Tin alloy electroplating
Characteristics of tin
Symbol: Sn
Atomic number: 50
Atomic weight: 118.71
Classification: Metal
Crystal structure: Tetragonal
Tin is soft ductile silver white metal.
Characteristic properties of tin and tin alloys:
Atomic number: 50
Atomic weight: 118.71
Classification: Metal
Crystal structure: Tetragonal
Tin is soft ductile silver white metal.
Characteristic properties of tin and tin alloys:
- Excellent cosmetic appearance;
- Excellent solderability;
- Very good ductility (malleability);
- Non-Toxicity;
- Good anti-friction properties (low friction, high galling resistance).
Applications of electroplated tin alloys
- Electronics and semiconductors industry
- Food containers and packages
- Engine bearings
Tin alloys used for electroplating
Most tin base alloys have been developed as non-toxic lead-free alternatives of the traditional tin-lead solder 63Sn-37Pb.
Electroplating process of tin base lead-free alloys requires strict control of the electrolyte composition and other process parameters. Small deviations in the deposited alloy composition may result in large changes in the melting point.
Another disadvantage of most tin base lead-free alloys is their proneness to form tin whiskers - mono-crystal tin filaments growing on the surface of tin base alloy. Whiskers growth is driven by the internal compressive stresses in the deposit caused by either parameters of the electroplating process or external factors (mechanical, thermal, environmental).
Long whiskers formed on a lead extend to other leads and may bridge across them causing catastrophic shorts of the circuit.
The following measures reduce the risk of whiskers formation: low brighteners plating solutions, annealing immediately after plating at 300-340°F (150-170°C) for 3-1 hours, reflow after the plating, nickel barrier preventing diffusion of copper from the substrate to the tin coating.
Bright tin is coated in electroplating solutions containing brighteners - organic additives causing formation of fine Grain structure deposit. Bright tin coating have excellent cosmetic appearance, however they are characterized by high internal stresses and contain increased amount of organics.
Matte tin coatings are made in electrolytes without additions of brighteners. Matte tin has dull appearance but the level of internal stresses in matte tin depositions is much less than in that of bright tin.
Pure tin has been used in food package applications and as cosmetic overlay.
Recently pure tin has been introduced as non-toxic replacement of lead containing solders. Maximum service temperature of pure tin solders is higher due to higher melting temperature of tin (450°F / 232°C).
Matte tin (in contrast to bright tin) is characterized by low whiskers growing therefore it is used in electronics.
Now toxic lead containing alloys have been replaced by lead-free alternatives.
Electroplating process of tin base lead-free alloys requires strict control of the electrolyte composition and other process parameters. Small deviations in the deposited alloy composition may result in large changes in the melting point.
Another disadvantage of most tin base lead-free alloys is their proneness to form tin whiskers - mono-crystal tin filaments growing on the surface of tin base alloy. Whiskers growth is driven by the internal compressive stresses in the deposit caused by either parameters of the electroplating process or external factors (mechanical, thermal, environmental).
Long whiskers formed on a lead extend to other leads and may bridge across them causing catastrophic shorts of the circuit.
The following measures reduce the risk of whiskers formation: low brighteners plating solutions, annealing immediately after plating at 300-340°F (150-170°C) for 3-1 hours, reflow after the plating, nickel barrier preventing diffusion of copper from the substrate to the tin coating.
- Pure tin
Bright tin is coated in electroplating solutions containing brighteners - organic additives causing formation of fine Grain structure deposit. Bright tin coating have excellent cosmetic appearance, however they are characterized by high internal stresses and contain increased amount of organics.
Matte tin coatings are made in electrolytes without additions of brighteners. Matte tin has dull appearance but the level of internal stresses in matte tin depositions is much less than in that of bright tin.
Pure tin has been used in food package applications and as cosmetic overlay.
Recently pure tin has been introduced as non-toxic replacement of lead containing solders. Maximum service temperature of pure tin solders is higher due to higher melting temperature of tin (450°F / 232°C).
Matte tin (in contrast to bright tin) is characterized by low whiskers growing therefore it is used in electronics.
- Tin-lead
Now toxic lead containing alloys have been replaced by lead-free alternatives.
