CN113403649A - Deep purification method of electrolyte for electrolyzing metal manganese - Google Patents

Deep purification method of electrolyte for electrolyzing metal manganese Download PDF

Info

Publication number
CN113403649A
CN113403649A CN202110481769.XA CN202110481769A CN113403649A CN 113403649 A CN113403649 A CN 113403649A CN 202110481769 A CN202110481769 A CN 202110481769A CN 113403649 A CN113403649 A CN 113403649A
Authority
CN
China
Prior art keywords
manganese
ammonia water
adjust
electrolyte
value
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.)
Pending
Application number
CN202110481769.XA
Other languages
Chinese (zh)
Inventor
贾天将
张志华
宋正平
段锋
马林
张国举
刘磊
马鹏飞
陆宇
陈建红
李凯
虎大勇
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ningxia Tianyuan Manganese Material Research Institute Co ltd
Original Assignee
Ningxia Tianyuan Manganese Material Research Institute Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ningxia Tianyuan Manganese Material Research Institute Co ltd filed Critical Ningxia Tianyuan Manganese Material Research Institute Co ltd
Priority to CN202110481769.XA priority Critical patent/CN113403649A/en
Publication of CN113403649A publication Critical patent/CN113403649A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/06Operating or servicing
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/06Electrolytic production, recovery or refining of metals by electrolysis of solutions or iron group metals, refractory metals or manganese
    • C25C1/10Electrolytic production, recovery or refining of metals by electrolysis of solutions or iron group metals, refractory metals or manganese of chromium or manganese

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The invention belongs to the technical field of chemical engineering, and particularly relates to a deep purification method of electrolyte for electrolyzing metal manganese, which comprises the following steps: (1) adding ammonia water into a manganese sulfate solution in the electrolytic manganese metal electrolyte preparation process to adjust the pH value to 5-5.5; (2) introducing air, adding 6.5-6.8kg/m3 hydrogen peroxide and 0.19-0.21kg/m3 aluminum sulfate according to the proportion, and stirring for 4-6 h; (3) carrying out primary filter pressing; (4) neutralizing; adding ammonia water to adjust the pH value to 7.0-7.2; (5) adding hydrogen peroxide to remove iron, and adding SDD to remove heavy metals; (6) adding 0.5-0.7kg/m3 aluminum sulfate and fully stirring; (7) adding 2.7-2.9 kg/m3 active carbon for harmful impurity adsorption; (8) standing and separating; (9) and (5) secondary filter pressing. The invention improves the utilization rate of metal manganese ions, reduces the addition of auxiliary materials such as sulfuric acid and the like, reduces the treatment cost and improves the production benefit.

