US1863868A - Chromium stripping bath - Google Patents

Chromium stripping bath Download PDF

Info

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
Authority
US
United States
Prior art keywords
chromium
acid
stripping
bath
stripping bath
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
Application number
US344918A
Inventor
John F Mccullough
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ternstedt Manufacturing Co
Original Assignee
Ternstedt Manufacturing Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ternstedt Manufacturing Co filed Critical Ternstedt Manufacturing Co
Priority to US344918A priority Critical patent/US1863868A/en
Application granted granted Critical
Publication of US1863868A publication Critical patent/US1863868A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F5/00Electrolytic 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.

Landscapes

  • 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.
US344918A 1929-03-06 1929-03-06 Chromium stripping bath Expired - Lifetime US1863868A (en)

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
US1863868A true US1863868A (en) 1932-06-21

Family

ID=23352659

Family Applications (1)

Application Number Title Priority Date Filing Date
US344918A Expired - Lifetime US1863868A (en) 1929-03-06 1929-03-06 Chromium stripping bath

Country Status (1)

Country Link
US (1) US1863868A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
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

Cited By (11)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US1863868A (en) Chromium stripping bath
GB870060A (en) Improvements in or relating to the plating of metallic surfaces
GB385067A (en) An improved method of producing firmly adherent galvanic deposits on aluminium and its alloys
US2676916A (en) Electroplating on aluminum
GB493485A (en) Process for the electrolytic production of metal coatings on objects with a non-conducting surface
GB1122795A (en) Improvements in corrosion-resisting decorative chromium electrolytic deposits
GB1299850A (en) Repair of chromium plated surfaces
US3511759A (en) Method and electrolytes for electro-depositing black chromium
US3207679A (en) Method for electroplating on titanium
CN104164685A (en) Method for plating nickel on steel plate
US3023149A (en) Electrolytic method of producing thin sheets of aluminum oxide
US2463483A (en) Protection of metallic objects by galvanic action
GB600873A (en) Improvements in or relating to the manufacture of thin copper articles
US3002901A (en) Electroplating process and bath
US3397127A (en) Method and bath for electroplating gold
US2794775A (en) Electroplating with tungsten
US2133996A (en) Art of gold plating
CN109537019A (en) A kind of ac electrolytic coloring method of hardening oxidation aluminium alloy
US2568780A (en) Rectifier manufacturing process and products obtained thereby
US2421265A (en) Rapid zinc depositing bath
US2753299A (en) Electroplating with antimony
US2356543A (en) Process for the electrolytic production of opaque layers, similar to enamel, on aluminium and its alloys
US1600076A (en) Electrodeposition of metallic chromium
US2938842A (en) Electrodeposition of fe-cr alloy
GB1333259A (en) Process for the treatment of decarburised steel to make it suitable for enamelling