首页> 外文期刊>Tsvetnye Metally: The Soviet Journal of Non-Ferrous Metals >ANODIC GAS COMPOSITION AND CARBON CONSUMPTION DURING ELECTROLYSIS OF CRYOLITE-ALUMINA MELTS
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ANODIC GAS COMPOSITION AND CARBON CONSUMPTION DURING ELECTROLYSIS OF CRYOLITE-ALUMINA MELTS

机译:冰晶石-铝熔体电解过程中的阳极气体组成和碳消耗

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The theoretical composition of the primary anodic gas - according to a proposed equation for the total process in an aluminum electrolyzer [1]: 3Al_2O_3 + 5C = 6Al + 4CO_2 + CO (1) - satisfactorily corresponds to known experimental data [2, 3]. Within temperatures of 915-940 deg C and current density at the anode of 0.64-1.43 A/cm~2 the gas contains - on average - 80.5 percent CO_2, 18.8 percent CO, and 0.6 percent O_2. The composition of secondary anodic gas can be calculated from the interaction between the carbon deposited on an anode and the CO_2 contained in the primary gas. The completeness of the secondary reaction according to the reaction CO_2 + C = 2CO (2) depends on the reaction capacity and the porosity of carbonaceous material being used, the temperature, and the structural features of the anode.
机译:初级阳极气体的理论组成-根据铝电解器中整个过程的建议方程式[1]:3Al_2O_3 + 5C = 6Al + 4CO_2 + CO(1)-令人满意地对应于已知实验数据[2,3] 。在915-940摄氏度的温度范围内,阳极的电流密度为0.64-1.43 A / cm〜2,该气体平均平均包含80.5%的CO_2、18.8%的CO和0.6%的O_2。可以从沉积在阳极上的碳与一次气体中包含的CO_2之间的相互作用来计算二次阳极气体的组成。根据反应CO_2 + C = 2CO(2)进行的二次反应的完成度取决于反应容量和所用碳质材料的孔隙率,温度以及阳极的结构特征。

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