CH171431A - Process for the production of a chrome ore concentrate. - Google Patents

Process for the production of a chrome ore concentrate.

Info

Publication number
CH171431A
CH171431A CH171431DA CH171431A CH 171431 A CH171431 A CH 171431A CH 171431D A CH171431D A CH 171431DA CH 171431 A CH171431 A CH 171431A
Authority
CH
Switzerland
Prior art keywords
production
chrome ore
ore concentrate
ore
ores
Prior art date
Application number
Other languages
German (de)
Inventor
A-G Neptunia
Original Assignee
Neptunia A G
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 Neptunia A G filed Critical Neptunia A G
Publication of CH171431A publication Critical patent/CH171431A/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/002Inorganic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/008Organic compounds containing oxygen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/02Collectors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/04Frothers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2203/00Specified materials treated by the flotation agents; Specified applications
    • B03D2203/02Ores
    • B03D2203/025Precious metal ores
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2203/00Specified materials treated by the flotation agents; Specified applications
    • B03D2203/02Ores
    • B03D2203/04Non-sulfide ores

Landscapes

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

  

  Verfahren zur Herstellung eines Chromerzkonzentrates.    Bekanntlich lassen sich viele oxydische  Erze und auch die meisten Gangartmineralien  bei Auswahl der geeigneten Bedingungen mit  höheren Öl- oder Fettsäuren und deren Salzen  flotieren. Bei vielen oxydischen Erzen ist dem  nach die Gefahr vorhanden, dass gleichzeitig mit  den nutzbaren Erzteilchen auch die wertlose  Gangart an der Flotation mitteilnimmt. Um  diesen Übelstand zu umgehen, ging man da  zu über, die     Sauerstoffatome    der Erzoberfläche  durch Schwefel zu ersetzen, uni dadurch eine  leichtere Schwimmbarkeit der Erze zu errei  chen. Diese Sulfidierung der Erzoberfläche  lässt sich aber nicht bei allen oxydischen Erzen  durchführen, da der Grad der Sulfidierung  von der Affinität, des Metalles zu Schwefel  abhängig ist.

   Als Beispiele nicht     sulfidier-          barer    Erze seien hier genannt: Oxydische  Beimengungen enthaltendes Gold, CuSiO3  Sn02, Pb0, Pb02, Pb02, Pb304, ZnCO3, Zn0,  <B>s</B>  Zn2Si04, Fe203, FeC0s, Fe0.Cr203, ferner  alle Mangan-Wolframerze.  



  Es wurde nun gefunden, dass sich der  oben erwähnte Übelstand des gleichzeitigen    Schwimmens von Erz und Gangart bei     oxydi-          schen    Chromerzen dadurch vermeiden lässt,  dass man dieselben einer Vorbehandlung mit  einer Heteropolysäure, wie zum Beispiel  Phosphormolybdänsäure, unterwirft.  



  Bei der nachfolgenden Aufbereitung las  sen sich dann die bei der Flotation üblichen  Zusätze, wie Öl- und Fettsäuren, sowie die  verschiedenen im Handel befindlichen speziel  len Flotationsmittel verwenden, wobei nur  das Erz obenauf schwimmt, während die  Gangart zu Boden sinkt, so dass eine voll  ständige Trennung erzielt werden kann.  



  Es ist natürlich auch möglich, solche  Heteropolysäuren zu verwenden, die durch  Hinzufügen ihrer     Komponenten    direkt zur  Trübe erhalten wurden. Weiterhin lassen sich  die Heteropolysäuren auch in Form ihrer  Salze verwenden.  



  <I>Beispiel</I>  1 kg Chromeisenstein wird in Anwesen  heit von Wasser der Einwirkung von<B>0,135</B>     gr          Phosphormolybdänsäure    unterworfen, worauf      man als Sammler 0,$-1 gr Na-Palmitat und  als Schäumer 0,02 gr Kiefernöl (Pineol) zu  setzt. Letztere liefern den Schaum, in wel  chem sich- das Erz frei von der Gangart an  sammelt. Es empfiehlt sich als weiteren Zu  satz 0,1 gr Wasserglas beizufügen, worauf  man den Flotationsprozess in bekannter Weise  vorsichgehen lässt.  



  An Stelle der Phosphormolybdänsäure oder  ihrer Salze kann man im vorstehenden Bei  spiel auch Phosphorwolframsäure verwenden.



  Process for the production of a chrome ore concentrate. It is known that many oxidic ores and also most gangue minerals can be floated with higher oleic or fatty acids and their salts if the appropriate conditions are selected. In the case of many oxide ores, there is therefore the risk that the worthless gangue will take part in the flotation at the same time as the usable ore particles. In order to get around this problem, people started to replace the oxygen atoms on the surface of the ore with sulfur in order to make the ore easier to float. However, this sulphidation of the ore surface cannot be carried out with all oxide ores, since the degree of sulphidation depends on the affinity of the metal to sulfur.

   Examples of non-sulphidable ores are: gold containing oxide additions, CuSiO3, Sn02, Pb0, Pb02, Pb02, Pb304, ZnCO3, Zn0, Zn2Si04, Fe203, FeC0s, Fe0.Cr203, and more all manganese-tungsten ores.



  It has now been found that the above-mentioned inconvenience of the simultaneous swimming of ore and gangue in oxidic chrome ores can be avoided by subjecting them to a pretreatment with a heteropoly acid, such as, for example, phosphomolybdic acid.



  In the subsequent processing, the additives customary in flotation, such as oleic and fatty acids, as well as the various special flotation agents available on the market, can then be used, with only the ore floating on top, while the gangue sinks to the bottom, so that one full permanent separation can be achieved.



  It is of course also possible to use such heteropolyacids which have been obtained by adding their components directly to the pulp. Furthermore, the heteropolyacids can also be used in the form of their salts.



  <I> Example </I> 1 kg of chrome iron stone is subjected to the action of <B> 0.135 </B> gram of phosphomolybdic acid in the presence of water, whereupon $ 0.- 1 gram of sodium palmitate is obtained as a collector and 0.15 as a foamer. Add 02 grams of pine oil. The latter provide the foam in which the ore collects, free from the gangue. It is advisable to add 0.1 gram of water glass as a further addition, after which the flotation process can be carried out in the known manner.



  Instead of phosphomolybdic acid or its salts, phosphotungstic acid can also be used in the above example.

 

Claims (1)

PATENANSPRUCH: Verfahren zur Herstellung eines Chrom erzkonzentrates, dadurch gekennzeichnet, dass man oxydisches Chromerz mit einer Heteropoly- säure behandelt und das so erhaltene Produkt einer Flotation unterwirft. UNTERANSPRUCH: Verfahren nach Patentanspruch, dadurch gekennzeichnet, dass man als Heteropolysäure Phosphormolybdänsäure verwendet. Claim to the patent: Process for the production of a chrome ore concentrate, characterized in that oxidic chrome ore is treated with a heteropoly acid and the product thus obtained is subjected to flotation. SUBClaim: Method according to claim, characterized in that the heteropoly acid used is phosphomolybdic acid.
CH171431D 1933-08-19 1933-08-19 Process for the production of a chrome ore concentrate. CH171431A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH171431T 1933-08-19

Publications (1)

Publication Number Publication Date
CH171431A true CH171431A (en) 1934-08-31

Family

ID=4423087

Family Applications (1)

Application Number Title Priority Date Filing Date
CH171431D CH171431A (en) 1933-08-19 1933-08-19 Process for the production of a chrome ore concentrate.

Country Status (1)

Country Link
CH (1) CH171431A (en)

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