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US3900385A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for continuous production of electrolytic manganese dioxide

Assignee: Mitsui Kinzoku Co Ltd
•
Filing: 1973-12-11
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Granted: 1975-08-19
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Expires: 1993-12-11
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Abstract

Abstract Method for continuous production of electrolytic manganese dioxide by electrolysis with an aqueous solution of manganese sulfate-sulfuric acid containing as impurity 30 g/l or more of magnesium in the form of magnesium sulfate while making up for consumed manganese by addition of a neutral aqueous manganese sulfate solution to electrolyte, is improved by concentrating said neutral aqueous manganese sulfate solution under reduced pressure at 40*C - 60*C to the volume corresponding to saturation point at from 15*C to 60*C and then cooling it to 15*C - 25*C. Crystal thus precipitated which mainly consists of magnesium sulfate is filtered away and the filtrate is added to the electrolyte to compensate for the consumed manganese. During electrolysis the concentration of magnesium in the form of magnesium sulfate is maintained at 45 g/l or less for avoiding troubles caused by the accumulation of magnesium sulfate in the electrolyte.

Inventors

  • 👤 Akio Era
  • 👤 Takeo Emoto

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 05:52
CPC Classifications
C; C25; C25B; C25B1/00; C25B1/01; C25B1/21

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 155 words
IN A METHOD FOR CONTINUOUS PRODUCTION OF ELECTROLYTIC MANGANESE DIOXIDE BY ELECTROLYSIS OF AN AQUEOUS MANGANESE SULFATE - SUFLURIC ACID SOLUTION CONTAINING 30 G/L OR MORE OF MAGANESIUM IN THE FORM OF MAGNESIUM SULFATE AS IMPURITY WHEREIN CONSUMED MANGANESE IS MADE UP FOR BY SUPPLYING A NEUTRAL AQUEOUS MANGANESE SULFATE SOLUTION PREPARED BY LEACHING OF MANGANESE ORE WHICH CONTAINS MAGNESIUM AS IMPURITY WITH SPENT ELECTROLYTE AND SULFURIC ACID FOLLOWED BY NEUTRALIZATION AND FILTRATION, THE IMPROVEMENT COMPRISING CONCENTRATING THE WHOLE AMOUNT OF OR A PART OF THE NEUTRAL MANGANESE SULFATE SOLUTION IN A VACUUM AT A TEMPERATUE OF BETWEEN 40*C. AND 60*C TO PRODUCE A SOLUTION HAVING A CONCENTRATION CORRESPONDING TO A SATURATION POINT AT FROM 15*C. TO 60*C., AND THEN RAPIDLY COOLING THE RESULTANT SOLUTION TO 15*C. - 25*C., TO GIVE CRYSTAL CONTAINING MAGNESIUM SULFATE, FILTERING AWAY THE CRYSTAL AND FEEDING THE FILTRATE TO THE ELECTROLYTIC CELL TO MAKE UP FOR THE WHOLE AMOUNT OF
Claim 2
Dependent Claim 155 words
IN A METHOD FOR CONTINUOUS PRODUCTION OF ELECTROLYTIC MANGANESE DIOXIDE BY ELECTROLYSIS OF AN AQUEOUS MANGANESE SULFATE - SUFLURIC ACID SOLUTION CONTAINING 30 G/L OR MORE OF MAGANESIUM IN THE FORM OF MAGNESIUM SULFATE AS IMPURITY WHEREIN CONSUMED MANGANESE IS MADE UP FOR BY SUPPLYING A NEUTRAL AQUEOUS MANGANESE SULFATE SOLUTION PREPARED BY LEACHING OF MANGANESE ORE WHICH CONTAINS MAGNESIUM AS IMPURITY WITH SPENT ELECTROLYTE AND SULFURIC ACID FOLLOWED BY NEUTRALIZATION AND FILTRATION, THE IMPROVEMENT COMPRISING CONCENTRATING THE WHOLE AMOUNT OF OR A PART OF THE NEUTRAL MANGANESE SULFATE SOLUTION IN A VACUUM AT A TEMPERATUE OF BETWEEN 40*C. AND 60*C TO PRODUCE A SOLUTION HAVING A CONCENTRATION CORRESPONDING TO A SATURATION POINT AT FROM 15*C. TO 60*C., AND THEN RAPIDLY COOLING THE RESULTANT SOLUTION TO 15*C. - 25*C., TO GIVE CRYSTAL CONTAINING MAGNESIUM SULFATE, FILTERING AWAY THE CRYSTAL AND FEEDING THE FILTRATE TO THE ELECTROLYTIC CELL TO MAKE UP FOR THE WHOLE AMOUNT OF
Claim 3
