EP0162954A2 - Process for obtaining a germanium concentrate - Google Patents

Process for obtaining a germanium concentrate Download PDF

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EP0162954A2
EP0162954A2 EP84114333A EP84114333A EP0162954A2 EP 0162954 A2 EP0162954 A2 EP 0162954A2 EP 84114333 A EP84114333 A EP 84114333A EP 84114333 A EP84114333 A EP 84114333A EP 0162954 A2 EP0162954 A2 EP 0162954A2
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Prior art keywords
germanium
concentrate
sulfuric acid
leaching
solution
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French (fr)
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EP0162954B1 (en
EP0162954A3 (en
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Lothar Dipl.-Ing. Leder
Kunibert Dr.-Ing. Hanusch
Hans-Joachim Müller
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Preussag AG
Preussag AG Metall
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Preussag AG
Preussag AG Metall
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/02Roasting processes
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B41/00Obtaining germanium

Definitions

  • the invention relates to a method for obtaining a processable germanium concentrate.
  • Germanium occurs as an accompanying element in concentrations of a few ppm in some deposits of sulfidic ores of the metals lead, copper and zinc.
  • Known Ge minerals are e.g. B. argyrodite, canfieldite, germanite and renierite. When processing the raw ores, the germanium minerals are concentrated in concentrates together with the sulfides of the main metals lead, zinc and copper.
  • the concentration of germanium only reaches such high values in the concentrates in a few particularly rich crude ores that a direct separation of the ge from the concentrates is technically possible and economically justifiable.
  • Germanium is also sulfidically condensed and separated from the exhaust gas in a nonoxidizing atmosphere. Together with the germanium sulfide, arsenic compounds and, depending on the temperature used, PbS are also sublimed. In most lead, zinc and copper concentrates, however, the germanium contents are so low that Ge enrichment and separation from the concentrate are out of the question. Germanium often accumulates in intermediate or Waste products from the processes for extracting the main metals.
  • the fly ash generated in addition to the main components of lead oxide and zinc oxide are other volatilizable metal compounds such as i - for example, those of arsenic, antimony, cadmium and Germaniums_
  • Such flue dusts are next geröstesten zinc ores in hydronteta turgisch-e often Ektro used ytician zinc recovery! .
  • the dust is leached with sulfuric acid, and germanium is precipitated and enriched from the solutions.
  • Germanium goes into the final slags of lead reduction. Germanium, together with lead and zinc, can be evaporated from them by a slag blowing process and, after oxidation and condensation, enriched and separated in a flying dust. The further concentration of germanium then takes place, as already mentioned several times, by leaching with sulfuric acid and germanium separation by z. B. Wood extract precipitation.
  • Ge concentrate production is very often carried out via intermediate products of metal extraction. Their composition and ge content can only be controlled to a limited extent. Many enrichment steps are required to produce a Ge concentrate with 10 to 20% Ge.
  • the object of the present invention is to propose a method which, in a very simple and direct manner, makes it possible to extract germanium from sulfidic concentrates.
  • germanium-containing sulfidic concentrate is mixed with such an amount of soda that the sulfur content is bound as sulfate and then the concentrate is roasted under oxidic conditions, the roasted material is leached with sulfuric acid and germanium is precipitated from the solution.
  • the mixture is roasted with sufficient air supply in the temperature range between 850 K and 1200 K, preferably at 1000 K.
  • the roasted material can be subjected to comminution before the sulfuric acid leaching, and the sulfuric acid leaching is carried out at temperatures between 313 and 370 K and the amount of sulfuric acid is such that an H 2 to 4 concentration in the solution after the leaching at least 5 g / t is included.
  • the process would be such that, for example, a copper concentrate with a certain low content of germanium is mixed with a soda amount sufficient to bind the sulfur of the concentrate as sulfate and this mixture is then roasted under oxidizing conditions , whereby the metal sulfides pass into the oxides.
  • a roasted product is formed which contains not only the sulfur but also the metals of the concentrate. This roasted material is leached with sulfuric acid, and so much sulfuric acid is added that a pH of approx. 1 is reached.
  • Germanium goes into solution. Germanium can be obtained from the solution thus produced by a suitable precipitant, such as. B. the frequently used tannin can be precipitated. Small amounts of copper, arsenic, iron and zinc are also precipitated.
  • the precipitation product is further processed into the actual germanium concentrate in a manner known per se by drying and annealing.
  • sulfidic copper concentrate 100 parts of a sulfidic copper concentrate, approximately the following composition are mixed with a sufficient amount of soda (Na-CO-) and then roasted with air.
  • the example shows that very little Ge was evaporated in this way of working.
  • the roasted product thus produced is then leached in a ratio of solid: water like 1:10 after comminution and so much concentrated sulfuric acid is added that a pH of less than 1 is established at the end of the leaching.
  • the leaching is preferably carried out at elevated temperatures, but can also be carried out at room temperature.
  • the filtrate based on the amount used in the roasted material, contained 94% of the Ge of particular interest. The total yield of the solution was therefore 89% Ge.
  • Ge is precipitated from this solution by adding a tannin solution.
  • the precipitated tannate contained
  • a concentrate was obtained by drying and annealing the tannate, the enthieit ⁇ This material corresponds to commercially available concentrates.
  • Example 2 The same germanium-containing copper concentrate as in Example 1 was mixed with an amount of soda sufficient for binding sulfur and then roasted with air.
  • the roast contained well As in Example 1, very little germanium was volatilized.
  • the roasted product produced became a 1:10 ratio of solid: water after adding 40 ml of concentrated sulfuric acid per 100 g of roasted product.
  • a fat product was produced from the clear solution in a manner known per se by adding a tannin solution contained.
  • This material corresponds to commercially available Ge concentrate qualities that can be further processed using chlorine style tatton.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
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  • Manufacture And Refinement Of Metals (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)

