US900597A - Process for producing an electrolytic deposit of metallic chromium. - Google Patents
Process for producing an electrolytic deposit of metallic chromium. Download PDFInfo
- Publication number
- US900597A US900597A US41113808A US1908411138A US900597A US 900597 A US900597 A US 900597A US 41113808 A US41113808 A US 41113808A US 1908411138 A US1908411138 A US 1908411138A US 900597 A US900597 A US 900597A
- Authority
- US
- United States
- Prior art keywords
- producing
- metallic chromium
- bath
- electrolytic deposit
- chromic acid
- 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 - Lifetime
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Classifications
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- 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
- C25D3/06—Electroplating: Baths therefor from solutions of chromium from solutions of trivalent chromium
Definitions
- FRANZ sALZER or vnnn'snnrr, GERMANY.
- the proportion of weights of CrO and Cr O is 2: 1, but the bath will'work better the more the weights of both compounds get nearer and the proportion will be about constant during the electrolysis. If for example a mixture is employed in which the proportion of (110 and Cr -O is 2 to 1, very much current will be necessary and the deposit .comparativel small. But if the proportion is 4' to 3 or sti l nearer the bath works better.
- the quantity of chromium compounds contained in the solution may amount to 5. to 25 per cent. of metalhe chromium.
- the bath can be prepared for instance by partial reduction of pure chromicacid, by
- the bath works if duly prepared and the it is well known, need a great amount of conductive salts in this bath only a very small amount of an electrolyte is allowed, because a greater addition would produce at the cathode chromous oxid (CrO) or only hydrogen.
- CrO cathode chromous oxid
- the composition of the bath can be maintained nearly unchanged if the anodes are partly separated from the cathodic solution by a diaphragm and partly not separated. As the temperature will gradually rise while the current passes, it is also very important to keep the temperature constant.- This may easily be done by'water cooling.
- What I claim is 1. The process for producing an electrolytic deposit of metallic chromium by employing a bath containing chromic acid and chromoxid.
- Ploy'ing' a-- bath containing -a mixture of chromic acid and chromoxid and. using anodes, which facilitate the oxidation of about the same amount chromoxid to chromic acid,as chromic acid is reduced at the cathode by passing an electric current through the bath.
Description
a ATES inzirn ENT 1 or nron. j
FRANZ sALZER, or vnnn'snnrr, GERMANY.
PROCESS FOR PRODUCING AN ELECTROLYTIC DEPOSIT 01E METALLIC GHROMIU'M.
j'ectof'the Emperor of Austria, residing in Dresden, Germany, at present in Uj pest, near Budapest, Austria-Hungary, have invented certain new and- -useful..1mprovements in Processes for Producing an Electrolytic Deposit of Metallic Chromium, of which the following is a specification.
It has been frequently tried to make a deposit ofmetallic chromium by electrolysis on account of its great passivity and resistance against chemical action and its hardness,
but all experiments made up to date have not succeeded in finding any method of practical use.
Various solutions of chromic salts and compounds have been used for this purpose, which gave a cathodic deposit with great difficulty and very high current density.-
By this invention it is possible to roduce easily a very coherent and firm deposlt of any thickness, much harder than steel, very flexible and of fine color. I use for this purpose a bath composed of a mixture of chromic acid and chromoxid in such proportions that the acid character is greatly diminished, but enough chromic acid must be present to make the bath conductive. Theoretically one could say that it consists mostly of chromic 'chromate (lr.,O (Cr() with more or less oxid of chromium than is due to this formula, but it is better to have an excess of oxid than the formula would demand.
According to the formula the proportion of weights of CrO and Cr O is 2: 1, but the bath will'work better the more the weights of both compounds get nearer and the proportion will be about constant during the electrolysis. If for example a mixture is employed in which the proportion of (110 and Cr -O is 2 to 1, very much current will be necessary and the deposit .comparativel small. But if the proportion is 4' to 3 or sti l nearer the bath works better. The quantity of chromium compounds contained in the solution may amount to 5. to 25 per cent. of metalhe chromium.
The bath can be prepared for instance by partial reduction of pure chromicacid, by
means of an electric current or chemically or by a partial saturation of-CrO with Cr (0H,)
' or by partial'oxidation of chromium salts.
a-little acid will be advantageous.
Specification of Letters Patent.
is reduced by the cathode.
conditions of the beginning being maintained with a cathodic current density of 2 to 5 amperes per sq. decimeter and 3 to 6 volts on any metal, the surface of it being carefully,-
Patented Oct..'6, 1908, Application filed January 16, 1908.. Serial No. $11,138.