- Lead-tin-copper
- Tin-copper
- Tin-silver
- Tin-silver-copper
- Tin-bismuth
- Tin-zinc
Tin alloy electroplating in fluoborate solutions
Bath ingredients:
Tin fluoborate Sn(BF4)2Lead fluoborate Pb(BF4)2Copper fluoborate Cu(BF4)2Fluoboric acid HBF4Boric acid H3BO3Organic brighteners (additives)
Deionized (DI) water
Operating conditions:
Temperature: 70-100°F (21-38°C)
Agitation: Solution and/or cathode rod, no air agitation
Anodes composition: similar to the coating composition
Anode/Cathode surface areas ratio: ≥1
Filtration: continuous with minimum 2 bath turnovers per hour, no carbon
Cathode current density: 20-70 A/ft² (2.2-7.6 A/dm²)
Bath formulations
Problems and troubleshooting
Tin fluoborate Sn(BF4)2Lead fluoborate Pb(BF4)2Copper fluoborate Cu(BF4)2Fluoboric acid HBF4Boric acid H3BO3Organic brighteners (additives)
Deionized (DI) water
Operating conditions:
Temperature: 70-100°F (21-38°C)
Agitation: Solution and/or cathode rod, no air agitation
Anodes composition: similar to the coating composition
Anode/Cathode surface areas ratio: ≥1
Filtration: continuous with minimum 2 bath turnovers per hour, no carbon
Cathode current density: 20-70 A/ft² (2.2-7.6 A/dm²)
Bath formulations
Tin alloy electroplating in fluoborate solutions | ||||||||||
Tin | Lead | Copper | Fluoboric acid | Boric acid | ||||||
Coating | oz/gal | g/l | oz/gal | g/l | oz/gal | g/l | oz/gal | g/l | oz/gal | g/l |
Pure tin (100Sn) | 5 | 37 | 26 | 200 | 4 | 30 | ||||
---|---|---|---|---|---|---|---|---|---|---|
90Sn-10Pb | 10 | 75 | 1.3 | 10 | 23 | 175 | 4 | 30 | ||
60Sn-40Pb | 7 | 52 | 4 | 30 | 17 | 128 | 4 | 30 | ||
10Sn-87Pb-3Cu | 1.3 | 10 | 9 | 68 | 0.33 | 2.5 | 17 | 128 | 4 | 30 |
Problems and troubleshooting
Problem | Cause | Corrective action |
---|---|---|
Burning at high current densities | 1. Low metals concentration 2. Too high current density | 1. Adjust metals concentrations 2. Adjust current density |
Treeing at high current densities | 1. Low additive concentration 2. Low acid concentration | 1. Ad additive 2. Ad acid |
Roughness | 1. Foreign particles in bath 2. Stannic tin 3. Sulfate/chloride contaminations | 1. Filter 2. Filter 3. Increase rinsing and filter the bath |
Poor throwing power | 1. Low acid concentration 2. Metallic contaminations | 1. Ad acid 2. Dummy bath at 1-2 A/ft² (0.1-0.2 A/dm²) |
Poor solderability | 1. Organic contaminations 2. Metallic contaminations | 1. Carbon treat 2. Dummy bath at 1-2 A/ft² (0.1-0.2 A/dm²) |
Poor adhesion | Poor substrate cleaning | Improve cleaning |
Brittle deposit | 1. Organic contaminations 2. Metallic contaminations | 1. Carbon treat 2. Dummy bath at 1-2 A/ft² (0.1-0.2 A/dm²) |
Dark deposit | 1. Organic contaminations 2. Low additive 3. Low temperature | 1. Carbon treat 2. Ad additive 3. Increase temperature |
Tin alloy electroplating in methane sulfonic solutions
Electroplating in methane sulfonic acid solutions is more controllable process than deposition in fluoborate solutions. It allows to obtain high quality tin base coatings of consistent chemical composition.
Bath ingredients:
Stannous methane sulfonate
Lead methane sulfonate
Copper methane sulfonate
Methane sulfonic acid (MSA)
Organic brighteners (additives)
Deionized (DI) water
Operating conditions:
Temperature: 70-100°F (21-38°C)
Agitation: Solution and/or cathode rod, no air agitation
Anodes composition: similar to the coating composition
Filtration: continuous with minimum 2 bath turnovers per hour, no carbon
Cathode current density: 10-40 A/ft² (1.1-4.3 A/dm²)
Bath formulations
Problems and troubleshooting
Bath ingredients:
Stannous methane sulfonate
Lead methane sulfonate
Copper methane sulfonate
Methane sulfonic acid (MSA)
Organic brighteners (additives)
Deionized (DI) water
Operating conditions:
Temperature: 70-100°F (21-38°C)
Agitation: Solution and/or cathode rod, no air agitation
Anodes composition: similar to the coating composition
Filtration: continuous with minimum 2 bath turnovers per hour, no carbon
Cathode current density: 10-40 A/ft² (1.1-4.3 A/dm²)
Bath formulations
Tin alloy electroplating in Methane sulfonic acid solutions | ||||||||||
Tin | Lead | Copper | MSA | |||||||
Coating | oz/gal | g/l | oz/gal | g/l | oz/gal | g/l | oz/gal | g/l | ||
Pure tin (100Sn) | 6 | 45 | 26 | 200 | ||||||
---|---|---|---|---|---|---|---|---|---|---|
90Sn-10Cu | 6.7 | 50 | 0.67 | 5 | 26 | 200 | ||||
