Abstract

The carbon anode, used in aluminum electrolysis (Hall–Heroult process), is over-consumed by air oxidation and carboxy-reaction (with CO2). Several anode features may affect this over-consumption, such as impurity content, graphitization level and anode porosity features (e.g., porosity volume fraction or pore size distribution). The two first parameters are basically related to the quality of raw materials and coke calcination conditions. Anode porosity is, however, greatly affected by anode manufacturing conditions, and is possible to be modified, to some extent, by adjusting the anode recipe and the processing parameters. This work aims to investigate the effect of anode porosity on its air reactivity. Baked anode samples were prepared in laboratory scale and then crushed into powder form (−4760 + 4000 µm). The recipe for anode preparation was similar to a typical industrial recipe, except that in the lab scale no butt particles were used in the recipe. Anode particles were then gasified at six different conversion levels (0, 5, 15, 25, 35 and 50 wt %) under air at 525 °C. The porosity was characterized in several pore size ranges, measured by nitrogen adsorption and mercury intrusion (0.0014–0.020, 0.002–0.025, 0.025–0.100, 0.1–40.0 and superior at 40 µm). The volume variation of each pore range, as a function of carbon conversion, was assessed and used to determine the size of the most active pores for air oxidation. The most active pore size was found to be the pores inferior at 40 µm before 15 wt % of gasification and pores superior at 40 µm between 15 and 50 wt % of carbon conversion. Limitation of pore size range could be used as an additional guideline, along with other targets such as high homogeneity and density, to set the optimum anode manufacturing parameters.

Highlights

  • Aluminum is produced by the reduction of alumina (Al2 O3 ) in an electrolysis cell at 960 ◦ C, according to the Hall–Héroult process

  • Anode particles were gasified under air at 525 ◦ C in two different reactors (Thermo-Gravimetric Analyzer and Fixed Bed Reactor) and at up to six carbon conversion levels (0, 5, 15, 25, 35 and 50 wt %)

  • The variation of gasification percentages of the anode particles allows the evaluation of surface area and pore volume evolution for different carbon conversion ranges

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Summary

Introduction

Aluminum is produced by the reduction of alumina (Al2 O3 ) in an electrolysis cell at 960 ◦ C, according to the Hall–Héroult process. The cell contains carbon anodes, carbon cathode and molten cryolite as electrolyte. The anode top is exposed to the ambient air (despite a cover of crushed bath and alumina) and the temperature ranges between. 400 and 600 ◦ C [1] In this range, the oxygen in the air can react with the carbon anode, according to the Equations (1) and (2). The oxygen in the air can react with the carbon anode, according to the Equations (1) and (2) Both reactions are undesirable since the carbon anode is consumed without

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