US1863868A - Chromium stripping bath - Google Patents
Chromium stripping bath Download PDFInfo
- Publication number
- US1863868A US1863868A US344918A US34491829A US1863868A US 1863868 A US1863868 A US 1863868A US 344918 A US344918 A US 344918A US 34491829 A US34491829 A US 34491829A US 1863868 A US1863868 A US 1863868A
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- US
- United States
- Prior art keywords
- chromium
- acid
- stripping
- bath
- stripping bath
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- 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.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F5/00—Electrolytic stripping of metallic layers or coatings
Definitions
- oxalic acid preferably use an aqueous solution of -120 grams per liter of water.
- the temperature range should be from, 77 to. degrees Fahrenheit; voltage, 12 volts in full load, using the article to be stripped as the anode.
- the chromium then me: serial No. 844,918.
- An electrolytic bath for stripping chromium plated articles with the article acting as the anode of the bath, which'bath comprises an aqueous solution of an organic acid capable of reducing chromium from the hexavalent to the trivalent form, and forming a good conductor of electricity, said solution being a constituent of a class consisting of oxalic acid, tartaric acid, and citric acid.
- An electrolytic birth for anodically stripping 'a chromium plated article comprising i I an aqueous solution of a substantial quantity of an organic acid electrolyte that is substantially passive to the base metal of thesaid chromium plated article.
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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 Methods And Accessories (AREA)
Description
Patented June 21. 1932 UNITED STATES PATENT OFFICE 4 JOHN F. MCC'ULLOUGH, OF DETROIT, MICHIGAN, ASSIGNOR 'I'O 'IERN STEDT MANUFAC- TURING COMPANY, OF DETROIT, MICHIGAN, A CORPORATION OF MICHIGAN cnaomuu srairrme BATH- have to be plated over again. It has been customary to use a caustic soda solution bath in doing this stripping, but it has been unlformly found necessary after the stripping to in some way work the nickel surface underneath, as by bufling, in order to prepare it for again receiving a deposit of chromium. In short, the nickel-plated surface is passive, and this I believe is due to the presence on the nickel. surface of an invisible oxide formed by the alkali chromate ion, Cro At any rate, the
surface after such a stripping action is substantially passive, and if it does receive any deposit of chromium this chromium is quite likely to peel oif.
- It is the object of my discovery to provide a stripping bath which will successfully remove the chromium and will not render the under surface passive to a second deposit of chromium. This I accom'plish by using a conducting acid aqueous solution which has the characteristic of reducing the chromic acid formed to a trivalent chromium. This-prevents the forming of the alkali chromate ions ness of the under. surface;
I find that substantially any of the organic acids which is a good electric conductor, and which is formed of hydrogen, carbon, and oxygen, and which is capable of reducing the CrO ,'the-h'exavalent form. of chromium, to a trivalent form, will answer the purpose. I find that oxalic acid, tartaric acid, and citric which I believe to be the cause of the passiveacid are most useful in this connection. For
instance, with oxalic acid I preferably use an aqueous solution of -120 grams per liter of water. The temperature range should be from, 77 to. degrees Fahrenheit; voltage, 12 volts in full load, using the article to be stripped as the anode. The chromium then me: serial No. 844,918.
dissolves in its hexavalent'state as chromic acid, and is then immediately reduced to the trivalent form by the oxalic acid, and thus the nickel plate is not rendered passive by the hexavalent chromium ion. The. reaction is as follows: At the anode Cr+3O:=Gr0 chromic acid; using oxalic acid, H C O we have the reaction:
201'0; (hexavalent)+6H:Cz0|-Cr|(0zO4)3-H3CO;+6H|O.
Using tartaric acid, C H O. the reaction is as follows:
20150:(hflX8V8l0nt)+24Ht0t= 2Cr+++(trivalent)+4HzO0:+400:+2H:0. Using citric acid, H C H O the reaction is as follows:
smegma-20:0, (hexava1ent)='= icr+++(trivalent)+ooo,+omo+e(cm)2co 00am. Qxalic acid is cheaper than citric or tartaric acid, and also a better conductor of electricity.
I might add that'hydrochloric acid has been used in stripping, but thisattacks' the ,base metal, such as die-cast metal, and it is also much slower than oxalic acid. 1 What I claim is: I
1. An electrolytic bath for stripping chromium plated articles by placing the article at the anode, comprising an aqueous solution of an organic electrolytic jacidic reducing agent. M
2. An electrolytic bath for stripping chromium plated articles, with the article acting as the anode of the bath, which'bath comprises an aqueous solution of an organic acid capable of reducing chromium from the hexavalent to the trivalent form, and forming a good conductor of electricity, said solution being a constituent of a class consisting of oxalic acid, tartaric acid, and citric acid.
