US2396570A - Methods for purifying manganese in metal state - Google Patents
Methods for purifying manganese in metal state Download PDFInfo
- Publication number
- US2396570A US2396570A US411429A US41142941A US2396570A US 2396570 A US2396570 A US 2396570A US 411429 A US411429 A US 411429A US 41142941 A US41142941 A US 41142941A US 2396570 A US2396570 A US 2396570A
- Authority
- US
- United States
- Prior art keywords
- manganese
- iron
- solution
- methods
- metal state
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 title description 20
- 229910052748 manganese Inorganic materials 0.000 title description 20
- 239000011572 manganese Substances 0.000 title description 20
- 238000000034 method Methods 0.000 title description 10
- 229910052751 metal Inorganic materials 0.000 title description 4
- 239000002184 metal Substances 0.000 title description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 28
- 229910052742 iron Inorganic materials 0.000 description 14
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 12
- 239000012535 impurity Substances 0.000 description 8
- 238000005868 electrolysis reaction Methods 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 5
- 230000003472 neutralizing effect Effects 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 238000006386 neutralization reaction Methods 0.000 description 4
- 239000007800 oxidant agent Substances 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000001117 sulphuric acid Substances 0.000 description 3
- 235000011149 sulphuric acid Nutrition 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 239000011702 manganese sulphate Substances 0.000 description 2
- 235000007079 manganese sulphate Nutrition 0.000 description 2
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 239000001166 ammonium sulphate Substances 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 1
- 150000002696 manganese Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- WBHQBSYUUJJSRZ-UHFFFAOYSA-M sodium bisulfate Chemical compound [Na+].OS([O-])(=O)=O WBHQBSYUUJJSRZ-UHFFFAOYSA-M 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B47/00—Obtaining manganese
Definitions
- manganese ores are rarely found in pure state in nature and metallic manganese and particularly free from iron is not easily obtained directly from manganese ores.
- This invention is directed to a method for purifying manganese and by means of the method of this invention iron and other impurities may be removed therefrom; in the method of this invention manganese and iron and other impurities contained in metallic manganese are converted into soluble salts by an attack by means of acid and subsequently iron and other impurities are precipitated by the addition of an oxidising agent followed by a neutralisation step; thereafter the precipitate containing the whole of iron and impurities present in the initial metal is separated by physical means and the solution of manganese salt is treated, preferably by electrolysis, to obtain pure manganese.
- the electrolysis step is effected with advantage in a suitable manner to obtain and hold the anolyte and catholyte separate from each other for their re-use in the process.
- Manganese dioxide is preferably used as oxidising agent for precipitating iron, and for such a purpose manganese dioxide obtained in said electrolysis step'is used with advantage because it is in pure state and does not introduce foreign substances in the solution.
- An oxidising agent is added to said solution, preferably manganese dioxide (MnOz) and thus iron present in the solution is converted into ferric state (Fe2(SO4)3) manganese being converted to the state of manganous salt (M11804).
- MnOz manganese dioxide
- Fe2(SO4)3 ferric state
- the solution is neutralised by an addition of a neutralizing agent as calcium carbonate or ammonia in gas or solution, in presence of ammonia salts; iron is thus precipitated as ferric hydrate.
- a neutralizing agent as calcium carbonate or ammonia in gas or solution, in presence of ammonia salts; iron is thus precipitated as ferric hydrate.
- the neutralisation step may be effected with advantage by using as neutralising agent the catholyte obtained from the subsequent electrolysis step.
- the precipitate is separated and the pure solution thus obtained is electrolysed with cathodes 80 made of aluminium or of stainless steel and with lead anodes, use being made of partitions of porous porcelain or bags of glass filaments and fabric and asbesto sheets to recover the anolyte and catholyte separately. Thereafter the manganese cathodes thus obtained are removed from the cathodes of the electrolysis cell pure manganese dioxide being obtained on the lead anodes for re-use in the process.
- the solution of metal manganese may if de- 49 sired be effected by means of other mineral acids such as hydrochloric acid; the corresponding salts of manganese and iron are thus obtained and iron is subsequently precipitated by an oxidation I step and thereafter the process is prosecuted in re-use in the process and introducing said catholyte in said neutralizing step, said anolyte, in said dissolving step and the manganese dioxide formed at theanode in the oxidizing step.
- other mineral acids such as hydrochloric acid
- a method for separating manganese from its ores having a content ofimpurities including iron consisting in dissolving said manganese by an acid to bring it in solution, adding an oxidising agent to said solution, neutralizing said solution by the addition 01 anfalkaline agent to cause the precipitation oi said -lliip lrities therefrom, electrolysing said solutionsto obtain manganese in pure state, said electrolysis step being carried out'by means of porous separating partitions and the anolyte and catholyte obtained in said electrolysis step being held separate from each other, and introducing said catholyte in said solution neutralising step and said anolyte in the said dissolution step.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
Patented Mar. 12, 1946 UNITED STATES PATENT .orncs Pietro Guareschi, Genoa, Italy; vested in the Alien Property Custodian No Drawing. Application September 18, 1941, Serial No. 411,429. In Italy October 8, 1940 2 Claims.
