Roasting-starting method of aluminium reduction cell with bulge-structure cathode

An aluminum electrolytic cell and roasting start-up technology, which is applied in the field of electrolytic aluminum, can solve the problems of complex equipment, large amount of carbon powder and coke particles embedded, electrolyte loss, etc., and achieve uniform current and temperature distribution, easy workload, and prevent breakage Effect

Inactive Publication Date: 2010-06-16
NORTHEASTERN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This roasting method can ensure the roasting quality of the electrolytic cell, and has been widely used in the roasting start-up of the electrolytic cell with a new cathode structure, but this method also has the disadvantages of expensive flame equipment used in the flame roasting stage, complex equipment, and troublesome operation
In addition to the flame-aluminum liquid two-stage roasting method, some aluminum plants also use carbon particle roasting technology. The biggest disadvantage of this method is that the amount of carbon powder coke particles embedded in the electrolytic cell is large, and the coke particles are not only placed on the cathode. The raised upper surface layer, and the coke particles need to be buried in the groove between the raised structure and the raised structure. As a result, after the electrolytic cell is started, a large amount of electrolyte carbon residue in the cell needs to be fished out
In this way, not only the labor volume and labor intensity of the electrolysis workers are greatly increased, but also a large amount of electrolyte loss is caused, the power consumption is also large, and the pollution to the environment is also serious.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] The firing starting method of the aluminum electrolytic cell with a raised structure in the cathode of the present invention is as follows:

[0020] 1. After the masonry and installation of the aluminum electrolytic cell with a protruding cathode structure is completed, and before roasting, a layer of coke particles with a particle size of 5mm is laid on the raised upper surface of each cathode carbon block of the electrolytic cell, and the paving thickness is 35mm.

[0021] The laid coke grains are a mixture of metallurgical coke grains, petroleum coke coke grains and artificial graphite coke grains in a mass ratio of 1:1:1.

[0022] 2. After the above process is completed, place the carbon anode flat on the upper surface of the coke particles or paste on the cathode protrusion. At this time, the aluminum guide rod on the carbon anode should be stuck on the anode busbar, and the anode busbar of the electrolytic cell is connected to the anode busbar. A shunt device is a...

Embodiment 2

[0030] The firing starting method of the aluminum electrolytic cell with a raised structure in the cathode of the present invention is as follows:

[0031] 1. After the masonry and installation of the aluminum electrolytic cell with a protruding cathode structure, before firing, lay a layer of coke particles with a granularity of 10mm on the raised upper surface of each cathode carbon block of the electrolytic cell, and the laying thickness is 10mm . Then lay a layer of paste on the laid coke grains, the thickness of the laying is 20mm, and fill the space between the cathode protrusions with solid metal aluminum. The solid metal aluminum is aluminum scrap, and there is no requirement for the particle size of aluminum scrap, aluminum wire, and aluminum ingot. , but the height filled with solid metal aluminum does not exceed the height of the cathode bump.

[0032] The coke particles laid are metallurgical coke particles.

[0033] The paste laid is a mixture of coke grains and...

Embodiment 3

[0040] The firing starting method of the aluminum electrolytic cell with a raised structure in the cathode of the present invention is as follows:

[0041] 1. After the masonry and installation of the aluminum electrolytic cell with a protruding cathode structure, before firing, lay a layer of coke particles with a particle size of 1mm on the raised upper surface of each cathode carbon block of the electrolytic cell, and the laying thickness is 60mm . Then lay a layer of paste on the laid coke grains, the laying thickness is 10mm, and the cathode protrusions are filled with solid metal aluminum. The solid metal aluminum is aluminum wire. There is no requirement for the particle size of the aluminum wire, but it is filled with solid metal aluminum. The height does not exceed the height of the cathode bump.

[0042] The laid coke particles are those of petroleum coke.

[0043] The paste laid is a mixture of coke grains and binders. The coke particles are the coke particles of...

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Abstract

The invention discloses a roasting-starting method of an aluminium reduction cell with a bulge-structure cathode. The bulged upper surface of the cathode carbon block is laid with a layer of coke grains, or a layer of mixed paste of coke grains and binder above the layer of coke grains; and a carbon anode is placed on the upper surface of the coke grains or the paste. When the coke grain resistor of the reduction cell is roasted to 500-800 DEG C, aluminium water is poured through an aluminium outlet, when the coke grain resistor is roasted to 950 DEG C by continuous energization, the aluminium outlet is opened, liquid electrolyte is poured, and the anode is lifted to execute wet starting of the reduction cell; or the coke grain resistor is roasted to 960-980 DEG C continuously, the liquid electrolyte is poured through the aluminium outlet, and simultaneously, the anode is lifted, the cell voltage is increased, and the reduction cell is started in a wet method directly. In the method, the used coke grains are less, the current and the temperature distribution on the surface of the cathode carbon block are uniform, thus avoiding cracking on the surface of the cathode carbon block owning to partial overheat.

Description

technical field [0001] The invention belongs to the technical field of electrolytic aluminum, and in particular relates to a method for starting the firing of an aluminum electrolytic cell. Background technique [0002] Invention patent 200810013029.8 proposes a method for starting the firing of an aluminum electrolytic cell with a new type of cathode structure with protrusions on the cathode surface. This method first uses flame roasting technology to make the temperature of the electrolytic cell reach above 700°C, and then pours aluminum liquid into it to implement Flame-aluminum liquid two-stage roasting technology. This roasting method can ensure the roasting quality of the electrolytic cell, and has been widely used in the roasting start-up of the electrolytic cell with a new cathode structure. However, this method also has the disadvantages that the flame equipment used in the flame roasting stage is expensive, complicated, and troublesome to operate. In addition to t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C25C3/06
Inventor 冯乃祥王耀武彭建平狄跃忠胡文鑫武小雷
Owner NORTHEASTERN UNIV
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