Claims
- 1. A process for depositing a smooth, even tin coating on a metallized surface, said process comprising immersing into a tin plating bath comprising
- a soluble stannous salt, a sulfur component which comprises a mixture of alkali metal polysulfides and at least one other sulfur-containing compound, a mineral acid, and a wetting agent, wherein said alkali metal polysulfides are present in sufficient amount to produce said smooth, even coating,
- an article having a metallized surface capable of chemically displacing tin from the tin plating bath, wherein the article is immersed in the bath until tin forms in a continuous coating on said metallized surface.
- 2. The process as defined in claim 1 wherein the stannous salt is selected from the group consisting of stannous salts of halides, sulfate, fluoborate, nitrate and acetate; the wetting agent is selected from the group consisting of organic anionic, non-ionic and cationic surfactants; and said mineral acid is selected from the group consisting of hydrochloric acid, sulfuric acid, nitric acid and phosphoric acid.
- 3. The process as defined in claim 1 wherein said stannous salt is stannous chloride, said sulfur component contains thiourea and alkali metal polysulfides, said mineral acid is hydrochloric acid and said wetting agent is a fluorinated carboxylic acid.
- 4. The process of claim 3 wherein the alkali metal polysulfides are present at a concentration of 0.005 to 0.2 g/l of the bath composition.
- 5. The process as defined in claim 3 wherein the ingredients of said tin plating bath are present in the following concentrations:
- ______________________________________Stannous chloride 21 g/lThiourea (chemically pure) 90 g/lAlkali metal polysulfide 0.1 g/lHydrochloric acid 36 mg/lFluorinated carboxylic acid 0.5 g/lWater Balance______________________________________
- 6. The process as defined in claim 3 wherein said fluorinated carboxylic acid is present in a concentration of from about 0.1 to about 5 g/l.
- 7. The process as defined in claim 1 wherein said bath is operated at a temperature of 50.degree.-80.degree. C.
- 8. The process as defined in claim 1 wherein said sulfur-containing compounds are selected from organic and inorganic sulfur compounds, said organic sulfur compounds selected from the group consisting of
- aliphatic sulfur-nitrogen compounds,
- 5- and 6-membered heterocyclic compounds containing S-N in the ring,
- dithiols,
- thio derivatives of alkyl glycols,
- thioamine acids; and
- said inorganic sulfur compounds selected from the group consisting of alkali metal sulfides, alkali metal thiocyanates, and alkali metal dithionates.
- 9. The process as defined in claim 1 wherein said tin plating bath comprises the components in the following concentrations:
- ______________________________________Soluble stannous salt 15 - 30 g/lSulfur component 15 - 120 g/lMineral acid 25 - 50 ml/lWetting agent 0.1 - 10 g/lWater Balance______________________________________
- 10. The process as defined in claim 8 wherein said sulfur component is present in an amount of 50-120 g/l.
- 11. The process as defined in claim 1 wherein said sulfur component contains thiourea and alkali metal polysulfides and wherein said alkali metal polysulfides are present in the range of 0.005 to 0.2 g/l of the bath composition.
- 12. A process for the manufacture of printed circuit boards having a smooth, even tin coating over areas of clean copper circuitry comprising the steps of:
- (1) immersing said circuit boards into an agitated immersion tin plating bath comprising a stannous salt, a sulfur component which comprises a mixture of alkali metal polysulfides and at least one other sulfur-containing compound, a mineral acid, and a wetting agent, wherein said alkali metal polysulfides are present in sufficient amount to produce said smooth, even coating, until tin forms in a continuous coating on said copper circuitry;
- (2) rinsing said boards; and
- (3) drying said boards.
- 13. The process as defined in claim 12 wherein the plating of tin in said tin plating bath is continued to a thickness of between about 50 and 300 millionths of an inch.
- 14. The process as defined in claim 12 wherein said tin plating bath is operated at a temperature of 50.degree.-80.degree. C.
- 15. The process as defined in claim 12 including a pre-cleaning cycle which is a mild etching process comprising the steps of (1) soaking the circuit boards in an alkaline cleaner, (2) rinsing the boards in water (3) dipping the boards in a 10% sulfuric acid solution and thereafter (4) rinsing the boards again in water.