Abstract

1. Process for obtaining an upgradable germanium concentrate from sulphur-containing metal concentrates in which the sulphur-containing concentrate is treated with a quantity of soda such that the sulphur content is fixed as sulfate, and is subsequently roasted under oxidizing conditions, the product of roasting leached with sulfuric acid, and germanium precipitated from the solution.

Description

Die Erfindung betrifft ein Verfahren zur Gewinnung eines weiterverarbeitbaren Germaniumkonzentrats.The invention relates to a method for obtaining a processable germanium concentrate.

Germanium kommt als Begleitelement in Konzentrationen von wenigen ppm in einigen Lagerstätten sulfidischer Erze der Metalle Blei, Kupfer und Zink vor. Bekannte Ge-Mineralien sind z. B. Argyrodit, Canfieldit, Germanit und Renierit. Bei der Aufarbeitung der Roherze werden die Germaniumminerale zusammen mit den Sulfiden der Hauptmetalle Blei, Zink und Kupfer in Konzentraten angereichert.Germanium occurs as an accompanying element in concentrations of a few ppm in some deposits of sulfidic ores of the metals lead, copper and zinc. Known Ge minerals are e.g. B. argyrodite, canfieldite, germanite and renierite. When processing the raw ores, the germanium minerals are concentrated in concentrates together with the sulfides of the main metals lead, zinc and copper.

Die Anreicherung des Germaniums erreicht nur bei einigen wenigen besonders Ge-reichen Roherzen so hohe Werte in den Konzentraten, daß eine direkte Ge-Abtrennung aus den Konzentraten technisch möglich und wirtschaftlich vertretbar ist.The concentration of germanium only reaches such high values in the concentrates in a few particularly rich crude ores that a direct separation of the ge from the concentrates is technically possible and economically justifiable.

So sind Verfahren bekannt, aus sulfidischen Blei- und/oder Kupferkonzentraten mit Ge-Gehalten von 0,2 bis 0, % das Germanium als Sulfid unter neutralen oder schwach reduzierenden Bedingungen bei Atmosphärendruck zu sublimieren.Methods are known for subliming the germanium as sulfide from sulfidic lead and / or copper concentrates with Ge contents of 0.2 to 0% under neutral or weakly reducing conditions at atmospheric pressure.

