CN103779617A - Method for adding carbonate into lead electrolyte to treat hydrofluoric acid - Google Patents

Method for adding carbonate into lead electrolyte to treat hydrofluoric acid Download PDF

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Publication number
CN103779617A
CN103779617A CN201210411542.9A CN201210411542A CN103779617A CN 103779617 A CN103779617 A CN 103779617A CN 201210411542 A CN201210411542 A CN 201210411542A CN 103779617 A CN103779617 A CN 103779617A
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Prior art keywords
hydrofluoric acid
lead
acid
carbonate
lead oxide
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CN201210411542.9A
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CN103779617B (en
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梁达保
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/06Lead-acid accumulators
    • H01M10/12Construction or manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0002Aqueous electrolytes
    • H01M2300/0005Acid electrolytes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention relates to a method for adding carbonate into lead electrolyte to treat hydrofluoric acid. The lead electrolyte is lead silicofluoride obtained through reaction between industrial silicofluoric acid and lead oxide. The method comprises the following steps of (1) adding silica powder into the industrial silicofluoric acid, wherein the silica powder reacts with hydrofluoric acid to generate silicofluoride, so as to remove a part of the hydrofluoric acid; (2) adding a certain amount of carbonate, and adding the lead oxide after the hydrofluoric acid is removed. The method has the beneficial effects that the using amount of the lead oxide is reduced; the added carbonate is low in cost, so that the cost can be effectively lowered.

Description

In lead electrolytic solution, add the method for processes of carbonate treatment hydrofluoric acid
Technical field
The present invention relates to chemical technology field, especially relate to a kind of method that adds processes of carbonate treatment hydrofluoric acid in lead electrolytic solution.
Background technology
Lead electrolytic solution of many uses, such as can be as the electrolyte of lead acid accumulator.Lead electrolytic solution obtains fluosilicic lead plumbate by industrial fluorosilicic acid and lead oxide reaction conventionally.React as follows:
H 2SiF 6+PbO->PbSiF 6+H 2O
In industrial fluorosilicic acid, hydrofluoric acid meeting and lead oxide reaction, consume lead oxide.Therefore industrial fluorosilicic acid needs to purify in the time making lead electrolytic solution, removes fluohydric acid content in industrial fluorosilicic acid.General hydrofluoric acid reaction needed adds a certain amount of Cab-O-sil, after exothermic reaction, generate silicofluoric acid, but can not thoroughly fully react completely in course of reaction, remaining hydrofluoric acid will react with lead oxide, owing to having consumed expensive lead oxide, cause production cost higher.
Summary of the invention
The present invention will address the above problem exactly, and a kind of method that adds processes of carbonate treatment hydrofluoric acid in lead electrolytic solution is provided.
The technical solution adopted for the present invention to solve the technical problems is:
In lead electrolytic solution, add a method for processes of carbonate treatment hydrofluoric acid, described lead electrolytic solution obtains fluosilicic lead plumbate by industrial fluorosilicic acid and lead oxide reaction, it is characterized in that, comprises the steps:
(1) in industrial fluorosilicic acid, add Cab-O-sil, Cab-O-sil and hydrofluoric acid reaction generate silicofluoric acid, thereby remove a part of hydrofluoric acid;
(2) add a certain amount of carbonate, add again lead oxide after removing hydrofluoric acid.
Further, described carbonate is calcium carbonate or calcium bicarbonate.
Operation principle of the present invention:
Old technique: industrial fluorosilicic acid-Jia Cab-O-sil-generation silicofluoric acid-Jia lead oxide-electrolyte;
New technology: industrial fluorosilicic acid-Jia Cab-O-sil-generation silicofluoric acid-Jia carbonate-Jia lead oxide-electrolyte.
Beneficial effect of the present invention: reduce the use amount of lead oxide, the carbonate adding is with low cost, can effectively reduce costs.
Embodiment
In lead electrolytic solution, add a method for processes of carbonate treatment hydrofluoric acid, described lead electrolytic solution obtains fluosilicic lead plumbate by industrial fluorosilicic acid and lead oxide reaction, it is characterized in that, comprises the steps:
(1) in industrial fluorosilicic acid, add Cab-O-sil, Cab-O-sil and hydrofluoric acid reaction generate silicofluoric acid, thereby remove a part of hydrofluoric acid;
(2) add a certain amount of carbonate, add again lead oxide after removing hydrofluoric acid.
Operation principle of the present invention:
Old technique: industrial fluorosilicic acid-Jia Cab-O-sil-generation silicofluoric acid-Jia lead oxide-electrolyte;
New technology: industrial fluorosilicic acid-Jia Cab-O-sil-generation silicofluoric acid-Jia carbonate-Jia lead oxide-electrolyte.
Embodiment 1:
Described carbonate is chosen as calcium bicarbonate
2HF+Ca(HCO 3) 2->CaF 2+2H 2O+2CO 2
Calcium bicarbonate can react with hydrofluoric acid, removes hydrofluoric acid, adds afterwards lead oxide again, just can avoid hydrofluoric acid and lead oxide to react, thereby reduces the use amount of lead oxide, can reduce costs.
Embodiment 2:
Described carbonate is chosen as calcium carbonate
2HF+CaCO 3->CaF 2+H 2O+CO 2
Calcium carbonate can react with hydrofluoric acid, removes hydrofluoric acid, adds afterwards lead oxide again, just can avoid hydrofluoric acid and lead oxide to react, thereby reduces the use amount of lead oxide, can reduce costs.