- 16. The process as defined in claim 12 including a pre-cleaning cycle which is a strong etching process comprising the steps of (1) immersing said circuit boards into an etchant dip wherein said etchant is ammonium persulfate, (2) rinsing with water, (3) dipping into a 10% sulfuric acid solution and (4) rinsing said board in water.
- 17. The process as defined in claim 12 wherein said rinsing step comprises rinsing said circuit boards in warm water at a temperature of about 100.degree. F.-120.degree. F.
- 18. The process as defined in claim 12 wherein said drying step comprises a warm oven bake operated at a temperature between about 200.degree. F.-250.degree. F.
- 19. The process as defined in claim 12 wherein after the drying step said boards are wire brushed.
- 20. The process as defined in claim 12 wherein before said pre-cleaning step a solder mask is applied to the circuit boards and said circuit boards are then cured sufficiently to prevent blistering during the tin plating step.
- 21. The process as defined in claim 12 wherein said sulfur-containing compounds are selected from organic and inorganic sulfur compounds, said organic sulfur compounds selected frpom the group consisting of
- aliphatic sulfur-nitrogen compounds,
- 5- and 6-membered heterocyclic compounds containing S-N in the ring,
- dithiols,
- thio derivatives of alkyl glycols,
- thioamine acids; and
- said inorganic sulfur compounds selected from the group consisting of alkali metal sulfides, alkali metal thiocyanates, and alkali metal dithionates.
- 22. The process as defined in claim 12 wherein said sulfur component contains thiourea and alkali metal polysulfides and wherein said alkali metal polysulfides are present in the range of 0.005 to 0.2 g/l of the bath composition.
- 23. The process as defined in claim 12 wherein in the tin plating bath the stannous salt is selected from the group consisting of stannous salts of halides, sulfate, fluoborate, nitrate, and acetate; the wetting agent is selected from the group consisting of organic anionic, nonionic and cationic surfactants; and said mineral acid is selected from the group consisting of hydrochloric acid, sulfuric acid, nitric acid, and phosphoric acid.
- 24. The process of claim 23 wherein the alkali metal polysulfides are present at a concentration of 0.0005 to 0.2 g/l of the bath composition.
- 25. The process as defined in claim 23 wherein said tin plating bath comprises the components in the following concentrations:
- ______________________________________Soluble stannous salt 15 - 30 g/lSulfur component 15 - 120 g/lMineral acid 25 - 50 ml/lWetting agent 0.1 - 10 g/lWater Balance______________________________________
- and wherein the alkali metal polysulfides of the sulfur component is present at a concentration of 0.005 to 0.2 g/l of the bath composition.
- 26. The process as defined in claim 12 wherein said tin plating bath comprises stannous chloride, thiourea, alkali metal polysulfides, hydrochloric acid and fluorocarboxylic acid wetting agent.
- 27. The process as defined in claim 26 wherein said fluorocarboxylic acid is present in a concentration of from about 0.1 to about 5 g/l.
- 28. The process as defined in claim 26 wherein the ingredients of said tin plating bath are present in the following concentrations:
- ______________________________________Stannous chloride 21 g/lThiourea (chemically pure) 90 g/lAlkali metal polysulfides 0.1 g/lHydrochloric acid 36 mg/lFluorocarboxylic acid 0.5 g/lWater Balance______________________________________
- 29. The process as defined in claim 12 wherein said tin plating bath comprises the components in the following concentrations:
- ______________________________________Soluble stannous salt 15 - 30 g/lSulfur component 15 - 120 g/lMineral acid 25 - 50 ml/lWetting agent 0.1 - 10 g/lWater Balance______________________________________
- 30. The process as defined in claim 29 wherein said sulfur component is present in an amount of 50-120 g/l.
Parent Case Info
This is a division of application Ser. No. 382,056 filed July 24, 1973, now U.S. Pat. No. 3,917,486.
US Referenced Citations (5)
Foreign Referenced Citations (1)
Number |
Date |
Country |
151,552 |
Jan 1962 |
SU |
Divisions (1)
|
Number |
Date |
Country |
Parent |
382056 |
Jul 1973 |
|