As known, manganese ores are rarely found in pure state in nature and metallic manganese and particularly free from iron is not easily obtained directly from manganese ores.
This invention is directed to a method for purifying manganese and by means of the method of this invention iron and other impurities may be removed therefrom; in the method of this invention manganese and iron and other impurities contained in metallic manganese are converted into soluble salts by an attack by means of acid and subsequently iron and other impurities are precipitated by the addition of an oxidising agent followed by a neutralisation step; thereafter the precipitate containing the whole of iron and impurities present in the initial metal is separated by physical means and the solution of manganese salt is treated, preferably by electrolysis, to obtain pure manganese.
The electrolysis step is effected with advantage in a suitable manner to obtain and hold the anolyte and catholyte separate from each other for their re-use in the process.
Manganese dioxide is preferably used as oxidising agent for precipitating iron, and for such a purpose manganese dioxide obtained in said electrolysis step'is used with advantage because it is in pure state and does not introduce foreign substances in the solution.
An embodiment of the method of this invention is hereinafter described by way of example.
Metallic manganese which is impure mainly because of a content of iron therein, is treated with sulphuric acid or sodium bisulphate; thus a solution is obtained which consists of man- 35 ganese sulphate and ferrous sulphate.
An oxidising agent is added to said solution, preferably manganese dioxide (MnOz) and thus iron present in the solution is converted into ferric state (Fe2(SO4)3) manganese being converted to the state of manganous salt (M11804).
Subsequently the solution is neutralised by an addition of a neutralizing agent as calcium carbonate or ammonia in gas or solution, in presence of ammonia salts; iron is thus precipitated as ferric hydrate. The neutralisation step may be effected with advantage by using as neutralising agent the catholyte obtained from the subsequent electrolysis step.
Then the precipitate is separated, this operation being effected physically by means of a decanter and a vacuum filter; thus a solution of M11304 free of impurities is obtained which is subsequently treated for deposition of manganese fected before the neutralisation one.
By way of example to recover one kilogramme' of manganese from a certain weight of manganese with an impurity content due to the presence of iron, silicon and other impurities therein, said metal manganese is comminuted and subsequently it is leached with dilute sulphuric acid (having a content of about 20% of sulphuric acid) to obtain manganese sulphate; to the solu- 20 tion of manganese sulphate an excess of manganese dioxide and then about 5 kilogrammes of ammonium sulphate and ammonia are added to secure the neutralisation of the acid liquor. Iron and other impurities are thus precipitated, 25 including silicon which is partly oxidised and partly removed in the state of silicic anhydride during the attack step.
The precipitate is separated and the pure solution thus obtained is electrolysed with cathodes 80 made of aluminium or of stainless steel and with lead anodes, use being made of partitions of porous porcelain or bags of glass filaments and fabric and asbesto sheets to recover the anolyte and catholyte separately. Thereafter the manganese cathodes thus obtained are removed from the cathodes of the electrolysis cell pure manganese dioxide being obtained on the lead anodes for re-use in the process.
The solution of metal manganese may if de- 49 sired be effected by means of other mineral acids such as hydrochloric acid; the corresponding salts of manganese and iron are thus obtained and iron is subsequently precipitated by an oxidation I step and thereafter the process is prosecuted in re-use in the process and introducing said catholyte in said neutralizing step, said anolyte, in said dissolving step and the manganese dioxide formed at theanode in the oxidizing step.
2. A method for separating manganese from its ores having a content ofimpurities including iron. consisting in dissolving said manganese by an acid to bring it in solution, adding an oxidising agent to said solution, neutralizing said solution by the addition 01 anfalkaline agent to cause the precipitation oi said -lliip lrities therefrom, electrolysing said solutionsto obtain manganese in pure state, said electrolysis step being carried out'by means of porous separating partitions and the anolyte and catholyte obtained in said electrolysis step being held separate from each other, and introducing said catholyte in said solution neutralising step and said anolyte in the said dissolution step.
PIEI'RO GUARESCHI.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT2396570X | 1940-10-08 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2396570A true US2396570A (en) | 1946-03-12 |
Family
ID=11435470
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US411429A Expired - Lifetime US2396570A (en) | 1940-10-08 | 1941-09-18 | Methods for purifying manganese in metal state |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2396570A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2798038A (en) * | 1953-12-02 | 1957-07-02 | Reginald S Dean | Electrodepositing manganese |
-
1941
- 1941-09-18 US US411429A patent/US2396570A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2798038A (en) * | 1953-12-02 | 1957-07-02 | Reginald S Dean | Electrodepositing manganese |
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