US1987749A - Electro-deposition of tin - Google Patents

Electro-deposition of tin Download PDF

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Publication number
US1987749A
US1987749A US654113A US65411333A US1987749A US 1987749 A US1987749 A US 1987749A US 654113 A US654113 A US 654113A US 65411333 A US65411333 A US 65411333A US 1987749 A US1987749 A US 1987749A
Authority
US
United States
Prior art keywords
tin
cresol
sulphuric acid
deposition
electro
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
US654113A
Other languages
English (en)
Inventor
Paul R Pine
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.)
Harshaw Chemical Co
Original Assignee
Harshaw Chemical 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 Harshaw Chemical Co filed Critical Harshaw Chemical Co
Priority to US654113A priority Critical patent/US1987749A/en
Priority to GB15248/33A priority patent/GB404533A/en
Priority to DEH136417D priority patent/DE641107C/de
Application granted granted Critical
Publication of US1987749A publication Critical patent/US1987749A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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
    • C25D3/30Electroplating: Baths therefor from solutions of tin
    • C25D3/32Electroplating: Baths therefor from solutions of tin characterised by the organic bath constituents used

Definitions

  • the invention comprises the features hereinafter fully described, and particularly pointed out in the claims, the following description setting forth in detail certain illustrative embodiments of the invention, these being indicative however, of but a few of the various.
  • the invention contemplates electro-deposition in an acid type of bath, employing the sulphate, and controlled by an agent which I designate a soluble resin or cresolresin.
  • the anode employed may be tin in suitable form, as for instance commercially pure tin, and the cathode may be of any suitable or desired form, depending upon whether a mere coating or a built-up deposit is contemplated.
  • the present process allows deposition not only on iron,.steel, copper, and other metals or their I alloys low in the electromotive series, but is also feasibly operative upon zinc, aluminum, and other metals or their alloys high in the electromotive series.
  • I incorporate a control agent of a soluble resin character, and desirably of synthetic origininvolving conjugation of phenolic radicles by an organic condensing compound.
  • a control agent of a soluble resin character, and desirably of synthetic origininvolving conjugation of phenolic radicles by an organic condensing compound.
  • Such an agent may be made for instance by reaction between refined cresol, from which all o-cresol has been removed, and such compounds as an aldehyde as formaldehyde, or gelatin, aloin, etc., and sulphuric acid. While a highly purified form of gelatin may be employed, practically the less purified forms such as glue may be applied.
  • I may for example, soften a calculated quantity of glue to a rubbery consistency with the smallest quantity of water, and stir into and heat in an excess of refined ,plete.
  • cresol from which the o-cresol has been removed and constituting essentially then a mixture of meta-cresol and para-cresol.
  • the mixture is heated to not above C. until reaction is com- Thereupon, a calculated amount of con-. centrated sulphuric acid is added, and the whole is heated to not over 110 C.
  • a vdesired amount of gelatin is treated with a calculated quantity of concentrated sulphuric acid, at a temperature not over C. and is allowed to stand'until waste matter rises to the top as scum. This is removed.
  • An amount of refined cresol corresponding in quantity to the gelatin is separately treated with an equi-molecular amount of sulphuric acid at a temperature not over C. for a minimum of one-half hour.
  • the two solutions are cooled to about 10 C. and are then mixed carefully such that the heat of reaction does not carry the temperature higher than about 60 C.
  • the reaction product is a water-soluble material containing little inert matter. If however, the temperature of the reaction were allowed to rise to 80-100 C., the product would be of different and unsuitable character by reason of the secondary reaction occurring.
  • tin in relatively great thickness, such as over two thousandths of an inch and more, and the current densities may run as high as 100 amperes per square foot of surface, and the tin is deposited in a dense fine semi-mirror surface such as has not heretofore been possible.
  • a fluoride in small amount, such as sodium fluoride, a harder surface results.
  • a nickel salt such as nickel sulphate, or nickel fluoride
  • the plating bath as preferably used then, may have such a composition as the following, it being understood that the last two ingredients are optionally added for results more desirable for certain usages.
  • the solution may be operated at temperatures of 20 C.- C., and current densities of 10-100 amperes per square foot. It correspondingly incurs a low power cost. And unlike prior practice, the plating of tin upon zinc and other like metals and alloys now becomes practicable.

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)
  • Artificial Filaments (AREA)
US654113A 1933-01-28 1933-01-28 Electro-deposition of tin Expired - Lifetime US1987749A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US654113A US1987749A (en) 1933-01-28 1933-01-28 Electro-deposition of tin
GB15248/33A GB404533A (en) 1933-01-28 1933-05-26 Improvements in or relating to the electro-deposition of tin
DEH136417D DE641107C (de) 1933-01-28 1933-05-30 Verfahren zum galvanischen Niederschlagen von Zinn

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US654113A US1987749A (en) 1933-01-28 1933-01-28 Electro-deposition of tin

Publications (1)

Publication Number Publication Date
US1987749A true US1987749A (en) 1935-01-15

Family

ID=24623478

Family Applications (1)

Application Number Title Priority Date Filing Date
US654113A Expired - Lifetime US1987749A (en) 1933-01-28 1933-01-28 Electro-deposition of tin

Country Status (3)

Country Link
US (1) US1987749A (de)
DE (1) DE641107C (de)
GB (1) GB404533A (de)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2598486A (en) * 1951-01-12 1952-05-27 United States Steel Corp Electrolytic tin plating baths
US2814589A (en) * 1955-08-02 1957-11-26 Bell Telephone Labor Inc Method of plating silicon
US3515653A (en) * 1965-04-10 1970-06-02 Yorkshire Dyeware & Chem Co Lt Preparation of additives for electroplating baths
US4388158A (en) * 1978-11-27 1983-06-14 Toyo Kohan Company, Ltd. Acidic tinplating process and process for producing an iron-tin alloy on the surface of a steel sheet
US5814202A (en) * 1997-10-14 1998-09-29 Usx Corporation Electrolytic tin plating process with reduced sludge production

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE971778C (de) * 1953-05-05 1959-03-26 Max Schloetter Fa Dr Ing Verfahren zur galvanischen Abscheidung von Zinn aus sauren Elektrolyten
CN112941565B (zh) * 2021-02-24 2024-05-14 恩施市致纯电子材料有限公司 一种高纯锡的制备方法

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2598486A (en) * 1951-01-12 1952-05-27 United States Steel Corp Electrolytic tin plating baths
US2814589A (en) * 1955-08-02 1957-11-26 Bell Telephone Labor Inc Method of plating silicon
US3515653A (en) * 1965-04-10 1970-06-02 Yorkshire Dyeware & Chem Co Lt Preparation of additives for electroplating baths
US4388158A (en) * 1978-11-27 1983-06-14 Toyo Kohan Company, Ltd. Acidic tinplating process and process for producing an iron-tin alloy on the surface of a steel sheet
US5814202A (en) * 1997-10-14 1998-09-29 Usx Corporation Electrolytic tin plating process with reduced sludge production

Also Published As

Publication number Publication date
DE641107C (de) 1937-01-20
GB404533A (en) 1934-01-18

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