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DE957262C - Extraction of vanadium - Google Patents

Extraction of vanadium

Info

Publication number
DE957262C
DE957262C DEF10185A DEF0010185A DE957262C DE 957262 C DE957262 C DE 957262C DE F10185 A DEF10185 A DE F10185A DE F0010185 A DEF0010185 A DE F0010185A DE 957262 C DE957262 C DE 957262C
Authority
DE
Germany
Prior art keywords
vanadium
water
chromate
carbonic acid
treated
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
DEF10185A
Other languages
German (de)
Inventor
Dr Benno Boehm
Dr Albert Glissmann
Dr Paul Henkel
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.)
Bayer AG
Original Assignee
Bayer AG
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 Bayer AG filed Critical Bayer AG
Priority to DEF10185A priority Critical patent/DE957262C/en
Application granted granted Critical
Publication of DE957262C publication Critical patent/DE957262C/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
    • C22B34/00Obtaining refractory metals
    • C22B34/20Obtaining niobium, tantalum or vanadium
    • C22B34/22Obtaining vanadium

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

Gewinnung von Vanadin Bei der Herstellung von Chromat durch alkalischen oxydierenden Schmelzaufschluß von Chromerz erhält man beim Ausziehen mit Wasser Chromatlösungen., die-je nach Herkunft des Chromerzes mehr oder weniger große Mengen Vanadin enthalten. Ein weiterer Anteil Vanadin verbleibt in der durch Wasser nicht aufschließbaren Gangart.Extraction of vanadium In the production of chromate by alkaline Oxidizing fusion of chromium ore is obtained by pulling it out with water Chromate solutions. Which-depending on the origin of the chrome ore, more or less large quantities Contains vanadium. Another portion of vanadium does not remain in the water unlockable gait.

Gegenstand der Erfindung ist ein Verfahren zur Gewinnung von Vanadi-n aus dem Aufschlußgut der Chromatherstellung, das darin besteht, daß das Aufschlußgut mit Wasser, das Kohlensäure und/oder _ Salze der Kohlensäure enthält, vorzugsweise bei Temperaturen über 5o° behandelt wird.The invention relates to a process for the production of vanadi-n from the disintegration material of the chromate production, which consists in that the disintegration material with water containing carbonic acid and / or salts of carbonic acid, preferably is treated at temperatures above 5o °.

Auf diese Weise werden Chromatlösungen erhalten, die einen erheblich höheren Vanadingehalt aufweisen als die üblicherweise durch Behandeln des Aufschlußgutes mit Wasserenthaltenen Chro, matlösungen. Aus den Vanadin enthaltenden Lösungen wird das Vanadin in üblicher Weise gewonnen.In this way, chromate solutions are obtained which have a considerable have a higher vanadium content than that usually obtained by treating the digestion material with chromate solutions containing water. From the solutions containing vanadium becomes the vanadium obtained in the usual way.

Die Kohlensäure kann der wäßrigen AnschJämmung des Aufschlußgutes als zooo/oiges Kohlendioxyd z. B. aus Bomben zugegeben werden; vorteilhaft verwendet man Kohlendioxyd enthaltende Abgase. Natürlich kann man auch Kohlendioxyd enthaltendes Wasser, z. B. Mineralwasser, vertuenden.The carbonic acid can cause the aqueous slurry of the digestion material as zoo / o carbon dioxide z. B. be added from bombs; it is advantageous to use exhaust gases containing carbon dioxide. Of course you can too Water containing carbon dioxide, e.g. B. mineral water.

An Stelle oder neben der Kohlensäure können auch Karbonate zur Erhöhung des Vanadingehaltes der Chromatlösung eingesetzt werden, z. B. Natriumkarbonat oder -bikarbonat. Beispiel i Aufschlußgut, das durch oxydierendes Rösten von Chromensens.tein aus Südafrika mit Soda erhalten ist, wird mit Wasser bei 8o° i Stunde verrührt. Danach wird von der Gangart abfiltriert und im Filtrat der Vanadingehalt zu 0,87 g/1 bestimmt.Instead of or in addition to carbonic acid, carbonates can also be used to increase the vanadium content of the chromate solution, e.g. B. sodium carbonate or bicarbonate. Example i Digestion material obtained by oxidizing roasting chromensite from South Africa with soda is stirred with water at 80 ° for an hour. The gangue is then filtered off and the vanadium content in the filtrate is determined to be 0.87 g / l.