Aus dem Abgas wird Germanium sulfidisch ebenfalls in nicht oxidierender Atmosphäre kondensiert und abgeschieden. Zusammen mit dem Germaniumsulfid werden Arsenverbindungen und je nach angewandter Temperatur auch PbS mit sublimiert. In den meisten Blei-, Zink- und Kupferkonzentraten sind die Germaniumgehalte jedoch so niedrig, daß eine Ge-Anreicherung und Abtrennung aus dem Konzentrat heraus nicht in Frage kommt. Häufig reichert sich das Germanium in Zwischen- oder Abfallprodukten der Prozesse zur Gewinnung der Hauptmetalle an.Germanium is also sulfidically condensed and separated from the exhaust gas in a nonoxidizing atmosphere. Together with the germanium sulfide, arsenic compounds and, depending on the temperature used, PbS are also sublimed. In most lead, zinc and copper concentrates, however, the germanium contents are so low that Ge enrichment and separation from the concentrate are out of the question. Germanium often accumulates in intermediate or Waste products from the processes for extracting the main metals.

So ist z. B. bekannt, daß beim Verschmelzen Ge-haltiger Kupferkonzentrate im Flammofen sich Germanium in den Flugstäuben auf Gehalte von z_ B. 0,2 bis 0,4 % anreichert. In diesen Flugstäuben sind daneben noch die Elemente Kupfer, Arsen, Eisen, Zink, Blei, Schwefel und andere enthalten. Aus solchen Flugstäuben kann Germanium dann durch schwefelsaures oder salzsaures Laugen herausgelöst werden= Mit in Lösung gehen ein Großteil der Begleitmetalle. Aus den Lösungen kann nach eventuell vorheriger Abtrennung von Kupfer, Arsen und Eisen das Germanium in an sich bekannter Weise durch Zugabe von Holzextrakten, wie z. B. Tannin, gefällt werden.So z. For example, it is known that when Ge-containing copper concentrates are melted in the flame furnace, germanium accumulates in the flue dust to contents of, for example, 0.2 to 0.4%. These flue dusts also contain the elements copper, arsenic, iron, zinc, lead, sulfur and others. Germanium can then be removed from such dusts by sulfuric acid or hydrochloric acid lye = a large part of the accompanying metals also go into solution. After any previous separation of copper, arsenic and iron, the germanium can be removed from the solutions in a manner known per se by adding wood extracts, such as. B. tannin.

Die so erzeugten Ge-Konzentrate mit z. B. 6 bis 20 % Ge-Gehalt steHen:einen üblichen handelsfähigen Rohstoff dar. Aus ihm wird z. B. durch ChtoriddestHtation CeCL abdestilliert und abgetrennt.The Ge concentrates so produced with z. B. 6 to 20% Ge content: a common tradable raw material. B. distilled and separated by ChtoriddestHtation CeCL.

Bei dem heute am stärksten verbreiteten Verfahren der hydrometallurgisch-elektrolytischen Zinkgewinnung bleibt das Germanium, wie man festgestellt hat, zu über 90 % im Laugungsrückstand. In einigen Hütten werden diese Rückstände thermisch aufgearbeitet und bevorzugt Blei und Zink, sofern interessant, auch das Germanium verflüchtigt und in einem Flugstaub angereichert.In the most widespread method of hydrometallurgical-electrolytic zinc production today, more than 90% of the germanium remains in the leaching residue. In some smelters, these residues are thermally processed and lead and zinc, if interesting, also volatilize the germanium and accumulate in a dust.

Die erzeugten Flugstäube enthalten neben den Hauptbestandteilen Bleioxid und Zinkoxid noch andere leicht verflüchtigbare Metallverbindungen, wie i- B. solche des Arsens, Antimons, Cadmiums und Germaniums_ Solche Flugstäube werden häufig neben geröstesten Zinkerzen bei der hydronteta!turgisch-e!ektro!ytischen Zinkgewinnung eingesetzt. Die Ftugstäube werden schwefelsauer gelaugt und aus den Lösungen wird Germanium gefällt und angereichert.The fly ash generated in addition to the main components of lead oxide and zinc oxide are other volatilizable metal compounds such as i - for example, those of arsenic, antimony, cadmium and Germaniums_ Such flue dusts are next geröstesten zinc ores in hydronteta turgisch-e often Ektro used ytischen zinc recovery! . The dust is leached with sulfuric acid, and germanium is precipitated and enriched from the solutions.

