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An aluminum electrolytic cell that slows down melt fluctuation and resists erosion

An aluminum electrolytic cell and anti-scouring technology, which is applied in the field of aluminum electrolytic cells, can solve problems such as the weakening of the dynamic self-regulation ability and protection function of the side of the tank, the difficulty in maintaining a stable and ideal shape of the side of the tank, and the difficulty in efficient and stable production of the electrolytic cell. No impact on electrolysis cost, prolong life and reduce energy consumption

Inactive Publication Date: 2016-03-30
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Under the increasing pressure of energy saving and consumption reduction, the current 300-600kA large-capacity and various new-type structure aluminum electrolytic cells generally adopt low voltage (3.70-3.90V), low electrolysis temperature (925-935 ℃), low superheat ( 10℃), low alumina concentration (1.5-2.5%), narrow material balance work area and narrow heat balance work area, coupled with the use of special-shaped cathode carbon blocks on some electrolytic cells, lead to dynamic self-adjustment of the tank sides The ability and protection function are greatly weakened. Once there is a small fluctuation in the electrolytic cell, the shape of the tank side is difficult to maintain a stable and ideal shape. As a result, the electrolytic cell is difficult to produce efficiently and stably, and the erosion of the side of the melt is intensified, shortening Tank life

Method used

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  • An aluminum electrolytic cell that slows down melt fluctuation and resists erosion
  • An aluminum electrolytic cell that slows down melt fluctuation and resists erosion
  • An aluminum electrolytic cell that slows down melt fluctuation and resists erosion

Examples

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Effect test

Embodiment 1

[0031] Such as figure 1 , figure 2 , image 3 and Figure 4 As shown, the electrolytic cell liner with rectangular artificial anti-wave tank sides of the present invention is composed of dry anti-seepage material 1, common side carbon block 2, tamping paste 3, high alumina brick 4, high-strength castable material 5, Calcium silicate board 6, artificial wave-proof tank side 7, cathode steel rod 8, cathode carbon block 9 and bottom lining 10, and several raised artificial wave-proof tank sides 7 are arranged on the aluminum electrolytic cell according to the flow rule of the melt On the side of the inner liner, the artificial anti-wave groove side 7 and the electrolytic cell lining jointly build a liner structure similar to the anti-wave lift. Wherein, the artificial anti-wave tank side 7 is installed on the side of the electrolyzer (such as figure 2 and image 3 As shown), the installation position is determined according to the flow field characteristics of the electrol...

Embodiment 2

[0033] Such as figure 2 , image 3 and Figure 5 As shown, the electrolytic cell liner with trapezoidal artificial anti-wave tank side of the present invention is composed of dry anti-seepage material 1, common side carbon block 2, tamping paste 3, high alumina brick 4, high-strength castable material 5, Calcium silicate board 6, artificial wave-proof tank side 7, cathode steel rod 8, cathode carbon block 9 and bottom lining 10, and several raised artificial wave-proof tank sides 7 are arranged on the aluminum electrolytic cell according to the flow rule of the melt Lined sides. In this embodiment, except that the horizontal appearance shape of the artificial anti-wave groove side 7 is changed into a trapezoid (such as Figure 5 Shown), others are consistent with embodiment 1. The vertical cross-sectional shape of the artificial anti-wave groove side 7 of the present embodiment is still figure 2 and image 3In the section shown, the upper and lower sides of the horizon...

Embodiment 3

[0035] Such as figure 2 , image 3 , Figure 6 and Figure 7 As shown, the electrolytic cell lining with "T" shaped artificial anti-wave tank side of the present invention is composed of dry anti-seepage material 1, ordinary side carbon block 2, tamping paste 3, high alumina brick 4, high-strength cast Material 5, calcium silicate board 6, artificial wave-proof groove side 7, cathode steel rod 8, cathode carbon block 9 and bottom lining 10, and several raised artificial wave-proof groove sides 7 are arranged on the aluminum The side of the liner of the electrolytic cell. In this embodiment, except that the horizontal appearance shape of the artificial anti-wave groove side 7 is changed to a "T" shape (such as Figure 6 Shown), others are consistent with embodiment 1. Wherein, the horizontal length dimensions L1 and L2 of the artificial anti-wave groove side 7 are 10cm-30cm and 20cm-50cm respectively, and H1 and H2 are 20cm-30cm and 5cm-15cm respectively. This embodiment...

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Abstract

The invention discloses an anti-scour aluminum electrolytic bath for retarding melt fluctuation. The anti-scour aluminum electrolytic bath comprises dry-type seepage-proof material (1), ordinary side carbon blocks (2), a cathode steel bar (8), cathode carbon blocks (9) and a bottom lining (10), wherein the side structure of the lining of the aluminum electrolytic bath is provided with a plurality of raised artificial breakwater ledges (7) according to melt flow regularity. The artificial breakwater ledges are arranged, and the effects of retarding the melt fluctuation and reducing the scour of a melt to sides are achieved, so that stable operation of the electrolytic bath with low energy consumption is realized; the artificial ledges are easy to produce and install, but the main body structure of the electrolytic bath is not influenced, so that long service life of the lining of the electrolytic bath is ensured.

Description

technical field [0001] The invention relates to an aluminum electrolytic cell, in particular to an aluminum electrolytic cell capable of slowing melt fluctuation and resisting erosion. Background technique [0002] The Hall-Héroult method is currently the only method for industrial primary aluminum production. It has the advantages of simple process and less direct pollution emissions, but it also has high energy consumption (>12500kWh / t- Al) and the short life of the tank (<2500 days). According to theoretical and practical analysis, the reason for the high energy consumption of the electrolyzer is determined by the electrochemical reaction itself in the electrolysis process on the one hand, and by the structural design of the electrolyzer and the configuration of process parameters on the other hand. Among them, the most direct parameter affecting energy consumption is the cell voltage, which is closely related to the pole distance of the electrolytic cell. However...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C25C3/08
Inventor 张红亮吕晓军俆宇杰杨帅田忠良李劼
Owner CENT SOUTH UNIV
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