Description

Deep purification method of electrolyte for electrolyzing metal manganese
Technical Field
The invention belongs to the technical field of chemical engineering, and particularly relates to a deep purification method of electrolyte for electrolyzing metal manganese.
Background
Since the diaphragm electrolysis method for producing the manganese metal is proposed in the 20 th century, the neutral MnSO4- (NH4)2SO4-H2O series cathode liquid is adopted to carry out diaphragm electrolysis to produce the manganese metal all over the world, and ammonia and an antioxidant must be added in the electrolysis. A large amount of free NH3 exists in the electrolyte, so that ammonia precipitation reaction is serious in the electrolytic process, and the working environment of first-line workers is severe. Because the double salts such as magnesium ammonium sulfate and the like are seriously crystallized in the electrolytic process of the electrolytic manganese metal industry, the diaphragm bag is blocked, the ion migration is hindered, and the like, the alkali of the electrolytic cell can affect the product quality and the yield.
Aiming at the problem that no effective solution exists in the prior art of double salt crystallization, the problem of diaphragm bag blockage can be improved only by increasing the tank cleaning cycle frequency, which undoubtedly increases the production cost.
Disclosure of Invention
In order to solve the technical problems, the invention provides a deep purification method of electrolyte for electrolyzing metal manganese, which enables the pH of bath solution in an electrolytic bath to be stabilized at a higher level and ensures the normal and efficient operation of electrolysis.
A deep purification method of electrolyte for electrolyzing metal manganese comprises the following steps:
(1) adding ammonia water into a manganese sulfate solution in the electrolytic manganese metal electrolyte preparation process to adjust the pH value to 5-5.5;
(2) introducing air, adding 6.5-6.8kg/m3 hydrogen peroxide and 0.19-0.21kg/m3 aluminum sulfate according to the proportion, and stirring for 4-6 h;
(3) carrying out primary filter pressing;
(4) neutralizing; adding ammonia water to adjust the pH value to 7.0-7.2;
(5) adding hydrogen peroxide to remove iron, and adding SDD to remove heavy metals;
(6) adding 0.5-0.7kg/m3 aluminum sulfate and fully stirring;
(7) adding 2.7-2.9 kg/m3 active carbon for harmful impurity adsorption;
(8) standing and separating;
(9) and (5) secondary filter pressing.
Further, in the step (1), ammonia water is added into the manganese sulfate solution to adjust the pH value, and the acidity is 1.5-1.6 g/L.
Further, before adding ammonia water to adjust the pH value in the step (4), introducing air again and stirring, and simultaneously adding 0.5-0.7kg/m3 of aluminum sulfate.
Description of the mechanism: the PH is adjusted to 5.0 before neutralization, hydrogen peroxide is added, iron and heavy metal are removed after filter pressing, and aluminum sulfate activated carbon is added for electrolysis, so that the negative effect of the acidic feed liquor on the yield of the veneer is weakened; meanwhile, the change of the treatment mode enables the yield of the veneer to reach a higher level under the condition that the liquid inlet amount is normal.
Has the advantages that: the invention improves the utilization rate of metal manganese ions, reduces the addition of auxiliary materials such as sulfuric acid and the like, reduces the treatment cost and improves the production benefit.
Detailed Description
The present invention will be described in further detail with reference to specific examples.
Example one
A deep purification method of electrolyte for electrolyzing metal manganese comprises the following steps:
(1) adding ammonia water into a manganese sulfate solution in the process of preparing electrolytic manganese metal electrolyte to adjust the pH value, and adjusting the pH value to 5;
(2) introducing air, adding 6.5kg/m3 hydrogen peroxide and 0.19 aluminum sulfate according to the proportion, and stirring for 4 hours;
(3) carrying out primary filter pressing;
(4) neutralizing; adding ammonia water to adjust the pH value to 7.0;
(5) adding hydrogen peroxide to remove iron to micro iron, and adding SDD to remove heavy metals to a nickel-free state;
(6) adding 0.5 aluminum sulfate and fully stirring;
(7) adding 2.7 kg/m3 activated carbon for adsorbing harmful impurities;
(8) standing and separating;
(9) and (5) secondary filter pressing.
In the step (1), ammonia water is added into the manganese sulfate solution to adjust the pH value, and the acidity is 1.5 g/L.
Before adding ammonia water to adjust the pH value in the step (4), introducing air again and stirring, and simultaneously adding 0.5 kg/m3 of aluminum sulfate.
Carry out the electrolysis through above-mentioned scheme, the interior tank liquor pH level of electrolysis trough has great promotion, can stabilize about 7.3~7.4, guarantees the normal clear of electrolysis, has weakened the negative effect of acid feed liquor to veneer output.
Example two
A deep purification method of electrolyte for electrolyzing metal manganese comprises the following steps:
(1) adding ammonia water into a manganese sulfate solution in the process of preparing electrolytic manganese metal electrolyte to adjust the pH value, and adjusting the pH value to 5.5;
(2) introducing air, adding 6.8kg/m3 hydrogen peroxide and 0.21kg/m3 aluminum sulfate according to the proportion, and stirring for 6 hours;
(3) carrying out primary filter pressing;
(4) neutralizing; adding ammonia water to adjust the pH value to 7.2;
(5) adding hydrogen peroxide to remove iron, and adding SDD to remove heavy metals;
(6) 0.7kg/m3 aluminum sulfate was added and sufficiently stirred;
(7) adding 2.9 kg/m3 activated carbon for adsorbing harmful impurities;
(8) standing and separating;
(9) and (5) secondary filter pressing.
In the step (1), ammonia water is added into the manganese sulfate solution to adjust the pH value, and the acidity is 1.6 g/L.
Before adding ammonia water to adjust the pH value in the step (4), introducing air again and stirring, and simultaneously adding 0.7kg/m3 of aluminum sulfate.
Carry out the electrolysis through above-mentioned scheme, the interior tank liquor pH level of electrolysis trough has great promotion, can stabilize about 7.3~7.5, guarantees the normal clear of electrolysis, has weakened the negative effect of acid feed liquor to veneer output.
EXAMPLE III
A deep purification method of electrolyte for electrolyzing metal manganese comprises the following steps:
(1) adding ammonia water into a manganese sulfate solution in the process of preparing electrolytic manganese metal electrolyte to adjust the pH value, and adjusting the pH value to 5;
(2) introducing air, adding 6.5-6.8kg/m3 hydrogen peroxide and 0.19-0.21kg/m3 aluminum sulfate according to the proportion, and stirring for 4-6 h;
(3) carrying out primary filter pressing;
(4) neutralizing; adding ammonia water to adjust the pH value to 7.0;
(5) adding hydrogen peroxide to remove iron, and adding SDD to remove heavy metals;
(6) 0.6kg/m3 aluminum sulfate was added and sufficiently stirred;
(7) adding 2.8 kg/m3 activated carbon for adsorbing harmful impurities;
(8) standing and separating;
(9) and (5) secondary filter pressing.
Further, in the step (1), ammonia water is added into the manganese sulfate solution to adjust the pH value, and the acidity is 1.52 g/L.
Further, before the pH was adjusted by adding ammonia water in the step (4), air was again introduced and stirred while adding aluminum sulfate in an amount of 0.6kg/m 3.
Carry out the electrolysis through above-mentioned scheme, the interior tank liquor pH level of electrolysis trough has great promotion, can stabilize about 7.2~7.3, guarantees the normal clear of electrolysis, has weakened the negative effect of acid feed liquor to veneer output.
Description of the mechanism: adjusting the pH value to 5-5.5 before neutralization, adding hydrogen peroxide, removing iron and heavy metals after filter pressing, and adding aluminum sulfate activated carbon for electrolysis, so that the negative effect of acidic feed liquor on the yield of the veneer is weakened; meanwhile, the change of the treatment mode enables the yield of the single plate to reach a higher level under the condition of normal liquid inlet amount, the utilization rate of the metal manganese ions to be obviously improved, and the addition of auxiliary materials such as activated carbon, aluminum sulfate, hydrogen peroxide, sulfuric acid and the like is correspondingly reduced.
In conclusion, the invention has the following obvious advantages: the invention improves the utilization rate of metal manganese ions, reduces the addition of auxiliary materials such as sulfuric acid and the like, reduces the treatment cost and improves the production benefit.
Finally, it should be noted that: the above examples are only intended to illustrate the technical solution of the present invention, but not to limit it; although the present invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; and the modifications or the substitutions do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.