Eine Probe des gleichen Aufschlußgutes wird ebenfalls bei 8o° mit 45 1 Kohlendioxyd je 1 Anschlämmung i Stunde behandelt. Der Vanadingehalt im Filtrat beträgt nach der Behandlung 4499/1. Beispiel 2 ioo Gewichtsteile Endschlamm der Bichromatherstellung, also der Schlamm, der bei der Behandlung der Chromatschmelze mit Wasser und Abfiltrieren der Chromatlösung hinterbleibt, werden mit ioo 1 Wasser bei go° i Stunde verrührt. Im Faltrat befinden sich o,29 g V/1. , Wird eine gleiche Menge Endschlamm unter Zugabe von io g Na,triumbikarbonat je i kg Endschlamm in gleicher Weise behandelt, so befinden sich im Filtrat o,62 g V/1.A sample of the same digestion material is also at 80 ° with 45 1 carbon dioxide per 1 slurry treated per hour. The vanadium content in the filtrate after treatment is 4499/1. Example 2 100 parts by weight of the final sludge Bichromate production, i.e. the sludge that is used in the treatment of the chromate melt with water and filtering off the chromate solution are washed with 100 1 of water stirred at go ° i hour. In the folding council there are 0.29 g V / 1. , Will be the same Amount of final sludge with the addition of 10 g of sodium trium bicarbonate per kg of final sludge in Treated in the same way, the filtrate contains 0.62 g V / 1.

Beispiel 3 Durch eine Satu.rationstrommel fließen stündlich io cbm einer wäßrigen Ansch:lämmung einer Chromatofenschmelze. Die Trommel wird stündlich mit' i5oo cbm Abgas mit einem C02 Gehalt von 811/o beschickt. Im Filtrat befinden sich i,oi g V/1.Example 3 Io cbm flow through a satellite ration drum every hour an aqueous slurry of a chromate furnace melt. The drum runs every hour charged with 1,500 cbm of exhaust gas with a C02 content of 811 / o. Are in the filtrate i, oi g V / 1.

Ohne Zugabe der C 02 haltigen Abgase befinden sich unter denselben Umständen im Filtrat nur 0,32 g V/1.Without the addition of the C 02 -containing exhaust gases there are among the same Under certain circumstances, only 0.32 g V / 1 in the filtrate.

Claims (2)

PATENTANSPRÜCHE: i. Gewinnung von Vanadin aus dem AufschluBgut der Chromathers.tellung, dadurch gekennzeichnet, daß das AufschluBgut mit Wasser, das Kohlensäure und/oder Salze der Kohlensäure enthält, vorzugsweise bei Temperaturen über 5o° behandelt wird. PATENT CLAIMS: i. Obtaining vanadium from the disintegration material of the chromate preparation, characterized in that the disintegration material is treated with water containing carbonic acid and / or salts of carbonic acid, preferably at temperatures above 50 °. 2. Verfahren gemäß Anspruch i, dadurch gekennzeichnet, daß das Aufschlußgut mit Wasser und Kohlendioxyd enthaltenden Abgasen behandelt wird. In Betracht gezogene Druckschriften: Österreichische Patentschrift Nr. 62 163; USA.-Patentschrift Nr. 2 435 304.2. The method according to claim i, characterized in that that the digestion material is treated with waste gases containing water and carbon dioxide will. Publications considered: Austrian patent specification No. 62 163; U.S. Patent No. 2,435,304.
DEF10185A 1952-10-19 1952-10-19 Extraction of vanadium Expired DE957262C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEF10185A DE957262C (en) 1952-10-19 1952-10-19 Extraction of vanadium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEF10185A DE957262C (en) 1952-10-19 1952-10-19 Extraction of vanadium

Publications (1)

Publication Number Publication Date
DE957262C true DE957262C (en) 1957-01-31

Family

ID=7086386

Family Applications (1)

Application Number Title Priority Date Filing Date
DEF10185A Expired DE957262C (en) 1952-10-19 1952-10-19 Extraction of vanadium

Country Status (1)

Country Link
DE (1) DE957262C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19526655C1 (en) * 1995-07-21 1997-01-16 Bayer Ag Process for the recovery of vanadium compounds from solid mixtures of metal oxides and metal sulfates

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT62163B (en) * 1909-11-24 1913-11-10 Auguste Henry Dr Perret Process for the treatment of materials which contain metals which have several stages of oxidation.
US2435304A (en) * 1944-05-11 1948-02-03 Coast Reduction Inc Method for recovering chromium values from ores

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT62163B (en) * 1909-11-24 1913-11-10 Auguste Henry Dr Perret Process for the treatment of materials which contain metals which have several stages of oxidation.
US2435304A (en) * 1944-05-11 1948-02-03 Coast Reduction Inc Method for recovering chromium values from ores

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19526655C1 (en) * 1995-07-21 1997-01-16 Bayer Ag Process for the recovery of vanadium compounds from solid mixtures of metal oxides and metal sulfates

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