US645490A - Humid process of extracting the metals bismuth or antimony from their sulfid ores. - Google Patents

Humid process of extracting the metals bismuth or antimony from their sulfid ores. Download PDF

Info

Publication number
US645490A
US645490A US71612499A US1899716124A US645490A US 645490 A US645490 A US 645490A US 71612499 A US71612499 A US 71612499A US 1899716124 A US1899716124 A US 1899716124A US 645490 A US645490 A US 645490A
Authority
US
United States
Prior art keywords
bismuth
antimony
chlorid
extracting
sulfid ores
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 - Lifetime
Application number
US71612499A
Inventor
John Ranald
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 US71612499A priority Critical patent/US645490A/en
Application granted granted Critical
Publication of US645490A publication Critical patent/US645490A/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C22B43/00Obtaining mercury

Definitions

  • ferrous chlorid is treated with iron, (which may be that obtained in a manner hereinafter described,) when ferrous chlorid alone is left in solution, the bismuth being precipitated chemically pure.
  • the ferrous chlorid is then oxidized to ferric chlorid, which can be done as follows:
  • the ferrous chlorid is subjected to the action of an electric current passing through it in a double cell-that is, two compartments or res"- ervoirs separated by a porous diaphragm-the anode being in the one compartment or reservoir and the cathode being in the other.
  • Ferric chlorid is rapidly formed at the anode and iron is deposited at the cathode.
  • the metal on being melted and "run into molds or the like assumes the crystalline state.
  • the tailings consist of sulfur and the residue of the ore.
  • the sulfur can be separated from the residue by any usual or convenient means-such, for example, as elutriation. If any gold be present, it can To all whom it may concern.-
  • the objects of my invention are to provide a new and improved process bywhich bismuth or antimony can be extracted from its sulfid ores without loss of the metal and whereby sulfur and also any gold present can be saved, less treating agent being required and the process efiecting a saving in time and labor (as against smelting) and enabling low- I will presume, for example, thatit is bismuth that is to be extracted, antimony being I extracted in the same manner.
  • the ore having been crushed is passed through a sieve, preferably one of thirty meshes to the square inch.
  • ferric-chlorid solution FeOl Aqlof moderate density-such, for example, as a density of 1,240 (as against water at 1,000)-and at a temperature at or near boiling-point.
  • ferric-chlorid solution FeOl Aqlof moderate density-such, for example, as a density of 1,240 (as against water at 1,000)-and at a temperature at or near boiling-point.
  • the heating of the solution may be effected in any convenient way-for example, by means of a jet of coal-gas or the like and air issuing into the charge through anozzle within a hood dipping into the charge.
  • the liquor resulting from the treatment of the ore with the solvent liquor is separated from the taillike) and while still at a hightqmture is be extracted from the tailin gs by any usual produced to ferric ohlorid and metallic ir on specification in the presence of two su'bscrib- 1n quantities the same as those originally ing witnesses.
  • j used and repeating the operation with anf other charge of crushed ore using the same JOHN RANALD' 5 ferric ohloridand metalliciron for this charge witnesseses: and so on with each charge of ore. WILLIAM FREDERICK UPTON,

