DE406665C - Process for the electrolytic deposition of metallic chromium - Google Patents
Process for the electrolytic deposition of metallic chromiumInfo
- Publication number
- DE406665C DE406665C DEL54219D DEL0054219D DE406665C DE 406665 C DE406665 C DE 406665C DE L54219 D DEL54219 D DE L54219D DE L0054219 D DEL0054219 D DE L0054219D DE 406665 C DE406665 C DE 406665C
- Authority
- DE
- Germany
- Prior art keywords
- metallic chromium
- solutions
- electrolytic deposition
- chromic acid
- chromium
- 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
Links
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 title claims description 11
- 229910052804 chromium Inorganic materials 0.000 title claims description 10
- 239000011651 chromium Substances 0.000 title claims description 10
- 238000000034 method Methods 0.000 title claims description 9
- 230000008021 deposition Effects 0.000 title claims description 6
- 239000002253 acid Substances 0.000 claims description 8
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 claims description 4
- 150000007513 acids Chemical class 0.000 claims description 3
- 239000007858 starting material Substances 0.000 claims description 3
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical compound [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 claims description 2
- 239000000155 melt Substances 0.000 claims description 2
- 230000008018 melting Effects 0.000 claims 2
- 238000002844 melting Methods 0.000 claims 2
- 230000002378 acidificating effect Effects 0.000 claims 1
- SOCTUWSJJQCPFX-UHFFFAOYSA-N dichromate(2-) Chemical compound [O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O SOCTUWSJJQCPFX-UHFFFAOYSA-N 0.000 claims 1
- 238000002386 leaching Methods 0.000 claims 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000000151 deposition Methods 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001845 chromium compounds Chemical class 0.000 description 1
- 230000001684 chronic effect Effects 0.000 description 1
- 231100000749 chronicity Toxicity 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000001465 metallisation Methods 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/04—Electroplating: Baths therefor from solutions of chromium
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating And Plating Baths Therefor (AREA)
Description
Verfahren zur elektrolytischen -Abscheidung von metallischem Chrom. Zusatz zum Patent 398054. Im Patent 398054 ist ein V erfahren beschrieben worden, um metallisches Chrom aus Lösungen von zweiwertigen Oxyden des Chroms abzuscheiden, die man bei der Elektrolyse von C hroinsäure oder chronisatirer Salze als Abscheidungsprodukte vor dein Eintritt der Metallabscheidung erhält und die Chromsäure oder Chroniate gar nicht oder nur noch in geringen Mengen enthalten, oder auch indem man L(isungen ihnen gleichwertiger Produkte verwendet. Es ist l:ereits in der Beschreibung des Patentes 398o54- darauf hingewiesen worden, claß nian solche Lösungen auf rein chemischem Wege herstellen kann, t1. a. lndeni nian Chronisäure-oder Kaliumbichroinatkrvstalle bis zum Aufschäumen der Charge schmilzt und sie nachträglich finit Wasser verdünnt bzw. in Wasser auflöst. Das gleiche Verfahren kann inan selbstverständlich auch finit anderen chromsauren Salzen (Chroniaten und Bichroinaten) anwenden. Es hat sich nun gezeigt, daß bei dieseln Verfahren gewisse Bedingungen erfüllt sein müssen. ohne deren Beobachtung inan zu Lösungen gelangt, die dinAbscheidung metallischen C hroms entweder nur hei höheren Stromdichten als praktisch durchführbar oder garnicht gestatten.Process for the electrolytic deposition of metallic chromium. Addition to the patent 398054. In the patent 398054 a process has been described to deposit metallic chromium from solutions of divalent oxides of chromium, which are obtained in the electrolysis of chroic acid or chronisatirer salts as deposition products before the occurrence of the metal deposition and the chromic acid or can ven 398o54- in the description of the patent has been pointed out, Class nian such solutions by purely chemical means prepared: not Chroniate or contain only small amounts of, or even by L (isungen them equivalent products used It is l. 1. A. Indenian chronic acid or potassium bichroinate crystals melt until the charge foams and are subsequently diluted with finite water or dissolved in water. The same process can of course also be used with other finite chromic acid salts (chroniates and bichroinates) has shown that certain conditions are met with these processes have to. without observing them, solutions can be obtained which allow the deposition of metallic chromium either only at higher current densities than practically feasible or not at all.
