Patent US4067789A successfully refreshed from Google Patents.
US4067789A
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Process for manganese removal from zinc metal bearing solutions
Assignee: Newmont Exploration Ltd
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Filing: 1976-05-03
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Granted: 1978-01-10
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Expires: 1996-05-03
Abstract
Abstract A process for the preferential removal of soluble manganous ions from a metal bearing solution, particularly a zinc sulfate solution to be subjected to electrolysis for the recovery of zinc, comprising treating said solution with an oxidant capable of oxidizing soluble manganous ion to insoluble and filterable gamma-manganese dioxide at a temperature and for a time sufficient to precipitate at least a portion of the manganese present in said solution as gamma-manganese dioxide, said oxidant being in an amount of from about 130% to 150% of the theoretical amount required for substantially total manganese removal from said solution, and separating said precipitate from said solution.
Inventors
- 👤 Leonard Harris
- 👤 Alfred K. Hanson, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 01:38
CPC Classifications
C; C01; C01G; C01G45/00; C01G45/02; C01G45/024; C01G9/00; C01G9/06; C22; C22B; C22B19/00; C22B19/20; C22B19/26; C01P; C01P2002/00; C01P2002/70; C01P2002/72; C01P2002/74; C01P2006/00; C01P2006/80; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
102 words
A process for removal of soluble manganous ions from a zinc sulfate bearing solution containing the same comprising the steps of treating said solution, or a portion of said solution, with an oxidant capable of oxidizing soluble manganous ion to insoluble and filterable gamma-manganese dioxide at a temperature and for a time sufficient to precipitate at least a portion of the manganous ion present in said solution as gamma-manganese dioxide, said oxidant being in an amount of from about 130% to 150% of the theoretical amount required for substantially total manganese removal from said solution, and separating said precipitate from said solution.
Claim 2
Dependent Claim
102 words
A process for removal of soluble manganous ions from a zinc sulfate bearing solution containing the same comprising the steps of treating said solution, or a portion of said solution, with an oxidant capable of oxidizing soluble manganous ion to insoluble and filterable gamma-manganese dioxide at a temperature and for a time sufficient to precipitate at least a portion of the manganous ion present in said solution as gamma-manganese dioxide, said oxidant being in an amount of from about 130% to 150% of the theoretical amount required for substantially total manganese removal from said solution, and separating said precipitate from said solution.
Claim 3
Dependent Claim
31 words
The process of claim 1 wherein the temperature is from about 90° C. to the boiling temperature of said solution, and the time is from about 30 minutes to two hours.
Claim 4
Dependent Claim
25 words
The process of claim 2 wherein the oxidant is ammonium persulfate, sodium persulfate, potassium persulfate, sodium bismuthate, sodium bromate, lead dioxide, or a mixture thereof.
Claim 5
Dependent Claim
40 words
The process of claim 3 wherein the zinc sulfate bearing solution is at a pH of from about 5 to 12, the oxidant is ammonium persulfate, the reaction time is about 2 hours, and the temperature is about 90° C.
Claim 6
Dependent Claim
52 words
The process of claim 3 wherein the manganese-free solution is returned for use in a hot acid leach circuit of an electrolytic zinc recovery process whereby the contained ammonium, sodium or potassium ions and sulfate ions are employed for the precipitation of iron as jarosite from an iron containing electrolytic leach solution.
Claim 7
Dependent Claim
130 words
In the process of recovering zinc from a manganese containing zinc concentrate wherein the concentrate is roasted and leached with an acid to solubilize the zinc, the resultant solution treated to remove any iron therefrom as jarosite, and then subjected to electrolysis to recover the zinc, the improvement comprising admixing with a portion of said solution prior to electrolysis an oxidant capable of oxidizing soluble manganous ion to insoluble and filterable gamma-manganese dioxide at a temperature and for a time sufficient to precipitate at least a portion of the manganous ion present in said solution as gamma-manganese dioxide, said oxidant being in an amount of from about 130% to 150% of the theoretical amount required for substantially total manganese removal from said solution, and separating said precipitate from said solution.
Claim 8
Dependent Claim
130 words
In the process of recovering zinc from a manganese containing zinc concentrate wherein the concentrate is roasted and leached with an acid to solubilize the zinc, the resultant solution treated to remove any iron therefrom as jarosite, and then subjected to electrolysis to recover the zinc, the improvement comprising admixing with a portion of said solution prior to electrolysis an oxidant capable of oxidizing soluble manganous ion to insoluble and filterable gamma-manganese dioxide at a temperature and for a time sufficient to precipitate at least a portion of the manganous ion present in said solution as gamma-manganese dioxide, said oxidant being in an amount of from about 130% to 150% of the theoretical amount required for substantially total manganese removal from said solution, and separating said precipitate from said solution.
Claim 9
Dependent Claim
48 words
The process of claim 6 wherein the oxidant is ammonium persulfate, sodium persulfate, or potassium persulfate, the temperature is from about 90° C. to the boiling temperature of said solution, the time is about 2 hours, and the pH of the solution is from about 5 to 12.
Claim 10
Dependent Claim
38 words
The process of claim 7 wherein the oxidant is ammonium persulfate, in an amount of 135% of said theoretical amount, the temperature is about 90° C., the time is about 2 hours, and the pH is about 5.5.
Claim 11
Dependent Claim
52 words
The process of claim 7 wherein the manganese-free solution is returned for use in a hot acid leach circuit of an electrolytic zinc recovery process whereby the contained ammonium, sodium or potassium ions and sulfate ions are employed for the precipitation of iron as jarosite from an iron containing electrolytic leach solution.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-01-09 | 1981-07-11 | 1982-01-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-01-09 | 1985-07-11 | 1986-01-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-01-09 | 1989-07-11 | 1990-01-10 | $7700.00 | Window Closed / Lapsed |