GB251736A - Process of separating antimony and lead - Google Patents

Process of separating antimony and lead

Info

Publication number
GB251736A
GB251736A GB723825A GB723825A GB251736A GB 251736 A GB251736 A GB 251736A GB 723825 A GB723825 A GB 723825A GB 723825 A GB723825 A GB 723825A GB 251736 A GB251736 A GB 251736A
Authority
GB
United Kingdom
Prior art keywords
antimony
lead
skim
fume
instance
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
GB723825A
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.)
American Smelting and Refining Co
Original Assignee
American Smelting and Refining Co
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 American Smelting and Refining Co filed Critical American Smelting and Refining Co
Priority to GB723825A priority Critical patent/GB251736A/en
Publication of GB251736A publication Critical patent/GB251736A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B13/00Obtaining lead
    • C22B13/06Refining

Abstract

251,736. Marks, E. C. R., (American Smelting & Refining Co.). March 17, 1925. Dry processes of refining lead.-Crude lead containing antimony in substantial quantities, is refined by maintaining it in fusion in an oxidizing atmosphere, for instance in a reverberatory furnace, at 1200-1700‹ F. At first a skim of tin oxide forms and is removed; then a fume of antimony oxide is liberated and a skim of antimony and lead oxides forms and is removed as long as the fume is produced. By the time the fume is no longer escaping the antimony has been reduced to about 5-7 per cent and the further removal of antimony is effected in the usual manner by skimming until the desired minimum content of antimony is attained. The temperature of the bath is then reduced for instance to 950-1000‹ F. when copper is separated as a skim.
GB723825A 1925-03-17 1925-03-17 Process of separating antimony and lead Expired GB251736A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB723825A GB251736A (en) 1925-03-17 1925-03-17 Process of separating antimony and lead

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB723825A GB251736A (en) 1925-03-17 1925-03-17 Process of separating antimony and lead

Publications (1)

Publication Number Publication Date
GB251736A true GB251736A (en) 1926-05-13

Family

ID=9829283

Family Applications (1)

Application Number Title Priority Date Filing Date
GB723825A Expired GB251736A (en) 1925-03-17 1925-03-17 Process of separating antimony and lead

Country Status (1)

Country Link
GB (1) GB251736A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107312935A (en) * 2017-06-30 2017-11-03 郴州市金贵银业股份有限公司 A kind of processing method of reducing slag after lead anode slurry melting

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107312935A (en) * 2017-06-30 2017-11-03 郴州市金贵银业股份有限公司 A kind of processing method of reducing slag after lead anode slurry melting

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