1994
DOI: 10.1007/bf01206536
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Aluminium electrolytic cells: A computer simulator for training and supervision

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Cited by 12 publications
(8 citation statements)
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“…[8]), and increasing them gradually for lower concentrations. The last part of Table II Similarly to the preceding cases, Figure 7 shows that, for lower concentrations, the sensitivity of the cell resistance increases, and, as a consequence, the quality of cell control improves.…”
Section: Control Of Cell In Statementioning
confidence: 93%
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“…[8]), and increasing them gradually for lower concentrations. The last part of Table II Similarly to the preceding cases, Figure 7 shows that, for lower concentrations, the sensitivity of the cell resistance increases, and, as a consequence, the quality of cell control improves.…”
Section: Control Of Cell In Statementioning
confidence: 93%
“…Note that the bands identified as lvq (3a), lvq (3b), and lvq (3c) of Figure 7 are generated by the criteria in Eqs. [8], [9], and [10], respectively. In this case, due to the parabolic form of the characteristic curve ( Figure 2) four operation zones can be clearly recognized in Figure 7: standard, lvq (3a), lvq (3b), and lvq (3c).…”
Section: Control Of Cell In Statementioning
confidence: 99%
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“…Hashimoto and Ikeuchi [5] split the cell into eight components and developed a nonlinear model that included ledge formation. More recently, Tikasz et al [6,7] built a model based on an 11-component cell and made of 18 differential equations and several algebraic relations. Conceived as a user-interactive computer simulator of the cell, it is currently used as a tool for research, process analysis, process supervision, and operator training.…”
Section: Previous Workmentioning
confidence: 99%
“…The flow pattern and velocity of the electrolyte are induced by the combined effects of the gas release pattern, the drag force from the metal pad, the thermal convection, and the magnetohydrodynamic force arising from the interaction between the magnetic fields and the electric current (Feng et al, 2010;Grjotheim and Welch, 1980;Doheim et al, 2008). Tikasz et al (1994) Incorporate 3 types of alumina for alumina balance calculation Biedler (2003) and Jessen (2008) Include heat loss from anode rods, deck plate into computation Apply first order dissolution rate equation Yurkov and Mann (2005) Incorporate 3 transformation phases of alumina for heat balance computation Kolås and Støre (2009) Consider emission and neutralization for the computation of AlF 3 mass balance Gusberti et al (2011) Apply extended cell control volume for heat balance computation different additional process features into consideration, most of them only compute the global temperature of important variables and overall ledge thickness. (Significant features of these models are listed in Table 1.)…”
Section: Introductionmentioning
confidence: 97%