Claims (3)

1. A deep purification method of electrolyte for electrolyzing metal manganese is characterized in that the purification process comprises the following steps:
(1) adding ammonia water into a manganese sulfate solution in the electrolytic manganese metal electrolyte preparation process to adjust the pH value to 5-5.5;
(2) introducing air, adding 6.5-6.8kg/m3 hydrogen peroxide and 0.19-0.21kg/m3 aluminum sulfate according to the proportion, and stirring for 4-6 h;
(3) carrying out primary filter pressing;
(4) neutralizing; adding ammonia water to adjust the pH value to 7.0-7.2;
(5) adding hydrogen peroxide to remove iron, and adding SDD to remove heavy metals;
(6) adding 0.5-0.7kg/m3 aluminum sulfate and fully stirring;
(7) adding 2.7-2.9 kg/m3 active carbon for harmful impurity adsorption;
(8) standing and separating;
(9) and (5) secondary filter pressing.
2. The method for deeply purifying an electrolytic manganese metal as claimed in claim 1, wherein in the step (1), the pH of the manganese sulfate solution is adjusted to 1.5 to 1.6g/L by adding ammonia water.
3. The method for deep purification of an electrolytic solution for electrolytic manganese metal according to claim 1, wherein before the addition of ammonia water to adjust the pH in the step (4), air is again introduced and stirred while adding aluminum sulfate in an amount of 0.5 to 0.7kg/m 3.
CN202110481769.XA 2021-04-30 2021-04-30 Deep purification method of electrolyte for electrolyzing metal manganese Pending CN113403649A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110481769.XA CN113403649A (en) 2021-04-30 2021-04-30 Deep purification method of electrolyte for electrolyzing metal manganese

