US2002083795A1PendingUtilityA1
Purification of zinc bearing material solutions containing manganese
Priority: Apr 9, 1999Filed: Oct 9, 2001Published: Jul 4, 2002
Est. expiryApr 9, 2019(expired)· nominal 20-yr term from priority
Inventors:Cesar Ferron
C01G 45/10Y02P10/20C22B 3/44C22B 19/26
20
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Claims
Abstract
Disclosed herein is a process for removing at least a portion of a manganese constituent from a zinc-bearng material, comprising the step of subjecting the material to a first oxidation mixture of SO 2 and oxygen, at conditions sufficient to oxidize the manganese constituent
Claims
exact text as granted — not AI-modified1 . A process for removing at least a portion of a manganese constituent from a zinc-bearing material, comprising the step of subjecting said material to a first oxidation mixture of SO 2 and oxygen, at conditions sufficient to oxidize said manganese constituent.
2 . A process as defined in claim 1 wherein the material is maintained at a pH sufficient to precipitate manganese while minimizing precipitation of said zinc constituent.
3 . A process for removing at least a portion of a manganese constituent from a zinc-bearng material, comprising the step of subjecting said material to a first oxidation mixture of SO 2 and oxygen, at conditions sufficient to oxidize said manganese constituent, wherein the material is maintained at a pH between 3 and 4 to form a manganese precipitate and no zinc precipitate.
4 . A process as defined in claim 3 wherein said pH is 3.
5 . A process as defined in claim 3 wherein said oxygen is in the form of O 2 .
6 . A process as defined in claim 3 wherein said oxidation mixture includes Air.
7 . A process as defined in claim 3 wherein the subjecting step occurs at a temperature ranging from about 40 to about 80° C.
8 . A process as defined in claim 7 wherein the subjecting step occurs at a temperature ranging from 50 to 80° C.
9 . A process as defined in claim 8 wherein the subjecting step occurs temperature ranging from 58 to 78° C.
10 . A process as defined in claim 8 wherein the subjecting step occurs at about 70° C.
11 . A process as defined in claim 8 wherein the subjecting step occurs at about 60° C.
12 . A process as defined in claim 5 wherein said SO 2 is at a concentration from 0.5% to 10%, with the balance O 2 gas.
13 . A process as defined in claim 12 wherein said SO 2 is at a concentration from 1 to 8%.
14 . A process as defined in claim 13 wherein SO 2 is at a concentration from 2to 3%.
15 . A process as defined in claim 5 wherein SO 2 is at a concentration from 0.1% to 2%, with the balance being Air.
16 . A process as defined in claim 15 wherein said SO 2 is at a concentration from 0.2 to 14%.
17 . A process as defined in claim 16 wherein SO 2 is at a concentration Drum 0.4 to 0.6%.
18 . A process as defined in claim 5 wherein said zinc bearing material is a leach solution.
19 . A process as defined in claim 5 wherein said zinc material is an electrolyte solution.
20 . A process for removing a manganese impurity from a zinc-bearing solution, comprising the steps of:
subjecting the solution to a mixture of SO 2 and oxygen, at conditions sufficient to oxidize said manganese constituent as manganese oxide; and maintaining the pH of the solution between 3 and 4 to form a manganese with essentially no zinc co-precipitate.Join the waitlist — get patent alerts
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