Erstens darf (las Ausgangsmaterial nicht einen wesentlichen Gehalt an freier Schwefelsäure oder anderen Säuren enthalten. (la durch deren Anwesenheit die niederwertigen Oxyde des Chroms, welche sich ,in der Schmelze bei Oberschreitung der Reduktionstemperatur (für C hromsäurekrystall z. B 170' C) bilden, wieder zu Chromaten oxydiert werden bz«-. deren Bildung überhaupt verhindert wird. So darf z. B. der Gehalt der Chromsäure an freier Schwefelsäure 7 bis 8 Prozent freie H.SO, nicht überschreiten. Ein geringer Prozentsatz von 2 bis 4 Prozent hingegen ist zweckmäßig, da das völlige Fehlen von freier Säure der Abscheidung metallischen Chroms wiederum insofern nicht zuträglich ist, als die Kathode sich dann leicht mit kolloidalen Oxv(len überzieht, die von .ihr absorbiert werden und die Abscheid.ung erschweren. Ein geringer Gehalt an freier Säure hält diese kolloidalen Oxyde hingegen in Lösung l)z@v. bringt sie zur Fällung und wirkt insofern vorteilhaft für die Metallahscheidting. Diesen Zusatz freier Säure kann inan natürlich auch nachträglich am Bade vor: ehnien.First, (read the starting material must not have a substantial content contain free sulfuric acid or other acids. (la by their presence the low-value oxides of chromium, which, when exceeded, in the melt the reduction temperature (for chromic acid crystal e.g. 170 ° C) form again Chromates are oxidized. whose formation is prevented at all. So may z. B. the content of chromic acid in free sulfuric acid 7 to 8 percent free H.SO, do not exceed. On the other hand, a low percentage of 2 to 4 percent is advisable, as the complete absence of free acid turns the deposition of metallic chromium insofar as is not beneficial as the cathode then easily becomes colloidal Oxygen coats, which are absorbed by it and make separation difficult. A low content of free acid, however, keeps these colloidal oxides in solution l) z @ v. causes them to precipitate and is therefore beneficial for Metallahscheidting. This addition of free acid can of course also be added to the bath afterwards.
Ferner ist zu beobachten, daß die Reduktion der Chronisätire bzw. der anderen als Ausgangsprodukte benutzten Chroinsalzc möglichst unter Verineidun` von Rühren und Abschluß von Luft erfolgt, tun zu verhindern, daß die Reduktion durch Zutritt des Luftsauerstoffes gestört wird. Zweckmäßig überläßt nian die Charge, sobald sie geschmolzen ist. sich selbst unter Bedeckung des Kessels mit einem Deckel und wartet, bis dichte rote Dämpfe entweichen und die Masse eine Lava ähnelnde Konsistenz angenommen hat. Dann gießt' man Wasser hinzu und kocht unter Lockerung der Masse nochmals auf.Furthermore, it can be observed that the reduction in chronicity resp. of the other chroin salts used as starting products, if possible under verineidun` done by stirring and closing off air, to prevent the reduction from happening Admission of atmospheric oxygen is disturbed. Appropriately, nian leaves the batch, once it's melted. himself under covering the kettle with a lid and waits until dense red vapors escape and the mass becomes a lava has assumed a similar consistency. Then you pour in water and boil in Loosen the mass again.
Daß auch hier die Abschoidung des metallischen Chroms die Vorstufe der Chromverbindung voraussetzt, geht aus folgender Beobachtung hervor. Wenn man, wie oben erwähnt, die Elektrolyse so einrichtet, daß auf der Kathode Otvdniederschläge statt 'Metall erscheinen, die sich, wenn man mit zu wenig Säuren oder zu geringen Stromstärken arbeitet, bilden, so beobachtet man, wenn man die Kathoden herausnimmt, wie das ausgesprochen braune - Hv droxv d nachträglich Wasserstoff entwickelt- Schwemmt man dieses Hvdroxv d in Wasser auf und säuert an, so merkt man bald @V asserstoffentwicklung. T-s ergibt sich daraus, daß die nach dem Verfahren hergestellte Chromlösung entweder fertiggebildete Chromoverbindungen enthält oder wenigstens so beschaffen ist, daß diese sich bei der Elektrolyse abscheiden. Säuert man ,die Flüssigkeiten schwach an, so daß das Hvdrosvd an der Kathode sich bei der Elektrolvse ti,icht abscheiden kami, und erhöht in g enügender u Weise die Stromstärken, so scheidet seich ohne Schwierigkeit .das metallische Chrom ab.That here too the separation of metallic chromium is the preliminary stage of the chromium compound is evident from the following observation. If, As mentioned above, the electrolysis is set up in such a way that there is precipitation on the cathode instead of 'metal appearing, if one has too few acids or too little Current intensities work, form, so one observes when one takes out the cathodes, like the downright brown - Hv droxv d subsequently developed hydrogen - washes away if you add this Hvdroxv d in water and acidify it, you will soon notice the evolution of hydrogen. T-s results from the fact that the chromium solution prepared by the process is either Completely formed chromo compounds contains or is at least such that these are deposited during electrolysis. If you acidify, the liquids are weak on, so that the Hvdrosvd on the cathode are not deposited in the electrolvse kami, and increases the amperage in a sufficient u way, then it separates without it Difficulty removing the metallic chrome.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEL54219D DE406665C (en) | 1921-10-21 | 1921-10-21 | Process for the electrolytic deposition of metallic chromium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEL54219D DE406665C (en) | 1921-10-21 | 1921-10-21 | Process for the electrolytic deposition of metallic chromium |
Publications (1)
Publication Number | Publication Date |
---|---|
DE406665C true DE406665C (en) | 1925-01-19 |
Family
ID=7275989
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEL54219D Expired DE406665C (en) | 1921-10-21 | 1921-10-21 | Process for the electrolytic deposition of metallic chromium |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE406665C (en) |
-
1921
- 1921-10-21 DE DEL54219D patent/DE406665C/en not_active Expired
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