February 2021
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120 Reads
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5 Citations
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February 2021
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120 Reads
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5 Citations
February 2016
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160 Reads
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9 Citations
Hydro's HAL Ultra cell technology development has achieved a major milestone to demonstrate greener aluminium production by operating two different electrolysis cell platforms at energy consumption levels below 12 kWh/kg. Two cells based on HAL300 and HAL4e technology have been rebuild with newly developed solutions to reduce cell resistance, enhance heat conservation and further improve standard operational procedures. Applying Hydro's portfolio of modelling tools, materials knowledge, process know-how and operational competence enabled the development team to design high performance cell components and methods to reduce process variability. These elements were pre-tested on several cells before merging into full demonstrators. The HAL4e and HAL4e Ultra cell technologies will be installed as part of the Karmøy technology pilot plant.
January 2016
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25 Reads
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3 Citations
Numerical simulation of coupled bath/metal magnetohydrodynamics (MHD) and MHD stability analysis allow the optimization of anode set pattern with respect to minimal cell disturbance. The contribution of anode gas-induced forces and the impact on the flow field are discussed. During a complete anode set cycle, the anode current distribution changes significantly due to varying anode resistances, frozen bath and different metal pad heights. Typically the largest disturbance to cell stability occurs during a short time span after the anode change. With steady-state MHD simulations immediately before and after each anode change - following the sequence of the underlying set pattern - the relevant cell current and ACD distribution are determined. The impact of these parameters on cell stability is predicted with a linear MHD stability analysis for a complete anode change cycle.
January 2016
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26 Reads
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2 Citations
Modernization of the 210,000 tpy VAW Rheinwerk smelter includes installation of point feeder, alumina conveying system, state-of-the-art pot control system and foresees an increase in amperage of up to 175 kA. For the modernized pots concepts for the potlining as well as for improvements of the busbar system were developed based solely on computer simulations. For the layout of the potlining a new three-dimensional thermoelectric cell model was applied that allows prediction of side ledge contours as well as heat and voltage balances. Based on this model the choice of semi-graphitic vs. fully graphitized cathode blocks was evaluated with respect of the anticipated increase in system amperage. Temperature fields and side ledge contours predicted are in good agreement with measurements. The busbar system, designed originally for a current load of 110 kA, was improved in a very efficient manner to cope with the higher amperage. Magneto-hydrodynamic simulations predicted and plant measurements demonstrated significant improvements in cell stability and performance.
January 2016
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40 Reads
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10 Citations
Hydro’s HAL Ultra cell technology development has achieved a major milestone to demonstrate greener aluminium production by operating two different electrolysis cell platforms at energy consumption levels below 12 kWh/kg. Two cells based on HAL300 and HAL4e technology have been rebuild with newly developed solutions to reduce cell resistance, enhance heat conservation and further improve standard operational procedures. Applying Hydro’s portfolio of modelling tools, materials knowledge, process know-how and operational competence enabled the development team to design high performance cell components and methods to reduce process variability. These elements were pre-tested on several cells before merging into full demonstrators. The HAL4e and HAL4e Ultra cell technologies will be installed as part of the Karmøy technology pilot plant.
January 2016
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58 Reads
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17 Citations
The growth rate, period of oscillation, and spatial shape of interface waves in Hall-Héroult cells are determined from a linear stability analysis in the three-dimensional domain of liquid bath and metal. The linearized Maxwell and momentum equations together with the demand for hydrostatic balance at the interface describe a self-exciting oscillator. The corresponding eigenvalue problem for the interface movement is solved numerically. The resulting periods of typically 20–40s are in good agreement with measurements. Both the steady-state as well as the oscillating component of the three-dimensional magnetic field and current density pattern are included. This gives a consistent description of different instability-driving mechanisms. The spatial distribution of the electromagnetic to kinetic energy transfer is used to localize the regions in the cell which mainly cause instabilities . The influences of current intensity, ACD, metal pad height, and density ratio on strength and type of instability are demonstrated.
February 2015
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24 Reads
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1 Citation
In the context of global climate change and Hydro's focus on reducing its greenhouse gas footprint, Hydro's Primary Metal Technology (PMT) department has been focusing on low energy pot development for the last decade. Disclosing some of the development is meant as one of Hydro's contributions to the industry's effort in reducing greenhouse gas production. This paper presents Hydro's PMT experiences with the use of external potshell insulation. It presents its early uses as a tool to improve pots having cold spots, to a solution for maintaining a cathode free from bottom deposits on pots where heat input is sharply decreased, opening the door to cheap retrofitting of smelters for low energy consumption. Hie authors also mention recent development where external insulation is becoming part of pot design, which, along with other efforts in reducing voltage drops, allows stable pot operation below 12kWli/kg. All rights reserved.
January 2015
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21 Reads
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2 Citations
In the context of global climate change and Hydro’s focus on reducing its greenhouse gas footprint, Hydro’s Primary Metal Technology (PMT) department has been focusing on low energy pot development for the last decade. Disclosing some of the development is meant as one of Hydro’s contributions to the industry’s effort in reducing greenhouse gas production. This paper presents Hydro’s PMT experiences with the use of external potshell insulation. It presents its early uses as a tool to improve pots having cold spots, to a solution for maintaining a cathode free from bottom deposits on pots where heat input is sharply decreased, opening the door to cheap retrofitting of smelters for low energy consumption. The authors also mention recent development where external insulation is becoming part of pot design, which, along with other efforts in reducing voltage drops, allows stable pot operation below 12kWh/kg.
