Method for reducing alumina or magnesia by utilizing supersonic gas flow
US-9617620-B2 · Apr 11, 2017 · US
US2024360536A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024360536-A1 |
| Application number | US-202318569062-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 9, 2023 |
| Priority date | Jan 11, 2022 |
| Publication date | Oct 31, 2024 |
| Grant date | — |
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The present invention relates to a method for recovering magnesium from sediment generated in an electrolytic chlorine generation system using seawater or brackish water, the method comprising the steps of: eluting magnesium by using sulfuric acid in magnesium hydroxide, which is sediment generated in an electrolytic chlorine generation system using seawater and brackish water; precipitating magnesium sulfate by adding an organic solvent to a magnesium-eluted solution; and after the precipitation of the magnesium sulfate, separating the organic solvent and sulfuric acid by using a vacuum evaporation method, and reusing the organic solvent.
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1 . A method for recovering magnesium from sediment generated in an electrolytic chlorine generation system using seawater or brackish water, comprising: eluting magnesium using sulfuric acid in magnesium hydroxide, a sediment generated in an electrolytic chlorine generation system using seawater and brackish water; precipitating magnesium sulfate (MgSO 4 ·xH 2 O(s)) by adding an organic solvent to the magnesium elution solution; and, after precipitating the magnesium sulfate, the organic solvent and sulfuric acid are separated using reduced pressure evaporation and reusing the organic solvent. 2 . The method of claim 1 , wherein the sulfuric acid is waste sulfuric acid. 3 . The method of claim 2 , wherein the waste sulfuric acid was generated at industrial sites. 4 . The method of claim 1 , wherein the method comprises the step of treating sediment generated from an electrolytic chlorine generation system using seawater and brackish water with sulfuric acid (H 2 SO 4 ) to extract high concentration of magnesium, and then separating the magnesium sulfate using an organic solvent. 5 . The method of claim 1 , wherein the seawater is seawater concentrate. 6 . The method of claim 1 , wherein the organic solvent is ethanol or acetone. 7 . (canceled) 8 . The method of claim 1 , wherein the method comprises eluting magnesium using 0.5 to 1 M sulfuric acid in magnesium hydroxide, a sediment generated in an electrolytic chlorine generation system and mixing the eluent with the sulfuric acid to ethanol or acetone in a ratio of 1:1.5 to 1:2 (v:v) to precipitate magnesium. 9 . The method of claim 8 , wherein the method comprises eluting magnesium using 0.5 M sulfuric acid in magnesium hydroxide, a sediment generated in an electrolytic chlorine generation system and mixing the eluent with the sulfuric acid to acetone in a ratio of 1:2 (v:v) to precipitate magnesium. 10 . A magnesium compound recovered by the method of claim 1 . 11 . The magnesium compound according to claim 10 , wherein the magnesium compound is magnesium sulfate. 12 . The magnesium compound according to claim 10 , wherein the sulfuric acid is waste sulfuric acid. 13 . The magnesium compound according to claim 12 , wherein the waste sulfuric acid was generated at industrial sites. 14 . The magnesium compound according to claim 10 , wherein the seawater is seawater concentrate. 15 . The magnesium compound according to claim 10 , wherein the organic solvent is ethanol or acetone.
Chlorides · CPC title
by acid leaching · CPC title
by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) · CPC title
Magnesium sulfates (double sulfates of magnesium with sodium or potassium C01D5/12, with other alkali metals {C01D15/00}, C01D17/00) · CPC title
by mass-spectroscopy · CPC title
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