GB239257A - Conversion of lead sulphate into lead carbonate - Google Patents

Conversion of lead sulphate into lead carbonate

Info

Publication number
GB239257A
GB239257A GB1110924A GB1110924A GB239257A GB 239257 A GB239257 A GB 239257A GB 1110924 A GB1110924 A GB 1110924A GB 1110924 A GB1110924 A GB 1110924A GB 239257 A GB239257 A GB 239257A
Authority
GB
United Kingdom
Prior art keywords
sulphate
liquor
lead
ammonia
effected
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
Application number
GB1110924A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to GB1110924A priority Critical patent/GB239257A/en
Publication of GB239257A publication Critical patent/GB239257A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G21/00Compounds of lead
    • C01G21/14Carbonates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

Ammonium sulphate is produced during the conversion of lead sulphate into lead carbonate. The lead sulphate is agitated with excess of ammonia, and carbon dioxide is introduced. The treatment with carbon dioxide may be effected simultaneously with the ammonia treatment, or the carbon dioxide may be wholly or in part dissolved in the ammonia, or the carbon dioxide treatment may be effected after the lead hydroxide has been formed and while it is suspended in its mother-liquor, or after it has been separated from its mother-liquor. The carbonation may be effected first at a comparatively low temperature such as 30 DEG C., and then at a higher temperature, say 40-50 DEG C. or higher, 70 DEG C. being mentioned. The reaction may be effected in counter-current, and the ammonium sulphate liquor may be so strong as to be ready for crystallization. Ammonia may be added during the carbonation to replace that carried away by the gases. When the reaction is finished, the mother-liquor is divided, one part, called the nucleus liquor, being made up by the addition of ammonia, water, and lead sulphate for another operation, while the other part, called the residual liquor, is treated to recover the constituents, for instance by distilling with lime. The process may be combined with processes in which lead is extracted from ores as sulphate or chloride. In the latter case the chloride is converted into sulphate as described in Specification 239,559, [Class 1 (iii), Oxides &c., Metallic].ALSO:Lead sulphate is converted into carbonate by agitation with ammonia solution in excess so as to produce the hydrate and passing carbon dioxide, or gases containing it through the suspension until the conversion is effected. The treatment with carbon dioxide may be effected simultaneously with the ammonia treatment, or the carbon dioxide may be wholly or in part dissolved in the ammonia, or the carbon dioxide treatment may be effected after the lead hydroxide has been formed and while it is suspended in its mother-liquor or after it has been separated from its mother-liquor. The carbonation may be effected first at a comparatively low temperature such as 30 DEG C. and then at a higher temperature, say 40-50 DEG C. or higher, 70 DEG C. being mentioned. The reaction may be effected in counter-current, the lead sulphate being first treated with a liquid in which part of the ammonia has already been converted into ammonium sulphate and then with fresh liquor, and the ammonium sulphate liquor may be so strong as to be ready for crystallization. Ammonia may be added during the carbonation to replace that carried away by the gases. When the reaction is finished and the lead carbonate is separated, the mother-liquor is divided, one part, called the nucleus liquor, being made up by the addition of ammonia, water, and lead sulphate for another operation, while the other part, called the residual liquor is treated to recover the constituents, for instance by distilling with lime. The process may be combined with processes in which lead is extracted from its ores &c. as sulphate or chloride. In the latter case the chloride is converted into sulphate for instance by treatment with zinc sulphate as described in Specification 239,559.
GB1110924A 1924-05-05 1924-05-05 Conversion of lead sulphate into lead carbonate Expired GB239257A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1110924A GB239257A (en) 1924-05-05 1924-05-05 Conversion of lead sulphate into lead carbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1110924A GB239257A (en) 1924-05-05 1924-05-05 Conversion of lead sulphate into lead carbonate

Publications (1)

Publication Number Publication Date
GB239257A true GB239257A (en) 1925-09-07

Family

ID=9980204

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1110924A Expired GB239257A (en) 1924-05-05 1924-05-05 Conversion of lead sulphate into lead carbonate

Country Status (1)

Country Link
GB (1) GB239257A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008087684A1 (en) 2007-01-17 2008-07-24 Millbrook Lead Recycling Technologies Limited Recovery of lead in form of high purity lead carbonates from spent lead batteries incl. electrode paste
CN112779414A (en) * 2020-12-17 2021-05-11 襄阳远锐资源工程技术有限公司 Lead plaster desulfurization process and desulfurization equipment thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008087684A1 (en) 2007-01-17 2008-07-24 Millbrook Lead Recycling Technologies Limited Recovery of lead in form of high purity lead carbonates from spent lead batteries incl. electrode paste
CN112779414A (en) * 2020-12-17 2021-05-11 襄阳远锐资源工程技术有限公司 Lead plaster desulfurization process and desulfurization equipment thereof

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