90Sn-10Pb | 3 | 22 | 0.4 | 3 | 26 | 200 | ||||
60Sn-40Pb | 2 | 15 | 1 | 7.5 | 26 | 200 |
Problems and troubleshooting
Problem | Cause | Corrective action |
---|---|---|
Burning at high current densities | 1. Low metals concentration 2. Too high current density | 1. Adjust metals concentrations 2. Adjust current density |
Treeing at high current densities | 1. Low additive concentration 2. Low acid concentration | 1. Ad additive 2. Ad acid |
Roughness | 1. Foreign particles in bath 2. Stannic tin | 1. Filter 2. Filter |
Poor adhesion | Poor substrate cleaning | Improve cleaning |
Tin electroplating in sulfate solutions
Bath ingredients:
Stannous sulfate SnSO4Sulfuric acid H2SO4Organic brighteners (additives)
Deionized (DI) water
Operating conditions:
Temperature: 70-100°F (21-38°C)
Agitation: Solution and/or cathode rod, no air agitation
Anodes composition: pure tin
Filtration: continuous with minimum 2 bath turnovers per hour, no carbon
Cathode current density: 10-40 A/ft² (1.1-4.3 A/dm²)
Bath formulations
Tin 6 oz/gal (45 g/l)
Sulfuric acid 16 oz/gal (120 g/l)
Problems and troubleshooting
Stannous sulfate SnSO4Sulfuric acid H2SO4Organic brighteners (additives)
Deionized (DI) water
Operating conditions:
Temperature: 70-100°F (21-38°C)
Agitation: Solution and/or cathode rod, no air agitation
Anodes composition: pure tin
Filtration: continuous with minimum 2 bath turnovers per hour, no carbon
Cathode current density: 10-40 A/ft² (1.1-4.3 A/dm²)
Bath formulations
Tin 6 oz/gal (45 g/l)
Sulfuric acid 16 oz/gal (120 g/l)
Problems and troubleshooting
Problem | Cause | Corrective action |
---|---|---|
Burning at high current densities | 1. Low metals concentration 2. Too high current density | 1. Adjust metals concentrations 2. Adjust current density |
Treeing at high current densities | 1. Low additive concentration 2. Low acid concentration | 1. Ad additive 2. Ad acid |
Roughness | 1. Foreign solid particles in bath 2. Stannic tin | 1. Filter 2. Filter |
Poor throwing power | 1. Low acid concentration 2. Low tin concentration | 1. Ad acid 2. Add stannous sulfate |
Poor solderability | 1. Organic contaminations 2. Metallic contaminations | 1. Carbon treat 2. Dummy bath at 1-2 A/ft² (0.1-0.2 A/dm²) |
Poor adhesion | Poor substrate cleaning | Improve cleaning |
Brittle deposit | 1. Organic contaminations 2. Metallic contaminations | 1. Carbon treat 2. Dummy bath at 1-2 A/ft² (0.1-0.2 A/dm²) |
Dark deposit | 1. Organic contaminations 2. Low additive 3. Low temperature | 1. Carbon treat 2. Ad additive 3. Increase temperature |
Tin electroplating in stannate solutions
Bath ingredients:
Potassium stannate K2SnO3•3H2O
Free potassium hydroxide KOH
No additives are required
Deionized (DI) water
Operating conditions:
Temperature: 150-180°F (66-82°C)
Agitation: Solution and/or cathode rod
Anodes composition: pure tin, steel, stainless steel
Filtration: continuous with minimum 2 bath turnovers per hour
Cathode current density: 30-100 A/ft² (3.2-11 A/dm²)
Bath formulations
Potassium stannate 13.5 oz/gal (100 g/l)
Free potassium hydroxide 2 oz/gal (15 g/l)
Problems and troubleshooting
Potassium stannate K2SnO3•3H2O
Free potassium hydroxide KOH
No additives are required
Deionized (DI) water
Operating conditions:
Temperature: 150-180°F (66-82°C)
Agitation: Solution and/or cathode rod
Anodes composition: pure tin, steel, stainless steel
Filtration: continuous with minimum 2 bath turnovers per hour
Cathode current density: 30-100 A/ft² (3.2-11 A/dm²)
Bath formulations
Potassium stannate 13.5 oz/gal (100 g/l)
Free potassium hydroxide 2 oz/gal (15 g/l)
Problems and troubleshooting
Problem | Cause | Corrective action |
---|---|---|
Low cathode efficiency | 1. Low tin concentration 2. Low temperature 3. High current density | 1. Ad potassium stannate 2. Increase temperature 3. Adjust current density |
Low anode efficiency | 1. Low free potassium hydroxide 2. Low temperature 3. High current density | 1. Ad potassium hydroxide 2. Increase temperature 3. Adjust current density or increase anode area |
Low conductivity | 1. Low temperature 2. Low free potassium hydroxide 3. Low tin concentration | 1. Increase temperature 2. Ad potassium hydroxide 3. Ad potassium stannate |
Spongy dark deposit | Stannous tin formation | Add hydrogen peroxide |
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