US1713514A - Process of electrolytically separating metallic chromium for the production of chromium coatings on other metals - Google Patents

Process of electrolytically separating metallic chromium for the production of chromium coatings on other metals Download PDF

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US1713514A
US1713514A US126928A US12692826A US1713514A US 1713514 A US1713514 A US 1713514A US 126928 A US126928 A US 126928A US 12692826 A US12692826 A US 12692826A US 1713514 A US1713514 A US 1713514A
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chromium
metals
bath
coatings
production
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US126928A
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Appel Rudolf
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/04Electroplating: Baths therefor from solutions of chromium

Definitions

  • the process for electrolytically depositing chromium on other metals for producing a chromium coating on such metals consists in subjecting the objects. to be coated as cathodes to electrolysis in a bath consisting of a chromic acid solution to which an alkali metal iodate such as sodium-iodate has been added, in an amount not exceeding .05 gram per litre of bath liquid.
  • sulphuric acid is also useful in certain cases where chromic acid is used, as there are in commerce certain qualities of chromic acid which are free from sulphuric acid or only contain a small percentage thereof.
  • anode I prefer to use electrodes of rolled lead which is more dense than cast lead certain cases may even'be less.
  • Example 1 To an aqueous solution of chromic acid containing about 5% of C10, sodium iodate NaIO, is added in which in most of the cases shoul be only about 0.5 grams per litre of the bath and in The object to be coated is introduced into the bath as the cathode, and as the anode an electrode of rolled lead is used.
  • Electrolysis is carried on at a temperature of from 35 to 40 C. at a bath voltage of from 3 to 4 volts and a current density of about .06 amperes per square centimetre.
  • the correct acidity of the bath is preferably ascertained by making a preliminary test, and if in such test there is a deposit of brown colored oxides on the cathode, some sulphuric acid should be added to the bath to obtain a good metal deposit.
  • a process for depositing chromium on other metals which comprises subjecting the metallic object to be coated to electrolysis in a chromic acid bath containing not more than 9.5 g'am of sodium iodate per litre of bath 2.
  • a process for depositing chromium on other metals which comprises subjecting the more closelyuantitiesmetallic object to be coated to electrolysis in a chromic acid bath containing 0.5 gram of sodium iodate per litre of bath liquid.
  • a process for depositing chromium on other metals which comprises subjecting the metallic object to be coated to electrolysis in a chromic acid bath containin about 5% of C10, and 0.5 gram of sodium iodate per litre of bath liquid, the electrolysis being carried on at a temperature of from 35 to 40 C. at.
  • a bath volta'ge of about from 3 to 4 volts and at a current density of about .06 amperes per square centimeter.
  • a process of electrolytically separating metallic chromium for the production of chromium coatings on other metals which process consists in subjecting the objects to be coated as cathodes to electrolysis in a chromic acid bath to which an alkali metal 10 iodate has been added in a quantity of 0.5 gram per liter of solution.

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  • 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