Beim Verhütten Ge-haltiger Bleikonzentrate, wie sie z. B. in Tsumeb/Namibia gefunden werden, geht Germanium in die Endschlacken der Bleireduktion. Aus ihnen kann Germanium, zusammen mit Blei und Zink, durch einen Schlackeverblaseprozeß verflüchtigt und nach Oxidation und Kondensation in einem Flugstaub angereichert und abgetrennt werden. Die weitere Aufkonzentrierung des Germaniums erfolgt dann, wie bereits mehrfach erwähnt, durch Laugung mit Schwefelsäure und Germaniumabtrennung durch z. B. Holzextraktfällung.When smelting Ge-containing lead concentrates such as z. B. found in Tsumeb / Namibia, Germanium goes into the final slags of lead reduction. Germanium, together with lead and zinc, can be evaporated from them by a slag blowing process and, after oxidation and condensation, enriched and separated in a flying dust. The further concentration of germanium then takes place, as already mentioned several times, by leaching with sulfuric acid and germanium separation by z. B. Wood extract precipitation.

Wie aus dieser kurzen Beschreibung der angewandten Technik: zu ersehen ist, erfolgt die Ge-Konzentraterzeugung sehr häufig über Zwischenprodukte der Metallgewinnung. Deren Zusammensetzung und Ge-Inhalte sind nur begrenzt steuerbar. Es sind viele Anreicherungsschritte zur Erzeugung eines Ge-Konzentrats mit 10 bis 20 % Ge notwendig.As can be seen from this brief description of the technology used: Ge concentrate production is very often carried out via intermediate products of metal extraction. Their composition and ge content can only be controlled to a limited extent. Many enrichment steps are required to produce a Ge concentrate with 10 to 20% Ge.

Aufgabe der vorliegenden Erfindung ist es nun, demgegenüber ein Verfahren vorzuschlagen, welches in einer sehr einfachen und direkten Weise ermöglicht, Germanium aus sulfidischen Konzentraten zu erschließen.The object of the present invention is to propose a method which, in a very simple and direct manner, makes it possible to extract germanium from sulfidic concentrates.

Gelöst wird diese Aufgabe dadurch, daß das germaniumhaltige sulfidische Konzentrat mit einer solchen Menge Soda versetzt wird, daß der Schwefelinhalt als Sulfat gebunden wird und anschließend das Konzentrat unter oxidischen Bedingungen geröstet, das Röstgut schwefelsauer gelaugt und Germanium aus der Lösung gefällt wird.This object is achieved in that the germanium-containing sulfidic concentrate is mixed with such an amount of soda that the sulfur content is bound as sulfate and then the concentrate is roasted under oxidic conditions, the roasted material is leached with sulfuric acid and germanium is precipitated from the solution.

Die Röstung des Gemisches erfolgt bei ausreichender Luftzufuhr im Temperaturbereich zwischen 850 K und 1200 K, vorzugsweise bei 1000 K.The mixture is roasted with sufficient air supply in the temperature range between 850 K and 1200 K, preferably at 1000 K.

In Verfolg des Erfindungsgedankens kann das Röstgut vor der schwefefsauren Laugung einer Zerkleinerung unterworfen werden, und die schwefelsaure Laugung wird bei Temperaturen zwischen 313 bis 370 K durchgeführt und die Schwefelsäuremenge so bemessen, daß nach der Laugung in der Lösung eine H 2so 4-Konzentration von mindestens 5 g/t enthalten ist.Following the concept of the invention, the roasted material can be subjected to comminution before the sulfuric acid leaching, and the sulfuric acid leaching is carried out at temperatures between 313 and 370 K and the amount of sulfuric acid is such that an H 2 to 4 concentration in the solution after the leaching at least 5 g / t is included.

