Abstract: An improved electroplating process and electroplating bath therefor is disclosed which is adapted to electrodeposit a tin-bismuth alloy. The electroplating bath contains tin ions, an alkali metal hydroxide, and bismuth citrate. Bismuth citrate exhibits relatively high solubility in hot alkaline alkali metal stannate electroplating baths when compared to conventional alkali metal bismuthates or other bismuth compounds which in general have poor solubility in hot alkali metal stannate electroplating baths. An improved process is provided for electrodepositing a tin-bismuth alloy on panels as adherent and uniform plates without signs of staining or tin-bismuth nodules. An additional and important feature of this invention is the advantageous blending of the bismuth citrate with the alkalic metal stannate in the dry solid state, if and when desired.

Abstract: In one specie a tin-plating bath contains an alkali metal stannate and generates an alkali metal hydroxide during the electrodeposition of tin. The tin-plating bath is circulated through the anode compartment of an electrodialytic cell that has a cation permselective membrane separating the anode compartment from the cathode compartment. The cathode compartment contains a suitable electrolyte and when a current is impressed across the electrodialytic cell, the alkali metal ions in the plating bath migrate through the permselective membrane into the cathode compartment and the stannate ions remain in the tin-plating bath in the anode compartment. The removal of the alkali metal ions from the tin-plating bath controls the alkali metal hydroxide content of the plating bath. The electrodialytic cell may be positioned in the tin plating bath and where feasible utilize the same power source as the plating bath.

Abstract: In one specie a tin-plating bath contains an alkali metal stannate and generates an alkali metal hydroxide during the electrodeposition of tin. The tin-plating bath is circulated through the anode compartment of an electrodialytic cell that has a cation permselective membrane separating the anode compartment from the cathode compartment. The cathode compartment contains a suitable electrolyte and when a current is impressed across the electrodialytic cell, the alkali metal ions in the plating bath migrate through the permselective membrane into the cathode compartment and the stannate ions remain in the tin-plating bath in the anode compartment. The removal of the alkali metal ions from the tin-plating bath controls the alkali metal hydroxide content of the plating bath. The electrodialytic cell may be positioned in the tin plating bath and where feasible utilize the same power source as the plating bath.

Abstract: Alkali metal stannates are produced in an electrochemical process by dissolving a tin anode in an appropriate alkali metal hydroxide in the anode compartment of an electrodialytic cell. The anode compartment of the electrodialytic cell is separated from a cathode compartment by an anionic or a cationic permselective ion exchange membrane. The tin is dissolved in the anode compartment in the stannous form and after reacting with the alkali metal hydroxide is oxidized to the stannic form to produce the desired alkali metal stannate.