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110481769.XA CN113403649A (en) 2021-04-30 2021-04-30 Deep purification method of electrolyte for electrolyzing metal manganese

Publications (1)

Publication Number Publication Date
CN113403649A true CN113403649A (en) 2021-09-17

Family

ID=77677791

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110481769.XA Pending CN113403649A (en) 2021-04-30 2021-04-30 Deep purification method of electrolyte for electrolyzing metal manganese

Country Status (1)

Country Link
CN (1) CN113403649A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103014760A (en) * 2013-01-09 2013-04-03 广西有色金属集团汇元锰业有限公司 Production method of electrolytic manganese metal
CN103074490A (en) * 2013-01-09 2013-05-01 广西有色金属集团汇元锰业有限公司 Purification method in electrolytic metal manganese production process by multi-mine method
CN103451423A (en) * 2013-09-04 2013-12-18 宁夏天元锰业有限公司 Solution preparation method of electrolytic manganese metal
CN106637295A (en) * 2016-12-09 2017-05-10 宁夏天元锰业有限公司 Purifying method for process of preparing electrolytic manganese metal electrolyte
JP2017178749A (en) * 2016-03-31 2017-10-05 東ソー株式会社 Method for producing manganese sulfate aqueous solution and method for producing manganese oxide

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103014760A (en) * 2013-01-09 2013-04-03 广西有色金属集团汇元锰业有限公司 Production method of electrolytic manganese metal
CN103074490A (en) * 2013-01-09 2013-05-01 广西有色金属集团汇元锰业有限公司 Purification method in electrolytic metal manganese production process by multi-mine method
CN103451423A (en) * 2013-09-04 2013-12-18 宁夏天元锰业有限公司 Solution preparation method of electrolytic manganese metal
JP2017178749A (en) * 2016-03-31 2017-10-05 東ソー株式会社 Method for producing manganese sulfate aqueous solution and method for producing manganese oxide
CN106637295A (en) * 2016-12-09 2017-05-10 宁夏天元锰业有限公司 Purifying method for process of preparing electrolytic manganese metal electrolyte

Similar Documents

Publication Publication Date Title
CN112939090B (en) Manganese sulfate purification and crystallization method
US20200039838A1 (en) System for extracting vanadium from leaching solution containing vanadium chromium silicon and for preparing vanadium pentoxide and processing method therefor
CN116334410A (en) Method for separating lithium from lithium-containing electrolyte waste residues in aluminum electrolysis
CN114524572A (en) Comprehensive treatment method for wastewater generated in iron phosphate production
CN113336260B (en) Method for recovering copper sulfate in acidic copper sulfate waste liquid
CN110734181A (en) deacidification wastewater treatment process
CN111187906B (en) Method for purifying manganese sulfate solution
CN113403649A (en) Deep purification method of electrolyte for electrolyzing metal manganese
CN106637295A (en) Purifying method for process of preparing electrolytic manganese metal electrolyte
CN217709144U (en) Ferric phosphate effluent disposal system
KR20180064753A (en) Methods for waste water treatment of Nitrogen trifluoride(NF3) process
CN111041248A (en) Method for recovering valuable metals in chlorine-containing waste liquid
CN116102211A (en) Method for treating synthesis wastewater of battery anode material precursor
CN102660756B (en) High-purity manganese metal and preparation method thereof
CN102649584B (en) Preparation method of sodium bichromate
CN108977842B (en) Process for producing cobalt sulfamate by ionic membrane multistage electrolysis method
CN108793546B (en) Method for recovering sodium chloride from sodium chlorate wastewater
CN111003699A (en) Method for producing feed-grade calcium hydrophosphate and co-producing industrial-grade calcium chloride by hydrochloric acid method
CN115072751B (en) Method for preparing low-fluorine lithium carbonate by recycling lithium iron phosphate battery
CN110983054A (en) Method for separating and recovering cobalt and nickel from manganese sulfate solution
CN210559435U (en) Device for separating and preparing manganese carbonate from manganese-containing wastewater
CN114628664B (en) Processing method of lithium iron phosphate anode material
CN116282163B (en) Method for improving quality of chromic anhydride
CN115109950B (en) Method for producing germanium concentrate by back extraction from hydroxamic acid loaded organic phase
CN115491499B (en) Method for separating and recovering strontium from zinc anode slime

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20210917

WD01 Invention patent application deemed withdrawn after publication