In Verfolg des Erfindungsgedankens würde sich das Verfahren etwa so darstellen, daß man beispielsweise ein Kupferkonzentrat mit einem bestimmten geringen Gehalt an Germanium mit einer Sodamenge vermischt, die ausreichend ist, um den Schwefel des Konzentrats als Sulfat zu binden und dieses Gemisch anschließend unter oxidierenden Bedingungen röstet, wobei die Metallsulfide in die Oxide übergehen. Es entsteht ein Röstgut, welches neben dem Schwefel auch die Metalle des Konzentrats enthält. Dieses Röstgut wird schwefelsauer gelaugt, und mit so viel Schwefelsäure versetzt, daß ein pH-Wert von ca. 1 erreicht wird. Dabei geht Germanium in Lösung. Aus der so erzeugten Lösung kann Germanium durch ein geeignetes Fällmittel, wie z. B. das häufig angewandte Tannin, ausgefällt werden. Dabei werden auch geringe Mengen von Kupfer, Arsen, Eisen und Zink mit gefällt. Die Weiterverarbeitung des Fällprodukts zum eigentlichen Germaniumkonzentrat erfolgt in an sich bekannter Weise durch Trocknen und Glühen.Following the idea of the invention, the process would be such that, for example, a copper concentrate with a certain low content of germanium is mixed with a soda amount sufficient to bind the sulfur of the concentrate as sulfate and this mixture is then roasted under oxidizing conditions , whereby the metal sulfides pass into the oxides. A roasted product is formed which contains not only the sulfur but also the metals of the concentrate. This roasted material is leached with sulfuric acid, and so much sulfuric acid is added that a pH of approx. 1 is reached. Germanium goes into solution. Germanium can be obtained from the solution thus produced by a suitable precipitant, such as. B. the frequently used tannin can be precipitated. Small amounts of copper, arsenic, iron and zinc are also precipitated. The precipitation product is further processed into the actual germanium concentrate in a manner known per se by drying and annealing.

Das Verfahren wird nun anhand zweier Beispiele ausführlicher beschrieben.The method will now be described in more detail using two examples.

Beispiel 1 Example 1

100 Teile eines sulfidischen Kupferkonzentrats, etwa der folgenden Zusammensetzung

Figure imgb0001
werden mit einer für die Schwefelbindung ausreichenden Menge Soda (Na-CO-) vermischt und danach unter Luftzufuhr geröstet.100 parts of a sulfidic copper concentrate, approximately the following composition
Figure imgb0001
are mixed with a sufficient amount of soda (Na-CO-) and then roasted with air.

Eine Analyse des Röstguts ergab, daß es von den wichtigen Elementen 99, % Cu, 95 % Ge und 100 % Fe vom Einsatz enthielt.Analysis of the roast showed that it contained 99% of the important elements, Cu, 95% Ge and 100% Fe from use.

Das Beispiel zeigt, daß bei dieser Arbeitsweise nur sehr wenig Ge verflüchtigt wurde. Das so erzeugte Röstgut wird nun im Verhältnis Feststoff : Wasser wie 1 : 10 nach einer Zerkleinerung gelaugt und dabei so viel konzentrierte Schwefelsäure zugesetzt, daß sich am Ende der Laugung ein pH-Wert von kleiner als 1 einstellt.The example shows that very little Ge was evaporated in this way of working. The roasted product thus produced is then leached in a ratio of solid: water like 1:10 after comminution and so much concentrated sulfuric acid is added that a pH of less than 1 is established at the end of the leaching.

Die Laugung erfolgt vorzugsweise bei erhöhten Temperaturen, kann aber auch bei Raumtemperatur vorgenommen werden. Nach einer Fest/Flüssig-Trennung enthielt das Filtrat, bezogen auf die Einsatzmenge im Röstgut, an dem hier besonders interessierenden Ge 94 %. Die Gesamtausbringung der Lösung betrug demnach 89 % Ge. Aus dieser Lösung wird Ge durch Zugabe einer Tanninlösung ausgefällt. Das ausgefällte Tannat enthielt

Figure imgb0002
The leaching is preferably carried out at elevated temperatures, but can also be carried out at room temperature. After a solid / liquid separation, the filtrate, based on the amount used in the roasted material, contained 94% of the Ge of particular interest. The total yield of the solution was therefore 89% Ge. Ge is precipitated from this solution by adding a tannin solution. The precipitated tannate contained
Figure imgb0002

Durch Trocknen und Glühen des Tannats wurde ein Konzentrat erhalten, das

Figure imgb0003
enthieit< Dieses Material entspricht handelsüblichen Konzentraten.A concentrate was obtained by drying and annealing the tannate, the
Figure imgb0003
enthieit <This material corresponds to commercially available concentrates.