3. An electrolytic bath for stripping chro-' mium plated articles, with the article as an anode, comprising an aqueous solution of oxalic acid. 1.
4. An electrolytic bath for stripping chr6- mium plated articles, with the article acting as an anode, comprising an aqueous solution of oxalic acid of from 60-120 grams of the acid per'liter of water, and with a tempera; ture range of from 77 degrees Fahrenheit of approximately; 12 volts.
2 1,aos,soa
to 85 degrees Fahrenheit, and with a voltage 5. An electrolytic birth for anodically stripping 'a chromium plated article, comprising i I an aqueous solution of a substantial quantity of an organic acid electrolyte that is substantially passive to the base metal of thesaid chromium plated article.
In testimony whereof I have aflixed my signature.
J OHN F. MGCULLOUGH.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US344918A US1863868A (en) | 1929-03-06 | 1929-03-06 | Chromium stripping bath |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US344918A US1863868A (en) | 1929-03-06 | 1929-03-06 | Chromium stripping bath |
Publications (1)
Publication Number | Publication Date |
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US1863868A true US1863868A (en) | 1932-06-21 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US344918A Expired - Lifetime US1863868A (en) | 1929-03-06 | 1929-03-06 | Chromium stripping bath |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2428141A (en) * | 1940-09-25 | 1947-09-30 | Gen Motors Corp | Process for cleaning, stripping, and polishing metal surfaces |
US2534911A (en) * | 1948-04-03 | 1950-12-19 | Houdaille Hershey Corp | Process of removing hydrogen embrittlement of bright nickel electrodeposits |
US2570174A (en) * | 1947-11-12 | 1951-10-02 | Gen Electric | Metal cleaning and plating process |
US3151049A (en) * | 1958-09-29 | 1964-09-29 | Union Carbide Corp | Electrolytic method of and bath for stripping coatings from bases |
US3304246A (en) * | 1963-12-26 | 1967-02-14 | Mitsubishi Heavy Ind Ltd | Method of electrolytically descaling steel including selective recovery of dissolved scale products |
US3357905A (en) * | 1960-03-28 | 1967-12-12 | Cleveland Twist Drill Co | Electrolyte composition and method of electrolytically removing stock from workpiece |
US4193853A (en) * | 1979-05-15 | 1980-03-18 | The United States Of America As Represented By The United States Department Of Energy | Decontaminating metal surfaces |
US4264418A (en) * | 1978-09-19 | 1981-04-28 | Kilene Corp. | Method for detersifying and oxide coating removal |
JP2006320805A (en) * | 2005-05-18 | 2006-11-30 | Hideo Yoshida | Extraction method of hexavalent chromium |
-
1929
- 1929-03-06 US US344918A patent/US1863868A/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2428141A (en) * | 1940-09-25 | 1947-09-30 | Gen Motors Corp | Process for cleaning, stripping, and polishing metal surfaces |
US2570174A (en) * | 1947-11-12 | 1951-10-02 | Gen Electric | Metal cleaning and plating process |
US2534911A (en) * | 1948-04-03 | 1950-12-19 | Houdaille Hershey Corp | Process of removing hydrogen embrittlement of bright nickel electrodeposits |
US3151049A (en) * | 1958-09-29 | 1964-09-29 | Union Carbide Corp | Electrolytic method of and bath for stripping coatings from bases |
US3357905A (en) * | 1960-03-28 | 1967-12-12 | Cleveland Twist Drill Co | Electrolyte composition and method of electrolytically removing stock from workpiece |
US3304246A (en) * | 1963-12-26 | 1967-02-14 | Mitsubishi Heavy Ind Ltd | Method of electrolytically descaling steel including selective recovery of dissolved scale products |
US4264418A (en) * | 1978-09-19 | 1981-04-28 | Kilene Corp. | Method for detersifying and oxide coating removal |
US4193853A (en) * | 1979-05-15 | 1980-03-18 | The United States Of America As Represented By The United States Department Of Energy | Decontaminating metal surfaces |
JP2006320805A (en) * | 2005-05-18 | 2006-11-30 | Hideo Yoshida | Extraction method of hexavalent chromium |
US20080087553A1 (en) * | 2005-05-18 | 2008-04-17 | Hideo Yoshida | Method of Extracting Hexavalent Chromium |
US8157982B2 (en) * | 2005-05-18 | 2012-04-17 | Hideo Yoshida | Method of extracting hexavalent chromium |
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