Claims (2)

1. in lead electrolytic solution, add a method for processes of carbonate treatment hydrofluoric acid, described lead electrolytic solution obtains fluosilicic lead plumbate by industrial fluorosilicic acid and lead oxide reaction, it is characterized in that, comprises the steps:
(1) in industrial fluorosilicic acid, add Cab-O-sil, Cab-O-sil and hydrofluoric acid reaction generate silicofluoric acid, thereby remove a part of hydrofluoric acid;
(2) add a certain amount of carbonate, add again lead oxide after removing hydrofluoric acid.
2. method according to claim 1, is characterized in that, described carbonate is calcium carbonate or calcium bicarbonate.
CN201210411542.9A 2012-10-25 2012-10-25 The method adding processes of carbonate treatment Fluohydric acid. in lead electrolytic solution Expired - Fee Related CN103779617B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210411542.9A CN103779617B (en) 2012-10-25 2012-10-25 The method adding processes of carbonate treatment Fluohydric acid. in lead electrolytic solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210411542.9A CN103779617B (en) 2012-10-25 2012-10-25 The method adding processes of carbonate treatment Fluohydric acid. in lead electrolytic solution

Publications (2)

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CN103779617A true CN103779617A (en) 2014-05-07
CN103779617B CN103779617B (en) 2016-08-17

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CN201210411542.9A Expired - Fee Related CN103779617B (en) 2012-10-25 2012-10-25 The method adding processes of carbonate treatment Fluohydric acid. in lead electrolytic solution

Country Status (1)

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CN (1) CN103779617B (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102534225A (en) * 2012-02-27 2012-07-04 牛辉 Treatment method for anode mud
CN102586804A (en) * 2012-03-27 2012-07-18 广西靖西县一洲锰业有限公司 Method for removing fluorine ion from manganese sulfate solution for producing electrolytic manganese metal

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102534225A (en) * 2012-02-27 2012-07-04 牛辉 Treatment method for anode mud
CN102586804A (en) * 2012-03-27 2012-07-18 广西靖西县一洲锰业有限公司 Method for removing fluorine ion from manganese sulfate solution for producing electrolytic manganese metal

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Inventor after: Liang Dabao

Inventor after: Liang Jing

Inventor after: Liang Jing

Inventor after: Li Liang

Inventor after: Li Senbo

Inventor after: Yin Jipei

Inventor before: Liang Dabao

COR Change of bibliographic data

Free format text: CORRECT: INVENTOR; FROM: LIANG DABAO TO: LIANG DABAO LIANG JING LIANG JING LI LIANG LI SENBO YIN JIPEI

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Granted publication date: 20160817