An electrolytic cell assembly for hydrometallurgical refining of metal and related method for lifting thereof. The cell assembly comprises a rectangular base for contacting a floor; four walls extending upward from the rectangular base and defining an electrolysis cavity for receiving electrolyte and electrodes; anchor apertures provided through the base and/or the walls for providing anchor points for lifting the electrolytic cell assembly off of the floor; and plugs and/or protective layer for plugging and/or covering the anchor apertures to seal the electrolysis cavity during hydrometallurgical refining.

An electrolytic cell assembly for hydrometallurgical refining of metal and related method for lifting thereof. The cell assembly comprises a rectangular base for contacting a floor; four walls extending upward from the rectangular base and defining an electrolysis cavity for receiving electrolyte and electrodes; anchor apertures provided through the base and/or the walls for providing anchor points for lifting the electrolytic cell assembly off of the floor; and plugs and/or protective layer for plugging and/or covering the anchor apertures to seal the electrolysis cavity during hydrometallurgical refining.

A hanger bar for an electrowinning cell, wherein hanger bar includes a bar portion and one or more contact portions adapted, in use, to be brought into contact with an electrical conductor. The contact portions are fabricated from an electrically conductive material, and a welded seal is formed between the bar portion and the contact portions in order to minimize corrosion.

A hanger bar for an electrowinning cell, wherein hanger bar includes a bar portion and one or more contact portions adapted, in use, to be brought into contact with an electrical conductor. The contact portions are fabricated from an electrically conductive material, and a welded seal is formed between the bar portion and the contact portions in order to minimize corrosion.

Provided is high purity tin having purity of 5N (99.999% by mass), which can suppress generation of particles. According to the high purity tin, the number of particles each having a particle diameter of 0.5 μm or more is 50,000 or less per a gram.

Provided is high purity tin having purity of 5N (99.999% by mass), which can suppress generation of particles. According to the high purity tin, the number of particles each having a particle diameter of 0.5 μm or more is 50,000 or less per a gram.

The invention relates to a new way of reducing dissolved metals, in particular Cu.sup.+2 to Cu.sup.0, in which the effect of the diffusion-limiting layer is regulated, optimising the variables which determine the mobilisation of the metal ion (Cu+.sup.2) towards the cathode and the thermodynamic stability of the reduction reaction of Cu+.sup.2 to Cu.sup.0 (or metal of interest) on the cathodic surface. The process is carried out by controlling a dimensionless ratio (referred to as t) or the cathodic polarisation, within certain predefined margins, dynamically adjusting concentrations, flows and/or electrical currents to maintain the predefined operating conditions at an optimum level.

The invention relates to a new way of reducing dissolved metals, in particular Cu.sup.+2 to Cu.sup.0, in which the effect of the diffusion-limiting layer is regulated, optimising the variables which determine the mobilisation of the metal ion (Cu+.sup.2) towards the cathode and the thermodynamic stability of the reduction reaction of Cu+.sup.2 to Cu.sup.0 (or metal of interest) on the cathodic surface. The process is carried out by controlling a dimensionless ratio (referred to as t) or the cathodic polarisation, within certain predefined margins, dynamically adjusting concentrations, flows and/or electrical currents to maintain the predefined operating conditions at an optimum level.

The invention relates to producing magnesium and chlorine from a solution of magnesium chloride-containing salts, using an electrolytic cell. A diaphragmless electrolytic cell includes: an electrolysis chamber with alternating anodes and cathodes; and a magnesium separation cell separated from the electrolysis chamber by a partition having upper V-shaped circulation channels and lower circulation channels. Electrolysis is carried out at 6-25 gas saturation of the electrolyte with chlorine bubbles in an interelectrode gap. The flow rate of the electrolyte in the upper circulation channels is 20-60. The ratio of current strength to electrolyte mass is 8-10. The ratio of the width of the electrolysis chamber to the width of the magnesium separation cell is 1.6-2.7. Additional channels are mounted in the partition, between the upper and lower circulation channels, said additional channels having a flow passage area of 0.016-0.048 of the area of the upper V-shaped channels.

The invention relates to producing magnesium and chlorine from a solution of magnesium chloride-containing salts, using an electrolytic cell. A diaphragmless electrolytic cell includes: an electrolysis chamber with alternating anodes and cathodes; and a magnesium separation cell separated from the electrolysis chamber by a partition having upper V-shaped circulation channels and lower circulation channels. Electrolysis is carried out at 6-25 gas saturation of the electrolyte with chlorine bubbles in an interelectrode gap. The flow rate of the electrolyte in the upper circulation channels is 20-60. The ratio of current strength to electrolyte mass is 8-10. The ratio of the width of the electrolysis chamber to the width of the magnesium separation cell is 1.6-2.7. Additional channels are mounted in the partition, between the upper and lower circulation channels, said additional channels having a flow passage area of 0.016-0.048 of the area of the upper V-shaped channels.