Beispiel 2Example 2

Dasselbe germaniumhaltige Kupferkonzentrat wie im Beispiel 1 wurde mit einer für die Schwefelbindung ausreichenden Sodamenge vermischt und danach unter Luftzufuhr geröstet.The same germanium-containing copper concentrate as in Example 1 was mixed with an amount of soda sufficient for binding sulfur and then roasted with air.

Das Röst gut enthielt

Figure imgb0004
Wie in Beispiel 1 wurde auch hier nur sehr wenig Germanium verflüchtigt. Das erzeugte Röstgut wurde im Verhältnis Feststoff : Wasser wie 1 : 10 nach Zugabe von 40 ml konzentrierter Schwefelsäure je 100 g Röstgut gelaugt.The roast contained well
Figure imgb0004
As in Example 1, very little germanium was volatilized. The roasted product produced became a 1:10 ratio of solid: water after adding 40 ml of concentrated sulfuric acid per 100 g of roasted product.

Die nach einer Fest-Flüssig-Trennung gewonnene Lösung enthielt, bezogen auf die Einsatzmengen im Röstgut

  • 91 % Ge. Das Gesamtausbringen in der Lösung betrug demnach ca. 89 % Ge.
The solution obtained after a solid-liquid separation contained, based on the amounts used in the roasted material
  • 91% Ge. The total yield in the solution was therefore about 89% Ge.

Das im Vergleich zu Beispiel 1 geringere Kupferausbringen wird auf den vergleichsweise niedrigeren Schwefelsäureeinsatz beim Laugen zurückgeführt.The lower copper yield compared to example 1 is attributed to the comparatively lower use of sulfuric acid in the lye.

Aus der klaren Lösung wurde in an sich bekannter Weise durch Zugabe einer Tanninlösung ein Fätfprodukt erzeugt, das

Figure imgb0005
enthielt.A fat product was produced from the clear solution in a manner known per se by adding a tannin solution
Figure imgb0005
contained.

Nach Verglühen dieses Produkts reichern sich die Metalle an auf

Figure imgb0006
After this product has burned up, the metals accumulate
Figure imgb0006

Dieses Material entspricht handelsüblichen und durch Chlordestiltatton weiter verarbeitbaren Ge-Konzentrat-Qualitäten.This material corresponds to commercially available Ge concentrate qualities that can be further processed using chlorine style tatton.

Claims (4)

1. Verfahren zur Gewinnung eines weiterverarbeitbaren Germaniumkonzentrats aus germaniumhaltigen sulfidischen Metallkonzentraten, wobei das Konzentrat einer Röstung und Laugung unterworfen wird, dadurch gekennzeichnet, daß das germaniumhaltige sulfidische Konzentrat mit einer solchen Menge Soda versetzt wird, daß der Schwefelinhalt als Sulfat gebunden, anschließend das Konzentrat unter oxidischen Bedingungen geröstet, das Röstgut schwefelsauer gelaugt und Germanium aus der Lösung gefällt wird.1. A process for obtaining a further processable germanium concentrate from germanium-containing sulfidic metal concentrates, the concentrate being subjected to roasting and leaching, characterized in that the germanium-containing sulfidic concentrate is mixed with an amount of soda such that the sulfur content is bound as sulfate, then the concentrate is added oxidized conditions, the roasted product is leached with sulfuric acid and germanium is precipitated from the solution. 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß die Röstung des Gemisches bei ausreichender Luftzufuhr im Temperaturbereich zwischen 850 K und 1200 K, vorzugsweise bei 1000 K, durchgeführt wird.2. The method according to claim 1, characterized in that the roasting of the mixture is carried out with sufficient air supply in the temperature range between 850 K and 1200 K, preferably at 1000 K. 3. Verfahren nach den Ansprüchen 1 und 2, dadurch gekennzeichnet, daß das erzeugte Röstgut nach vorheriger Zerkleinerung der schwefelsauren Laugung unterworfen wird.3. Process according to claims 1 and 2, characterized in that the roasted product produced is subjected to the sulfuric acid leaching after prior comminution. 4. Verfahren nach den AnsprÜchen bis 3, dadurch gekennzeichnet, daß die schwefelsaure Laugung bei Temperaturen von 313 bis 370 K durchgeführt und die Schwefe!säuremenge so bemessen wird, daß nach der Laugung In der Lösung eine H-SO .-Konzentration von mindestens 5 gff enthalten ist.4. The method according to claims 3, characterized in that the sulfuric acid leaching is carried out at temperatures of 313 to 370 K and the amount of sulfuric acid is so dimensioned that after the leaching in the solution an H-SO. Concentration of at least 5 gff is included.
EP84114333A 1984-05-23 1984-11-27 Process for obtaining a germanium concentrate Expired - Lifetime EP0162954B1 (en)