April 2013
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33 Reads
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10 Citations
TMS Light Metals
Introduction MHD Stability Analysis of Anode Set Pattern Optimization of Anode Set Pattern Effect of Gas Bubbles Conclusion
April 2013
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32 Reads
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4 Citations
Modernization of the 210,000 tpy VAW Rheinwerk smelter includes installation of point feeder, alumina conveying system, state-of-the-art pot control system and foresees an increase in amperage of up to 175 kA. For the modernized pots concepts for the potlining as well as for improvements of the busbar system were developed based solely on computer simulations. For the layout of the potlining a new three-dimensional thermoelectric cell model was applied that allows prediction of side ledge contours as well as heat and voltage balances. Based on this model the choice of semi-graphitic vs. fully graphitized cathode blocks was evaluated with respect of the anticipated increase in system amperage. Temperature fields and side ledge contours predicted are in good agreement with measurements. The busbar system, designed originally for a current load of 110 kA, was improved in a very efficient manner to cope with the higher amperage. Magneto-hydrodynamic simulations predicted and plant measurements demonstrated significant improvements in cell stability and performance. © 2013 The Minerals, Metals & Materials Society. Published 2013 by John Wiley & Sons, Inc.
... The Hall-Héroult process, on average, releases 1.5 t CO2eq/t Al from the prebaked anodes during electrodeposition of aluminum, but values down to 1.40 t CO2eq/t Al have been reported by Reny et al. [14]. Additionally, an average of 0.75 t CO2eq/t Al, ranging from 0. 13 [15]. ...
February 2021
... In metallurgy, magnetohydrodynamics is routinely used to heat, pump, stir, damp and levitate liquid metals [8]. The work [9] analyzed the magnetohydrodynamic instabilities in aluminum reduction cells. MHD instabilities refer to the interfacial gravity waves developing at the electrolyte-aluminum interface. ...
January 2016
... The plant comprises 48 cells that utilise the HAL4e technology, which has a specific energy consumption of 12.3 kWh/kg, along with 12 cells that employ the latest HAL4e Ultra technology, with a specific energy consumption ranging between 11.5-11.8 kWh/kg (Segatz et al., 2016). Notably, these values are considerably lower than the global average energy consumption of 14 kWh/kg for aluminium production and Hydro's average of 13.8 kWh/kg. ...
January 2016
... The production of aluminum by molten salt electrolysis is energy demanding with a considerable amount of input energy lost in the form of heat release to the surroundings. Today, state-of-the-art smelters are able to reach specific energy consumptions as low as 12 kWh/kg Al, while potline amperages have increased up to 500-600 kA [1,2]. The continued move towards low energy cells (lean cells) will require better insulated cells, as less heat will be generated to maintain operational temperature. ...
February 2016
... The first uses 'shallow water' theory to analyse wave propagation at the bath-metal interface 8,9 , and calculates wave growth rates (doubling times) for the most unstable waveforms to compare different designs. The second approach is to develop full 3-D models that treat in detail the geometry and generally treat the background flow with a multiphase three-dimensional model 10,11 . In these models an artificial perturbation is induced on the metal surface, and the damping response monitored via fluctuation in the anode currents (ACD). ...
January 1998
... At the same time, the extra ledge convergence loop that was initially developed to run on a VAX platform was recoded to be incorporated directly in ANSYS ® by using the ANSYS ® parametric design language (APDL) which means that the same model could be run on any computer platform. The availability of faster computers also permitted the development of 3D thermo-electric cell slice models[10,11]. It is now possible to develop full thermo-electric corner/quarter cell model[12] and even coupled 3D magneto-hydrodynamic (MHD) and thermo-electric quarter cell model[13]. ...
April 2013
... Inside the electrolysis cell, liquid metal and cryolite bath, operating at about 950 °C, are separated into two layers, about 200 mm thick, by the relatively small density difference (metal 2270 g/cm 3 , bath 2070 g/cm 3 ) and surface tension of about 0.56 N/m. In the macro-scale flow domain of the full cell, the magnetic field shapes the circulating metal layer by Lorentz forces [4] , which further induces local currents and fields. Besides the magnetohydrodynamic (MHD) stirring of the metal pad, the gas bubbles cause stirring of the bath layer. ...
April 2013
TMS Light Metals
... doi:10.1016/j.apm.2010.02.001 influence on the stability of planetary and stellar atmospheres and in practical applications in nuclear weapons, geophysics, industry as well as astrophysics, see for example, Refs. [4][5][6]. ...
January 1994
... As another example, CHAM produced the first Electrolytic SmelTER (ESTER) CFD code, for the aluminium-production industry, to simulate multi-anode electrolytic smelters of the Hall-cell type, in which electromagnetic effects and gravity waves on the molten-metal/electrolyte interface can interact to limit the performance of the equipment. Later on, ESTER was superseded by a PHOENICS-based product, Rosten [154], that was also used extensively by the industry [155][156][157]. Coal-and gas-fired furnaces, heat-exchangers, diesel and petrol (gasoline) engines, power condensers, steam generators, and natural-draught cooling towers were all among the equipment items for which CHAM produced the first CFD packages. ...
January 1993
... En se basant sur le bilan de masse effectué par Dagoberto [18], le modèle considère la réaction formant de la cryolithe comme la seule réaction subséquente à survenir lorsque les vapeurs de bain entrent en contact avec l'humidité de l'air ambiante. Na 3 AlF 6 = 2 NaF + NaAlF 4 3 NaAlF 4 + 3H 2 0 = 6 HF+ Al 2 0 3 + Na 3 AlF 6 ( 13) ( 14) Enfin, le bain électrolytique contient également une fraction d'impuretés qui se distribuent en équilibre avec la concentration dans le métal. Certains auteurs ont discuté le coefficient de distribution des impuretés utilisées dans le modèle, ou bien une concentration constante a été ciblée. ...
January 2009