The bath works if duly prepared and the it is well known, need a great amount of conductive salts in this bath only a very small amount of an electrolyte is allowed, because a greater addition would produce at the cathode chromous oxid (CrO) or only hydrogen. There are different ways to keep the composition of the bath constant for instance by using insoluble anodes, which facilitate the oxidation of about as much chromoxid to chromic acid,'as chromic acid Electrodes consisting of fused ferro-ferric-oxid (Fe OQ, for instance, have this property. If other insoluble anodes are used as for instance lead or platinum, the composition of the bath can be maintained nearly unchanged if the anodes are partly separated from the cathodic solution by a diaphragm and partly not separated. As the temperature will gradually rise while the current passes, it is also very important to keep the temperature constant.- This may easily be done by'water cooling.
What I claim is 1. The process for producing an electrolytic deposit of metallic chromium by employing a bath containing chromic acid and chromoxid.
2. The process of producing an electrolytic deposit of metallic chromium by employing a bath containing chromic acid and chromoxid, theproportion of chromoxid approximating that of the chromic acid.
3. The process for producing an electrolytic deposit of metallic chromium by employing a bath containing a mixture of a mixture of chromic 'acid and chromoxid, chromic' acid being in excess.
4. The process for producing an electrolytic. deposit of metallic chromium by. em-
lo in a bath containing a mixture of chromic acid and chromoxid and a small amount of an electrolyte. I
5 The process'for. producingan electrolytic deposit of metallic chromium by em.
Ploy'ing' a-- bath containing -a mixture of chromic acid and chromoxid and. using anodes, which facilitate the oxidation of about the same amount chromoxid to chromic acid,as chromic acid is reduced at the cathode by passing an electric current through the bath. I
6. The process for producing an electrolytic deposit of metallic chromium by emas chromic acid is reduced at theeathode by passing an electric current through the bath.
7. The process for'producing an electrolytic deposit of metallic chromium by employing a bath containing a mixture of chromic acid and chromoxid and using anodes partly separated from the cathodic solution by a diaphragm, and partly not separated.
*8. The process for producing an electrolytic deposit of metallic chromium by employing a bath containing a mixture of chromic acid and chromoxid and a small amount of an electrolyte and using anodes partly separated from the cathodic solution y a diaphragm, and partly not separated.
9. The process for producing an electrolytic deposit of metallic chromium by employing a bath containing a mixture of chromic acid and'ehromoxid and by cooling the bath during'the passage of the current.
"10. Theprocess for roducing an electro FRANZ SALZER.
Witnesses SIGMUND BERNAUER, G. GUNDERMAN.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US41113808A US900597A (en) | 1908-01-16 | 1908-01-16 | Process for producing an electrolytic deposit of metallic chromium. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US41113808A US900597A (en) | 1908-01-16 | 1908-01-16 | Process for producing an electrolytic deposit of metallic chromium. |
Publications (1)
Publication Number | Publication Date |
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US900597A true US900597A (en) | 1908-10-06 |
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Application Number | Title | Priority Date | Filing Date |
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US41113808A Expired - Lifetime US900597A (en) | 1908-01-16 | 1908-01-16 | Process for producing an electrolytic deposit of metallic chromium. |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3279958A (en) * | 1962-10-15 | 1966-10-18 | Hooker Chemical Corp | Method of rinsing conversion coatings with chromium complex solutions from chromic acid |
US20070227895A1 (en) * | 2006-03-31 | 2007-10-04 | Bishop Craig V | Crystalline chromium deposit |
US8187448B2 (en) | 2007-10-02 | 2012-05-29 | Atotech Deutschland Gmbh | Crystalline chromium alloy deposit |
-
1908
- 1908-01-16 US US41113808A patent/US900597A/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3279958A (en) * | 1962-10-15 | 1966-10-18 | Hooker Chemical Corp | Method of rinsing conversion coatings with chromium complex solutions from chromic acid |
US20070227895A1 (en) * | 2006-03-31 | 2007-10-04 | Bishop Craig V | Crystalline chromium deposit |
US7887930B2 (en) | 2006-03-31 | 2011-02-15 | Atotech Deutschland Gmbh | Crystalline chromium deposit |
US20110132765A1 (en) * | 2006-03-31 | 2011-06-09 | Bishop Craig V | Crystalline chromium deposit |
US8187448B2 (en) | 2007-10-02 | 2012-05-29 | Atotech Deutschland Gmbh | Crystalline chromium alloy deposit |
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