Abstract: An aluminium production cell includes an elongated cathode current collector bar in contact with a carbonaceous cathode, the cathode current collector bar of copper or a copper alloy coated on its surface facing the cathode or all around with a thin steel protective layer 0.15 mm to 4 mm thick that forms an effective protection of the current collector bar from diffusion of aluminium or other reaction products produced on the carbonaceous cathode during operation. The volume ratio of the copper or copper alloy to the thin steel protective layer is for example in a range 400%-500%. The protective thin steel layer including an optional pre-applied thinner conductive non-ferrous under or overcoat is preferably in direct contact with the carbonaceous cathode that is ready to use with no need for rodding with cast iron.

Abstract: The invention relates to an electrolytic cell (1) for the production of aluminium (2) including collector bars structure modifications (13,14,15,16) under the cathode (4), namely a copper collector bar held in a U-shaped profile or directly embedded into the cathode. This leads to an optimized current distribution in the liquid aluminium metal (2) and/or inside the carbon cathode allowing for operating the cell at lower voltage. The lower voltage results from either a lower anode to cathode distance (ACD), and/or to lower voltage drop inside the carbon cathode from liquid metal to the end of the collector bar.

Abstract: An electrolytic cell for the production of aluminium including collector bars under the cathode, namely a copper collector bar whose external terminal end is connected by a conductor element providing electrical connection of the collector bar to an external bus. This conductor element comprises a flexible connector strip of the same or a different highly conductive metal as the conductor bar, such as copper.

Abstract: The invention relates to an electrolytic cell (1) for the production of aluminium (2) including collector bars structure modifications (13,14,15,16) under the cathode (4), namely a copper collector bar held in a U-shaped profile or directly embedded into the cathode. This leads to an optimized current distribution in the liquid aluminium metal (2) and/or inside the carbon cathode allowing for operating the cell at lower voltage. The lower voltage results from either a lower anode to cathode distance (ACD), and/or to lower voltage drop inside the carbon cathode from liquid metal to the end of the collector bar.