Patent GB-760102-A (GB)
Title: Methods and apparatus for electrolytic decomposition
IPC: C25B1/36
Filed: 1952-05-22
Abstract: 760,102. Electrolytic cells. HOOKER ELECTROCHEMICAL CO. May 22, 1952 [June 6, 1951], No. 13027/52. Class 41. An electrolytic cell for the decomposition of alkali metal chloride in an electrolyte, having a vertical descending flow of mercury to provide cathode services, comprises an anode assembly providing a plurality of elongated vertical anode surfaces positioned opposite each other with an intervening space between them and with a plurality of pairs of vertical anodically active strips with the strips of each pair facing each other across the space so that there is a sheet of electrolyte passing upward between the pairs of the surface strips, and a plurality of vertically flowing tubes of mercury in the space between the vertical anode surfaces and positioned within the sheet of electrolyte and spaced from the opposite anode surfaces to form the sheet as tubular columns of electrolyte around said cathode tubes having between them the remaining portions of electrolyte sheet between the anode surface strips so that the tubular columns and intervening portions form the continuous sheet rising vertically along the opposite anode surfaces and surrounding a plurality of the vertically flowing tubes of mercury. The cell comprises a body 1, including an inlet 4 for introducing electrolyte solution, an outlet 5 for removal of chlorine and overflow of brine; a top 2 including means 6 for securing vertical graphite anodes 7 and means 8 for connecting the anodes to a circuit; and a bottom 3 which includes a base-plate 9 which holds vertical tubular cathode supports 10, an inlet 11 for introducing mercury, an outlet 13 for removing amalgam, and means 14 for connecting the cathodes to the circuit. The anodes 7 (seen in plan in Fig. 2) have spaced vertical anodically active surface strips 43 and grooves 19 surrounding the cathode supports 10. Mercury entering at 11 is distributed by a manifold 12 to the tubular cathode supports 10, passes up and overflows from the tops of the supports 10 to form a continuous thin film flowing down the outside of the supports 10, and flows across the base plate 9 to outlet 13. Electrolyte entering at 4 fills the cell to a level determined by outlet 5 and submerges the cathode supports 10. The electrolyte flows down spaces 25 provided between the anodes 7 and the shell 26 of the cell, and spaces between groups of anodes if these are provided; these spaces are in communication at both the top and bottom of the cell. Electrolyte rises up as columns between the anode surface strips 43, and also rises up as tubular columns surrounding the mercury cathodes around supports 10, the electrolyte being aided in this upward flow by bubbles of chlorine released at the anode surfaces. Alkali metal, such as sodium, formed at the cathodes, amalgamates, and the amalgam is removed through outlet 13, which is provided with means for washing and decomposing the amalgam, and means for flushing the cell to remove accumulated deposits. The cathode supports 10 may have " funnel " tops acting as weirs; the tops may also be notched at spaced intervals, or constructed of porous metal. The supports may be oval or hexagonal tubes as well as cylindrical in shape. Instead of tubes, solid wires or rods may be used with means to introduce mercury on top of such members. Cables or wires may also be used passing between the anode surfaces, being covered with mercury by dipping into wells of mercury at the bottom of the run. The anodes may be flat sheets when new, as vertical grooves will be worn in the graphite. In modifications the anodes may be as shown in plan in Figs. 20, 21 and 22, where 45, 50 and 52 are anodes and 46 are cathodes.