Patented May 21, 1929.
UNITED STATES PATENT OFFICE.
RUDOLF APPEL, 0F BERLIN, GERMANY.
PROCESS OF ELECTROLYTICALLY SEPARATING METALLIC GHROMIUM FOR- THE PRO- DUCTION OF CHROMIUM COATINGS ON OTHER METALS.
No Drawing.
In my prior application for U. S. patent Ser. N 0. 112,408 filed May 28th, 1926, I have described a process for the electrolytic separation of metallic chromium for the purpose of coating other metals with metallic chromium. The said process substantially con-' sists in subjecting the objects to be coated with chromium to electrolysis as cathodes in a bath containing chromic acid to which small quantities of certain electrolytes, especially neutral or acidsalts of organic or inorganic acids, have been added. In certain cases the bath is a'cidulated, preferably with sulphuric acid, and it is preferred to use anodes consisting of rolled lead. By this process coatings are obtained which are perfectly non-porous and strongly adherent to the metal to be coated, and the coatings can be obtained according to the conditions in various colours and, if desired, with polished surfaces without any subsequent treatment.
Now, on further investigation I have found that especially favourable results are obtained by using as the addition to the chromic acid bath a salt of a certain acid not mentioned in my prior application, and while it is not desired to make in the prcsent application any claim for the general idea of making to the bath additions of the eneral nature referred to in my prior app ication, it is desired to claim in the present application the special addition hereinafter referred to.
Therefore, according to the present invention the process for electrolytically depositing chromium on other metals for producing a chromium coating on such metals consists in subjecting the objects. to be coated as cathodes to electrolysis in a bath consisting of a chromic acid solution to which an alkali metal iodate such as sodium-iodate has been added, in an amount not exceeding .05 gram per litre of bath liquid.
The addition of sulphuric acid is also useful in certain cases where chromic acid is used, as there are in commerce certain qualities of chromic acid which are free from sulphuric acid or only contain a small percentage thereof.
As the anode I prefer to use electrodes of rolled lead which is more dense than cast lead certain cases may even'be less.
Application filed August 3, 1926, Serial No. 126,928.
and less liable to be attacked by the electro lytic bath and to contaminate the latter.
The advantage of adding sodium iodate instead of the salts referred to in my said,
Example. To an aqueous solution of chromic acid containing about 5% of C10,, sodium iodate NaIO, is added in which in most of the cases shoul be only about 0.5 grams per litre of the bath and in The object to be coated is introduced into the bath as the cathode, and as the anode an electrode of rolled lead is used.
Electrolysis is carried on at a temperature of from 35 to 40 C. at a bath voltage of from 3 to 4 volts and a current density of about .06 amperes per square centimetre. The correct acidity of the bath is preferably ascertained by making a preliminary test, and if in such test there is a deposit of brown colored oxides on the cathode, some sulphuric acid should be added to the bath to obtain a good metal deposit.
Under the conditions indicated a pure metallic bright deposit of chromium is obtained. By varying the temperature, voltage .and current density it is possible to modify the colour of the deposit. For instance, at a temperature of about from 10 to 25 C. a brownish black coating is obtained.
. What I claim is:
1. A process for depositing chromium on other metals which comprises subjecting the metallic object to be coated to electrolysis in a chromic acid bath containing not more than 9.5 g'am of sodium iodate per litre of bath 2. A process for depositing chromium on other metals which comprises subjecting the more closelyuantitiesmetallic object to be coated to electrolysis in a chromic acid bath containing 0.5 gram of sodium iodate per litre of bath liquid.
3. A process for depositing chromium on other metals which comprises subjecting the metallic object to be coated to electrolysis in a chromic acid bath containin about 5% of C10, and 0.5 gram of sodium iodate per litre of bath liquid, the electrolysis being carried on at a temperature of from 35 to 40 C. at.
a bath volta'ge of about from 3 to 4 volts and at a current density of about .06 amperes per square centimeter.
4; A process of electrolytically separating metallic chromium for the production of chromium coatings on other metals, which process consists in subjecting the objects to be coated as cathodes to electrolysis in a chromic acid bath to which an alkali metal 10 iodate has been added in a quantity of 0.5 gram per liter of solution.
In testimony whereof I have affixed my signature.
RUDOLF APPEL.
US126928A 1926-07-21 1926-08-03 Process of electrolytically separating metallic chromium for the production of chromium coatings on other metals Expired - Lifetime US1713514A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2577833A (en) * 1949-07-23 1951-12-11 Westby George Process for electrowinning chromium
US2783194A (en) * 1955-03-04 1957-02-26 Fred I Nobel Iodate-containing plating baths

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2577833A (en) * 1949-07-23 1951-12-11 Westby George Process for electrowinning chromium
US2783194A (en) * 1955-03-04 1957-02-26 Fred I Nobel Iodate-containing plating baths

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