GB2084191A

GB2084191A - Electro-deposition of alloys

Info

Publication number: GB2084191A
Application number: GB8030638A
Authority: GB
Original assignee: Vandervell Products Ltd
Current assignee: Federal Mogul Shoreham Ltd
Priority date: 1980-09-23
Filing date: 1980-09-23
Publication date: 1982-04-07
Also published as: BR8106041A; ATE10862T1; EP0048579B1; CA1172599A; EP0048579A1; DE3167841D1

Abstract

Apparatus and method for the electro-deposition of a ternary alloy on to a cathode comprises an anolyte containing chamber 14 and a catholyte containing chamber 10 in communication with one another only through the medium of a cation exchange membrane 16. The apparatus is used for depositing a ternary bearing alloy, such as lead-antimony-tin or lead-tin-copper on to the bronze substrate of a steel backed bearing member; the bearing member comprising the cathode 12. Use of the method and apparatus prevents undesirable immersion plating of the lead-containing anode 20 by metals from the plating solution which are more noble than lead.

Description

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GB 2 084 1 91A 1

SPECIFICATION

Method and apparatus for the electro-deposition of lead alloys

5 This invention relates to a method and apparatus for the electro-deposition of an alloy coating on 5 to a backing member, such a process being of particular interest to the coating of a load carrying bearing surface on to the backing member of a plain bearing.

Such a bearing may comprise for example a half shell backing member of steel with a bronze sybstrate bonded thereto and on to which is electro-deposited a bearing surface coating of lead-10 indium or lead-antimony-tin. Binary and ternary alloys can be co-deposited electrolytically as is 10 described for example in British Patents 577335 and 628459 and in U.S.A. Patent 2605149. In British Patent 577335 it is stated, and has been verified in tests, that coatings of ternary alfoys such as lead-antimony-tin or lead-tin-copper can replace the more usual lead-tin or lead-indium binary alloy coatings as bearing surfaces.

1 5 However in the electro-deposition of ternary alloys containing antimony or copper, there is a 15 displacement reaction when a soluble metal anode is used. For example in British Patent 628459 it is stated that antimony will immersion plate on to a lead, lead-tin or lead-tin-antimony anode. In Patent 628459 it is stated that this immersion plating is adherent enough so that the anode may be used two or three times and then the antimony my be scrubbed off 20 and reclaimed and, whereas such a procedure may be acceptable for small scale operation, it 20 would not be feasible to operate a continuous production plating process wherein anodes were required to be removed many times during the working operation for scrubbing.

Similarly if a lead-tin-copper electrolyte is utilised, the copper in the plating solution immersion plates out on to metal anodes such as lead or lead-tin and, although such an 25 electrolyte has been in production use for many years, the removal of all the anodes from the 25 bath during idle periods is required, and frequent additions of copper fluoroborate are necessary to replace losses from the electrolyte.

It is the object of the present invention to provide an improved method and apparatus which will prevent the undesirable immersion plating of a soluble metal anode containing lead by 30 metals from the plating solution which are more noble than lead. 30

In accordance with one aspect of the invention there is provided apparatus for the electro-deposition of an alloy on to a cathode comprising a first chamber within which the cathode is located and which contains a catholyte solution; a second chamber within which the anode is located and which contains an anolyte solution, and said first and second chambers communi-35 eating with one another only through the medium of a cation exchange membrane. 35

In accordance with a further aspect of the invention there is provided a method of electro-depositing an alloy on to a metal cathode comprising the steps of immersing the cathode in a first chamber containing a catholyte solution; immersing a metal anode in a second chamber containing an anolyte solution communicating with said catholyte solution only through the 40 medium of a cation exchange membrane and applying a direct current between the anode and 40 cathode.

In use of the apparatus and method according to the invention the anolyte will not contain elements capable of immersion plating on to the anode. Thus if the catholyte comprises a lead-antimony-tin plating solution then the anolyte will not contain any antimony. Similarly if the 45 catholyte comprises a lead-tin-copper plating solution then the anolyte will not contain copper. 45 When the apparatus is in use, metal ions arising from the anode pass through the cation exchange membrane towards the cathode under the influence of the plating potential. Since the anolyte contains no metal capable of immersion plating on to the anode the anode will remain clean. At the end of a plating operation, when the plating potential is disconnected, the 50 antimony or copper or arsenic in the catholyte (depending on what alloy is being co-deposited) 50 is*prevented from entering the anolyte by the physical barrier of the cation exchange membrane.

That is to say, metal ions can pass in one direction only, i.e. towards the cathode, and then only under the influence of the plating potential applied between the anode and cathode. Thus the anolyte solution in the second chamber remains free of ions capable of immersion plating on to 55 the anode. 55

A further advantage of the use of a cation exchange membrane to physically separate the catholyte and anolyte solutions is that the composition of the catholyte may be controlled more readily since metal is not lost therefrom by immersion plating which in turn means that the electro-deposited alloys have more consistent compositions.

60 Other features of the invention will become apparent from the following description given 60

herein solely by way of example and with reference to the accompanying drawing which shows, in diagrammatic form, a plan view of a plating bath in accordance with the invention.

Referring to the drawings there is shown a first chamber 10 within which is locatable a member 12 to be plated and which comprises the cathode; such member may comprise a steel 65 backing member with a bronze substrate bonded thereto and on to which is to be co-deposited a 65

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ternary alloy as a bearing surface. This first chamber 10 is capable of being filled with the catholyte solution.

