Filter system, closure element, and filter element
US-2017197160-A1 · Jul 13, 2017 · US
US10625178B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10625178-B2 |
| Application number | US-201816120727-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 4, 2018 |
| Priority date | Mar 10, 2016 |
| Publication date | Apr 21, 2020 |
| Grant date | Apr 21, 2020 |
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A method for separating organic solvent(s) from an aqueous process stream including organic solvent(s), includes passing the aqueous stream including organic solvent(s) through a granular bed including glass granules, wherein at least 90% of said glass granules have a maximum particle diameter smaller than 1.0 mm.
Opening claim text (preview).
The invention claimed is: 1. A method for separating organic solvent(s) from an aqueous process stream comprising organic solvent(s), the method comprising: passing said aqueous process stream comprising organic solvent(s) through a granular bed comprising glass granules, wherein at least 90% of said glass granules have a maximum particle diameter smaller than 1.0 mm, and wherein said aqueous process stream comprises organic solvent(s) is an electrolyte solution resulting from a metal leaching process. 2. The method as claimed in claim 1 , wherein the cross section filtration velocity is from 10 to 80 m/h. 3. The method as claimed in claim 1 , wherein at least 90% of said glass granules have a maximum particle diameter smaller than 0.85 mm. 4. The method as claimed in claim 1 , wherein at least 50% of said glass granules have a maximum particle diameter greater than 0.1 mm. 5. The method as claimed in claim 1 , wherein at least 90% of said glass granules have a maximum particle diameter greater than 0.2 mm. 6. The method as claimed in claim 1 , wherein at least 80% of said glass granules have a maximum particle diameter smaller than 0.7 mm. 7. The method as claimed in claim 1 , wherein at least 50% of said glass granules have a maximum particle diameter smaller than 0.6 mm. 8. The method as claimed in claim 1 , wherein at least 50% of said glass granules have a maximum particle diameter from 0.3 to 0.7 mm. 9. The method as claimed in claim 1 , wherein said glass granules are spherical. 10. A method of using glass particles for separating organic solvent(s) from an aqueous process stream comprising organic solvent(s), comprising: utilizing glass granules wherein at least 90% of said glass granules have a maximum particle diameter smaller than 1.0 mm, and wherein the aqueous process stream comprising organic solvent(s) is an electrolyte solution resulting from a metal leaching process. 11. The method as claimed in claim 10 , wherein at least 90% of said glass granules have a maximum particle diameter smaller than 0.85 mm. 12. The method as claimed in claim 10 , wherein at least 50% of said glass granules have a maximum particle diameter greater than 0.2 mm. 13. The method as claimed in claim 10 , wherein at least 50% of said glass granules have a maximum particle diameter from 0.3 to 0.7 mm. 14. The method as claimed in claim 10 , wherein said glass granules are spherical. 15. A method for recovering metal(s) from a starting material comprising said metal(s), comprising: (i) leaching the starting material in a leaching solution to obtain a pregnant leaching solution; (ii) extracting the metal(s) from the pregnant leaching solution by a extraction solution comprising organic solvent(s) to obtain an organic solution comprising the metal(s); (iii) stripping metals(s) from the organic solution comprising the metal(s) with an aqueous solution to obtain an electrolyte solution comprising said metal(s); (iv) removing any remaining organic solvent(s) from the electrolyte solution by the method claimed in claim 1 , to obtain a purified electrolyte solution; and (v) recovering metal(s) from the purified electrolyte solution.
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Breaking emulsions · CPC title
with stationary filtering elements · CPC title
Inorganic material, e.g. asbestos fibres, glass beads or fibres · CPC title
Particle diameter · CPC title
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