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DE3419120 1984-05-23
DE3419120A DE3419120C1 (en) 1984-05-23 1984-05-23 Process for obtaining a germanium concentrate that can be processed

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EP0162954A3 EP0162954A3 (en) 1988-03-16
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WO2006033535A1 (en) * 2004-09-20 2006-03-30 Seung, Keun Ku Method of manufacturing germanium-containing solution from yellow soil
CN101638725A (en) * 2009-08-14 2010-02-03 扬州宁达贵金属有限公司 Method for enriching germanium concentrates from low-germanium coal dust
CN116875826A (en) * 2023-09-07 2023-10-13 昆明理工大学 Method for extracting germanium by zinc oxide smoke depth and short process

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102191391B (en) * 2010-03-02 2013-08-21 南华茂森综合利用有限责任公司 Method for extracting germanium from high-impurity low-grade complex zinc oxide powder

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1082311A (en) * 1952-08-18 1954-12-28 Zh Sekitan Sogo Kenkyujo Germanium recovery process
US2827369A (en) * 1953-12-23 1958-03-18 Metallurg De Hoboken Soc Gen Method of separating germanium from primary materials containing germanium and other, less volatile, elements
DE1067221B (en) * 1959-10-15 Siemens & Halske Aktiengesellschaft, Berlin und München Process for the production of germanium for directional conductors, transistors or the like
GB865306A (en) * 1959-06-25 1961-04-12 Charles Lilley Horn Metal recovery process
DE1163787B (en) * 1960-01-16 1964-02-27 Ledoga Spa Process for the production of germanium from its acidic solutions

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1184088B (en) * 1964-03-10 1964-12-23 Stolberger Zink Ag Process for the extraction of non-ferrous heavy metals

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1067221B (en) * 1959-10-15 Siemens & Halske Aktiengesellschaft, Berlin und München Process for the production of germanium for directional conductors, transistors or the like
FR1082311A (en) * 1952-08-18 1954-12-28 Zh Sekitan Sogo Kenkyujo Germanium recovery process
US2827369A (en) * 1953-12-23 1958-03-18 Metallurg De Hoboken Soc Gen Method of separating germanium from primary materials containing germanium and other, less volatile, elements
GB865306A (en) * 1959-06-25 1961-04-12 Charles Lilley Horn Metal recovery process
DE1163787B (en) * 1960-01-16 1964-02-27 Ledoga Spa Process for the production of germanium from its acidic solutions

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006033535A1 (en) * 2004-09-20 2006-03-30 Seung, Keun Ku Method of manufacturing germanium-containing solution from yellow soil
CN101638725A (en) * 2009-08-14 2010-02-03 扬州宁达贵金属有限公司 Method for enriching germanium concentrates from low-germanium coal dust
CN101638725B (en) * 2009-08-14 2014-05-07 扬州宁达贵金属有限公司 Method for enriching germanium concentrates from low-germanium coal dust
CN116875826A (en) * 2023-09-07 2023-10-13 昆明理工大学 Method for extracting germanium by zinc oxide smoke depth and short process
CN116875826B (en) * 2023-09-07 2023-11-14 昆明理工大学 Method for extracting germanium by zinc oxide smoke depth and short process

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EP0162954B1 (en) 1990-04-11
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ZA849151B (en) 1985-07-31
DE3419120C1 (en) 1985-10-10
EP0162954A3 (en) 1988-03-16

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