AT97908B - Process for the extraction of chrome alum. - Google Patents
Process for the extraction of chrome alum.Info
- Publication number
- AT97908B AT97908B AT97908DA AT97908B AT 97908 B AT97908 B AT 97908B AT 97908D A AT97908D A AT 97908DA AT 97908 B AT97908 B AT 97908B
- Authority
- AT
- Austria
- Prior art keywords
- chrome alum
- ferrochrome
- iron
- bath
- extraction
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 5
- OIDPCXKPHYRNKH-UHFFFAOYSA-J chrome alum Chemical compound [K]OS(=O)(=O)O[Cr]1OS(=O)(=O)O1 OIDPCXKPHYRNKH-UHFFFAOYSA-J 0.000 title claims description 4
- 238000000605 extraction Methods 0.000 title description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 14
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 11
- 229910000604 Ferrochrome Inorganic materials 0.000 claims description 7
- 229910052742 iron Inorganic materials 0.000 claims description 7
- GRWVQDDAKZFPFI-UHFFFAOYSA-H chromium(III) sulfate Chemical compound [Cr+3].[Cr+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O GRWVQDDAKZFPFI-UHFFFAOYSA-H 0.000 claims description 6
- 238000005868 electrolysis reaction Methods 0.000 claims description 2
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims description 2
- 229910052939 potassium sulfate Inorganic materials 0.000 claims description 2
- 235000011151 potassium sulphates Nutrition 0.000 claims description 2
- 239000001120 potassium sulphate Substances 0.000 claims 1
- 229940037003 alum Drugs 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- LCPUDZUWZDSKMX-UHFFFAOYSA-K azane;hydrogen sulfate;iron(3+);sulfate;dodecahydrate Chemical compound [NH4+].O.O.O.O.O.O.O.O.O.O.O.O.[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O LCPUDZUWZDSKMX-UHFFFAOYSA-K 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
Landscapes
- Electrolytic Production Of Metals (AREA)
Description
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Verfahren zur Gewinnung von Cllromalaun.
EMI1.1
stande und besteht im Wesentlichen darin, dass Ferrochrom als Anoden im SchwefelsÅaurebad der Elektrolyse unterworfen wird, wodurch das Bad in Chromsulfat übergeht, während sich das Eisen des Ferrochroms an der oder den Kathoden abscheidet, das erhaltene Chromsulfat kann dann in bekannter Weise durch Zusatz von Kaliumsulfat in Chromalaun übergeführt werden.
Man erreicht dadurch, gegenüber den bekannten Verfahren der Erzeugung von Chromalaun aus Ferrochrom, bei welchen Ferrochrom in Schwefelsäure gelöst, aus dem Gemisch von Chromsulfat und
EMI1.2
alaun und Eisenalaun übergefiihrt und schliesslich der letztere entfernt wird, den Vorteil einer wesentlich einfacheren Arbeit und eines reineren Produktes, da das Eisen überhaupt nicht in Lösung geht.
Bei der praktischen Ausführung des Verfahrens werden die Ferrochromstüeke als Anoden in eine gewöhnliche elektrolytische Wanne in der üblichen Weise eingehängt und als Kathoden Hartblei-oder Eisenplatten verwendet, als Anfangsbad dient verdünnte Schwefelsäure ; nimmt man die Konzentration der Schwefelsäure von Haus aus ziemlich hoch, so empfiehlt es sich, anfänglich Hartblei-Kathoden zu verwenden und nach einiger Zeit, wenn das Bad mit Chromsulfat genügend angereichert ist, gegen Eisenkithoden zu vertauschen. Verwendet man dagegen von Anfang an Eisenkathoden, so ist es empfehlenswert, die Säurekonzentration anfänglich niedrig zu halten und allmählich durch Zufluss konzentrierter Schwefelsäure zu steigern.
Soll das Eisen aus dem Bade völlig entfernt werden, so tauscht man gegen Schluss der elektrolytischen Behandlung die Ferrochromanoden gegen unlösliche, z. B. aus Hartblei bestehende aus. Die Temperatur des Bades wird vorteilhafterweise auf etwa 800 C gehalten. Die Spannung und Stromdichte hängen von den Betriebsbedingungen ab und werden zweckentsprechend gewählt.
**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.
<Desc / Clms Page number 1>
Process for the extraction of Cllromalum.
EMI1.1
was and consists essentially in the fact that ferrochrome is subjected to electrolysis as anodes in the sulfuric acid bath, whereby the bath turns into chromium sulfate, while the iron of the ferrochrome is deposited on the cathode (s), the chromium sulfate obtained can then be added in a known manner by adding potassium sulfate be transferred to chrome alum.
This is achieved, compared to the known method of producing chromium alum from ferrochrome, in which ferrochrome dissolved in sulfuric acid, from the mixture of chromium sulfate and
EMI1.2
alum and iron alum are transferred and the latter is finally removed, the advantage of a much simpler work and a purer product, since the iron does not go into solution at all.
In the practical implementation of the method, the ferrochromium pieces are hung as anodes in an ordinary electrolytic tank in the usual way and hard lead or iron plates are used as cathodes, diluted sulfuric acid serves as the initial bath; If the concentration of sulfuric acid is inherently high, it is advisable to use hard lead cathodes initially and, after a while, when the bath is sufficiently enriched with chromium sulphate, to replace it with iron cathodes. If, on the other hand, iron cathodes are used from the start, it is advisable to keep the acid concentration low initially and gradually increase it by adding concentrated sulfuric acid.
If the iron is to be completely removed from the bath, the ferrochromanodes are exchanged for insoluble ones, e.g. B. made of hard lead. The temperature of the bath is advantageously kept at around 800.degree. The voltage and current density depend on the operating conditions and are selected appropriately.
** WARNING ** End of DESC field may overlap beginning of CLMS **.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT97908T | 1922-08-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT97908B true AT97908B (en) | 1924-09-25 |
Family
ID=3617302
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT97908D AT97908B (en) | 1922-08-28 | 1922-08-28 | Process for the extraction of chrome alum. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT97908B (en) |
-
1922
- 1922-08-28 AT AT97908D patent/AT97908B/en active
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