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Method of obtaining refined aluminium, starting from aluminium alloy scrap

机译:从铝合金废料开始获得精炼铝的方法

摘要

630,891. Electrolyte refining of aluminium. COMPAGNIE DE PRODUITS CHIMIQUES ET ELECTROMETALLURGIQUES ALAIS, FROGES & CAMARGUE. Dec. 30, 1946, No. 37983. Convention date, Dec. 3, 1945. Drawings to Specification. [Class 41] In the three-layer method of refining aluminium from aluminium alloy scrap, scrap is added to the anodic layer in excess of the quantity of alloy treated corresponding to the quantity of refined metal produced at the cathode such that as a result of the progressive increase of its depth, the anodic layer preserves a content of the heavy constituent (e.g. copper or zinc) lower than the value (40 per cent for Cu) incompatible with the purity of the refined aluminium. The initial depth of the anodic layer may be the minimum depth through which the alloy to be treated will sufficiently rapidly diffuse during the recharging step and the increase in depth of the anodic layer during the working of the cell may be equal to the depth of the electrolyte layer. The anodic alloy may be renewed by drawing off a portion thereof and diluting, as regards the heavy constituent (e.g. Cu or Zn), the remaining portion by the addition of alloy to be treated. Arrangements are provided for lifting the cathode block making contact with the refined aluminium as the bottom layer of alloy and hence the layer of refined aluminium rises and comprise a crank-wheel for lifting a rod supporting the block. Specification 405,596 is referred to.
机译:630,891。电解精炼铝。 COMPAGNIE DE PRODUITS CHIMIQUES ET ELECTROMETALLURGIQUES ALAIS,FROGES&CAMARGUE。 1946年12月30日,第37983号。公约日期,1945年12月3日。 [等级41]在从铝合金废料中精炼铝的三层方法中,将废料添加到阳极层中的量要多于与在阴极处产生的精炼金属的量相对应的合金处理量,因此随着其深度的逐渐增加,阳极层保留的重组分(例如铜或锌)的含量低于与精炼铝的纯度不相容的值(铜的40%)。阳极层的初始深度可以是在再充电步骤中待处理的合金将足够迅速扩散的最小深度,并且在电池工作期间阳极层的深度增加可以等于阳极层的深度。电解质层。可以通过抽出一部分阳极合金并通过添加要处理的合金来稀释重组分(例如铜或锌)中的剩余部分来更新阳极合金。提供了用于提升阴极块的装置,该阴极块随着合金的底层与精炼铝接触,因此精炼铝层上升,并且包括用于提升支撑着阴极块的杆的曲轴。参考规范405,596。

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