At the end of the first chamber 10 remote from the cathode 12 there is provided a second chamber 14 wholely contained within the first chamber and communicating therewith only - 5 through the medium of a cation exchange membrane 16. This second chamber 14 is 5

conveniently of box like rectangular configuration having an open top and an open front across which is secured the exchange membrane 1 6 by means of detachable clamping plates and gaskets. To provide support and protection for the exchange membrane 16a sheet 18 of porous polyethylene may be sealingly located by the gaskets on one or both sides of the membrane 16 10 the polyethylene sheeting 18 being provided to prevent physical damage to the exchange 10

membrane 1 6 and also providing support against sag or swelling of the exchange membrane which may occur in use. >

The cation exchange membrane is a proprietary item and may be of the type available from Permutit-Boby of Brentford, Middlesex, England.

15 The anode 20 is locatable within the second chamber 14 and the chamber 14 is capable of 15 being filled with an anolyte solution to at least the same level as that of the catholyte solution in the first chamber 10. It may be preferable for the level of the anolyte solution to be above that of the catholyte solution to provide a slight hydrostatic pressure in favour of the anolyte.

The following examples of use of the apparatus will serve to illustrate the invention:-20 20

Example 1

The apparatus was used for the electro-deposition of a ternary alloy of lead-antimony-tin to give a coating having a basis of lead and containing between 9.5% and 10.5% by weight of antimony and between 5.5% and 6.5% by weight of tin in the deposited alloy. The anode was 25 a lead-tin anode containing 5% to 25% by weight of tin. 25

The cathode comprised a steel backing member on to which was bonded a bronze substrate.

It is preferable to electroplate a base coating of cobalt or nickel on to the bronze substrate thereby to give a better surface for the deposition of the required ternary alloy particularly for the prevention of dispersal to tin into the bronze.

30 The catholyte solution in the first chamber was as follows:- 30

Lead 1 50 grammes/litre added as lead fluoroborate

Antimony 6 grammes/litre added as

35 antimony trifluoride 35

Tin (stannous) 22 grammes/litre added as tin fluoroborate Resorcinol 7.5 grammes/litre

Gelatin 0.75 grammes/litre

40 Free fluoroboric acid 20 grammes/litre 40

The temperature of the catholyte was maintained at 40°C and a cathode current density of 30 amperes per square foot was utilised for approximately 20 minutes to give a deposited alloy thickness of 25 um.

45 The second chamber was filled with an anolyte solution of the following composition 45

Lead 150 grammes/litre added as lead fluoroborate

Tin 22 grammes/litre added as tin

50 fluoroborate . 50

Resorcinol 7.5 grammes/litre

Gelatin 0.75 grammes/litre

Free fluoroboric acid 20 grammes/litre

55 The temperature of the anolyte solution was maintained at 40°C. 55

Example 2

In this example identical constructions of anode and cathode were utilised as in the preceding example but the electrolyte solutions were chosen to give a ternary alloy deposit on the cathode 60 of lead-tin-copper having a basis of lead and containing between 8% and 12% by weight of tin 60 and between 2% and 3% by weight of copper in the deposited alloy.

A catholyte solution of the following composition was used:-

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Resorcinol Gelatin 10 Free fluoroboric acid

5

Tin (Stannous)

Copper

Lead

100 grammes/litre added as lead fluoroborate

10 grammes/litre added as tin fluoroborate

3 grammes/litre added as copper fluoroborate 5 grammes/litre 0.5 grammes/litre 40 grammes /litre

10

5

The temperature of the catholyte solution was maintained at 25°C and cathode current density of 20 amperes per square foot was utilised for approximately 20 minutes to give a deposited ternary alloy of 25 um thickness.

15 The anolyte solution was identical in all respects with the catholyte solution with the exception 15 that no copper fluoroborate was present in the anolyte.

In both examples it was found that the anode remained clean and that the plating elements had been lost from the catholyte to the cathode at a controlled rate.

2. Apparatus as claimed in Claim 1 wherein said second chamber is located within said first chamber.

3. Apparatus as claimed in either one of Claims 1 or 2 wherein the anode is a lead-tin anode.

30 4. Apparatus as claimed in any one of the preceding claims wherein the cathode is a steel 30 backed bearing member.

5. Apparatus for the electro-deposition of a bearing alloy on to the substrate of a steel backed bearing member constructed and arranged substantially as hereinbefore described with reference to and as shown in the accompanying drawings.

35 6. A method of electro-depositing an alloy on to a metal cathode comprising the steps of 35 immersing the cathode in a first chamber containing a catholyte solution; immersing a metal anode in a second chamber containing an anolyte solution communicating with said catholyte solution only through the medium of a cation exchange membrane and applying a direct current between the anode and cathode.

40 7. A method according to Claim 6 wherein the catholyte solution is a lead-antimony-tin 40

solution, the anolyte solution is a lead-tin solution and the anode is a lead-tin anode.

8. A method according to Claim 6 wherein the catholyte solution is a lead-tin-copper solution, the anolyte solution is a lead-tin solution and the anode is a lead-tin anode.

9. A method of electro-depositing a bearing alloy on to the substrate of a steel backed

45 bearing substantially as hereinbefore described. 45

Claims

20 CLAIMS

20

1. Apparatus for the electro-deposition of an alloy on to a cathode comprising a first chamber within which the cathode is located and which contains a catholyte solution; a second chamber within which the anode is located and which contains an anolyte solution, and said first and second chambers communicating with one another only through the medium of a

25 cation exchange membrane.

25

Printed for Her Majesty's Stationery Office by Burgess & Son (Abingdon) Ltd.—1982.

Published at The Patent Office. 25 Southampton Buildings, London. WC2A 1AY. from which copies may be obtained.