Dependent Claim 36 words
Method as defined by claim 1 wherein said spent electrolyte contains 10 - 40 g/l of manganese in the form of manganese sulfate and 30 - 45 g/l of magnesium in the form of magnesium sulfate.
Claim 4
Dependent Claim 39 words
Method as defined by claim 1 wherein said neutral aqueous manganese sulfate solution contains 40 - 70 g/l of manganese in the form of manganese sulfate and 30 - 50 g/l of magnesium in the form of magnesium sulfate.
Claim 5
Dependent Claim 16 words
Method as defined by claim 1 wherein electrolysis is carried out while blowing in live steam.
Claim 6
Dependent Claim 220 words
In a method for production of electrolytic manganese dioxide by electrolysis of an aqueous manganese sulfate - sulfuric acid solution containing 10 - 40 g/l of manganese in the form of manganese sulfate and as impurity 30 - 45 g/l of magnesium in the form of magnesium sulfate, wherein consumed manganese is made up for by supplying a neutral manganese sulfate solution containing 40 - 70 g/l of manganese in the form of manganese sulfate and 30 - 50 g/l of magnesium in the form of magnesium sulfate, said neutral solution being prepared by leaching manganese ore containing magnesium as impurity with a spent electrolyte followed by neutralization and filtration; the improvement comprising concentrating the whole amount of or a part of said neutral aqueous solution of manganese sulfate in a vacuum at a temperature between 40*C. and 60*C. to produce a solution having a concentration corresponding to a saturation point at from 15*C. to 60*C., and then rapidly cooling the resultant solution to 15*- 25*C., to give crystal containing magnesium sulfate, filtering away the crystal and feeding the filtrate to the electrolytic taNk to make up for the whole amount of or a part of consumed manganese, whereby the content of magnesium in the form of magnesium sulfate in the electrolyte is maintained at not more than 45 g/l.
Claim 7
Dependent Claim 220 words
In a method for production of electrolytic manganese dioxide by electrolysis of an aqueous manganese sulfate - sulfuric acid solution containing 10 - 40 g/l of manganese in the form of manganese sulfate and as impurity 30 - 45 g/l of magnesium in the form of magnesium sulfate, wherein consumed manganese is made up for by supplying a neutral manganese sulfate solution containing 40 - 70 g/l of manganese in the form of manganese sulfate and 30 - 50 g/l of magnesium in the form of magnesium sulfate, said neutral solution being prepared by leaching manganese ore containing magnesium as impurity with a spent electrolyte followed by neutralization and filtration; the improvement comprising concentrating the whole amount of or a part of said neutral aqueous solution of manganese sulfate in a vacuum at a temperature between 40*C. and 60*C. to produce a solution having a concentration corresponding to a saturation point at from 15*C. to 60*C., and then rapidly cooling the resultant solution to 15*- 25*C., to give crystal containing magnesium sulfate, filtering away the crystal and feeding the filtrate to the electrolytic taNk to make up for the whole amount of or a part of consumed manganese, whereby the content of magnesium in the form of magnesium sulfate in the electrolyte is maintained at not more than 45 g/l.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-08-18 1979-02-17 1979-08-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-08-18 1983-02-17 1983-08-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-08-18 1987-02-17 1987-08-19 $7700.00 Window Closed / Lapsed

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