Process for removal of selenium from water by dithionite ions
US-2017349462-A1 · Dec 7, 2017 · US
US2025243058A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025243058-A1 |
| Application number | US-202418770198-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 11, 2024 |
| Priority date | Jan 25, 2024 |
| Publication date | Jul 31, 2025 |
| Grant date | — |
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Provided is a method for preparing 7N tellurium, including the following steps: mixing 2N crude tellurium with concentrated sulfuric acid, and subjecting a resulting mixture to oxidation roasting to obtain a selenium dioxide vapor and a roasting residue; mixing the roasting residue with a strong base solution, and subjecting a resulting solution to electrolysis to obtain 4N electrolytic tellurium; subjecting the 4N electrolytic tellurium to vacuum distillation to obtain 5N tellurium; and melting the 5N tellurium to obtain a tellurium melt, immersing a crystallizer in the tellurium melt, and subjecting the tellurium melt to crystallization to obtain the 7N tellurium; wherein the method is performed for a total time of less than 14 days.
Opening claim text (preview).
1 . A method for preparing 7N tellurium, comprising the following steps: mixing 2N crude tellurium with concentrated sulfuric acid, and subjecting a resulting mixture to oxidation roasting to obtain a selenium dioxide vapor and a roasting residue; mixing the roasting residue with a strong base solution, and subjecting a resulting solution to electrolysis to obtain 4N electrolytic tellurium; subjecting the 4N electrolytic tellurium to vacuum distillation to obtain 5N tellurium; and melting the 5N tellurium to obtain a tellurium melt, immersing a crystallizer in the tellurium melt, and subjecting the tellurium melt to crystallization to obtain the 7N tellurium; wherein the method is performed for a total time of less than 14 days. 2 . The method according to claim 1 , wherein a mass ratio of the 2N crude tellurium to the concentrated sulfuric acid is in a range of (1-3):1, and a mass concentration of the concentrated sulfuric acid is 98%. 3 . The method according to claim 1 , wherein the oxidation roasting is conducted at a temperature of 350° C. to 600° C. for 0.5 h to 3 h. 4 . The method according to claim 1 , wherein in the resulting solution, a concentration of tellurium is in a range of 100 g/L to 300 g/L and a concentration of the strong base is in a range of 90 g/L to 130 g/L. 5 . The method according to claim 1 , wherein the electrolysis is conducted for 50 h to 110 h at a temperature of 30° C. to 50° C. with a current density of 45 A/m 2 to 55 A/m 2 ; and during the electrolysis, the resulting solution is in a circulating state with a circulating rate of 1 mL/s to 5 mL/s. 6 . The method according to claim 1 , wherein the vacuum distillation is conducted at a temperature of 450° C. to 600° C. and a vacuum degree of 0 Pa to 100 Pa. 7 . The method according to claim 1 , wherein the tellurium melt has a temperature of 460° C. to 560° C. 8 . The method according to claim 1 , wherein an immersion depth of the crystallizer is 50 mm to 100 mm below a liquid level of the tellurium melt. 9 . The method according to claim 1 , wherein the crystallizer has an initial temperature of 460° C. to 500° C., and after the crystallizer is immersed for 10 min to 60 min, a temperature of the crystallizer is reduced to 420° C. to 440° C. 10 . The method according to claim 1 , wherein the crystallization comprises static crystallization and rotary crystallization, and a rotational speed for the rotary crystallization is less than 120 r/min. 11 . The method according to claim 2 , wherein the oxidation roasting is conducted at a temperature of 350° C. to 600° C. for 0.5 h to 3 h. 12 . The method according to claim 4 , wherein the electrolysis is conducted for 50 h to 110 h at a temperature of 30° C. to 50° C. with a current density of 45 A/m 2 to 55 A/m 2 ; and during the electrolysis, the resulting solution is in a circulating state with a circulating rate of 1 mL/s to 5 mL/s. 13 . The method according to claim 7 , wherein an immersion depth of the crystallizer is 50 mm to 100 mm below a liquid level of the tellurium melt. 14 . The method according to claim 7 , wherein the crystallizer has an initial temperature of 460° C. to 500° C., and after the crystallizer is immersed for 10 min to 60 min, a temperature of the crystallizer is reduced to 420° C. to 440° C. 15 . The method according to claim 7 , wherein the crystallization comprises static crystallization and rotary crystallization, and a rotational speed for the rotary crystallization is less than 120 r/min.
Compositional purity · CPC title
Elemental selenium or tellurium · CPC title
Recycling · CPC title
Processes · CPC title
Products · CPC title
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