tank.
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