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Description

' grade ores to be successfully treated.
. all the bismuth is extracted from the ore in 5 formed in the presence of ferrous chlorid if 5o ings (which can be done by siphoning or the UNITED STATES PATENT mes.
JOHN RANAZLD, or LONDON, ENGLAND.
HUMlD raocrss or ExTRAcnNc THE METALS BlSMUTH OR ANTlMONY FROM THEIR sumo oars.
SPECIFICATION forming part of Letters Patent No. 645,490, dated March 13, 1900. Application filed May 9. 1899. Serial No. 716,124. (No specimens.)
treated with iron, (which may be that obtained in a manner hereinafter described,) when ferrous chlorid alone is left in solution, the bismuth being precipitated chemically pure. The ferrous chlorid is then oxidized to ferric chlorid, which can be done as follows: The ferrous chlorid is subjected to the action of an electric current passing through it in a double cell-that is, two compartments or res"- ervoirs separated by a porous diaphragm-the anode being in the one compartment or reservoir and the cathode being in the other. Ferric chlorid is rapidly formed at the anode and iron is deposited at the cathode. By the equation 3FeOl :ZFeGl -\Fe it is seen that for every two parts of ferric chlorid produced one part of iron is deposited, or for six parts of ferric chlorid three parts of iron are deposited. In the previous equation six parts of ferric chlorid produced two parts of bismuth trichlorid, and to replace this bismuth by iron in or er that ferrous chlorid may alone result three parts of iron are necessary. The iron deposited on the cathode, as aforesaid, is therefore the amount required to throw down the bismuth from another charge of crushed sulfid ore, and so the process is continuous, the same solvent being used re- .Ipeatedly. The metal on being melted and "run into molds or the like assumes the crystalline state. The tailings consist of sulfur and the residue of the ore. The sulfur can be separated from the residue by any usual or convenient means-such, for example, as elutriation. If any gold be present, it can To all whom it may concern.-
Be it known that 1, JOHN RANALD, a subject of the Queen of Great Britain and Ireland, and a resident of 62 Streatham Hill, London, England, have invented a new and useful Improvement in Humid Processes for the Extraction of the Metals Bismuth or Antimony from their Sulfid Ores, which invention is y set forth in the following specification. The objects of my invention are to provide a new and improved process bywhich bismuth or antimony can be extracted from its sulfid ores without loss of the metal and whereby sulfur and also any gold present can be saved, less treating agent being required and the process efiecting a saving in time and labor (as against smelting) and enabling low- I will presume, for example, thatit is bismuth that is to be extracted, antimony being I extracted in the same manner. The ore having been crushed is passed through a sieve, preferably one of thirty meshes to the square inch. It is then in calculated amount thrown into vats containing the solvent liquor-viz., ferric-chlorid solution (FeOl Aqlof moderate density-such, for example, as a density of 1,240 (as against water at 1,000)-and at a temperature at or near boiling-point. 0 parts of the vat or apparatus which come in contact with the heated ferric-chlorid solution should present a surface of iron to the solution. The heating of the solution may be effected in any convenient way-for example, by means of a jet of coal-gas or the like and air issuing into the charge through anozzle within a hood dipping into the charge.
In accordance with the following equation or suitable means.
As before mentioned, my invent-ion can be applied in a like manner to the recovery of antimony from sulfid ores thereof.
1 claim The process of extracting bismuth or antimony from its sulfid ores consisting in crushing the ore to be treated and bringing a solution of ferric chlorid to or about boiling temperature and introducing the crushed ore into the said solution while at the said temperature, separating the liquor from the tailings and then precipitating from the liquor the bismuth or antimony by means of metallic iron, then converting the ferrous chlorid thus the form of bismuth trichlorid. The liquor then consists of ferrous chlorid and bismuth chlorid. The oxychlorid of bismuth is not ferric chlorid of sufficiently-high specific gravity be used in the first place. The liquor resulting from the treatment of the ore with the solvent liquor is separated from the taillike) and while still at a hightqmture is be extracted from the tailin gs by any usual produced to ferric ohlorid and metallic ir on specification in the presence of two su'bscrib- 1n quantities the same as those originally ing witnesses. j used and repeating the operation with anf other charge of crushed ore using the same JOHN RANALD' 5 ferric ohloridand metalliciron for this charge Witnesses: and so on with each charge of ore. WILLIAM FREDERICK UPTON,
In testimony whereof I have signed thisl J OHN EDWARD NEWTON.
US71612499A 1899-05-09 1899-05-09 Humid process of extracting the metals bismuth or antimony from their sulfid ores. Expired - Lifetime US645490A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US71612499A US645490A (en) 1899-05-09 1899-05-09 Humid process of extracting the metals bismuth or antimony from their sulfid ores.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US71612499A US645490A (en) 1899-05-09 1899-05-09 Humid process of extracting the metals bismuth or antimony from their sulfid ores.

Publications (1)

Publication Number Publication Date
US645490A true US645490A (en) 1900-03-13

Family

ID=2714066

Family Applications (1)

Application Number Title Priority Date Filing Date
US71612499A Expired - Lifetime US645490A (en) 1899-05-09 1899-05-09 Humid process of extracting the metals bismuth or antimony from their sulfid ores.

Country Status (1)

Country Link
US (1) US645490A (en)

Similar Documents

Publication Publication Date Title
US2655472A (en) Process of extracting and recovering metals by leaching and electrolysis
US894383A (en) Treatment of ores by means of the precipitation process.
US645490A (en) Humid process of extracting the metals bismuth or antimony from their sulfid ores.
US1396740A (en) Process of treating complex zinc-lead ores
US607287A (en) Office
US1232080A (en) Process of recovering copper.
US1018734A (en) Process of treating tin-bearing material.
US592055A (en) Process of treating ores
US546873A (en) Croft
US518732A (en) Art of producing metallic zinc
US571369A (en) Process of refining gold and silver bullion
US1748748A (en) Treatment of lead-zinc sulphide ores, mattes, and the like
US1011899A (en) Metallurgy of metal sulfids.
US657030A (en) Process of extracting bismuth from ores containing bismuth oxids, &c.
US1785247A (en) Recovery of metallic elements and alloys
US709038A (en) Process of treating telluride gold ores.
US631040A (en) Process of extracting precious metals from their ores.
US1069498A (en) Process of treating ores.
US1182320A (en) Method of treating flue products.
US714861A (en) Process of electrolytic separation of copper and nickel.
US873648A (en) Making iron from metallic sulfids.
US1173467A (en) Process of treating zinc ores.
US841721A (en) Process of treating ores.
US978211A (en) Art of extracting metals electrolytically.
US839451A (en) Treatment of pyritic ores.