An industrial oxidative ladle refining process of metallurgical grade silicon has been experimentally examined. An extensive industrial sampling campaign has been performed and samples of silicon and slag have been analyzed by inductively coupled plasma mass spectroscopy (ICP-MS). The elemental concentrations of 45 elements have been evaluated with respect to sampling time during the refining process. Major elements, such as Ca and Al, as well as trace elements are studied. The refining kinetics is discussed and groups of elements with different behaviors are distinguished. For 21 elements, which are responsive to the refining process, kinetic parameters are established. The alkaline and alkaline earth elements are identified as having the highest refining rates, whereas the rare earth elements are slower and most transition metals are quite unresponsive to the oxidative refining operation.
Flue gas recirculation (FGR) for the silicon process may facilitate increasing the CO2 concentration in the off-gas, which will be beneficial for potential future carbon capture. Lower oxygen concentration in the combustion gas will also reduce NOX emissions. An existing 400 kVA Submerged Arc Furnace (SAF) pilot setup was modified to be able to recirculate flue gas and equipped with gas analysis to monitor both the flue gas and the mixed combustion gas entering the furnace. Over a running period of 80 h, including 32 h of startup, twelve different combinations of FGR ratios and flow rates were tested using typical industrial raw materials. Increased CO2 flue gas concentrations were successfully demonstrated with concentrations over 20 vol % CO2. Emissions of NOX were shown to be reduced when isolating stable comparable periods within each tapping cycle. Graphical Abstract
Flue gas recirculation (FGR) for the silicon process may facilitate increasing the CO 2 concentration in the off-gas, which will be beneficial for potential future carbon capture. Lower oxygen concentration in the combustion gas will also reduce NO X emissions. An existing 400 kVA Submerged Arc Furnace (SAF) pilot setup was modified to be able to recirculate flue gas and equipped with gas analysis to monitor both the flue gas and the mixed combustion gas entering the furnace. Over a running period of 80 h, including 32 h of startup, twelve different combinations of FGR ratios and flow rates were tested using typical industrial raw materials. Increased CO 2 flue gas concentrations were successfully demonstrated with concentrations over 20 vol % CO 2 . Emissions of NO X were shown to be reduced when isolating stable comparable periods within each tapping cycle.The contributing editor for this article was Mansoor Barati.
Flue gas recirculation (FGR) is a method used in several industries to control emissions and process conditions, such as NO x reduction and temperature levels, and increase the CO2 concentration in the off-gas, to be better suited for methods of carbon capture. In this study, the influence of FGR, varying levels of flue gas flow and oxygen concentration on the emissions of polycyclic aromatic hydrocarbons (PAHs) was investigated during Si alloy production. In addition, computational fluid dynamics (CFD) modeling was performed using OpenFOAM for combustion of C2H2 and H2 with varying O2 levels to simulate FGR and to gain better insight into the impact of furnace operations on the PAH evolution. Experimental results show that increasing FGR (0–82.5%) and decreasing levels of oxygen (20.7–13.3 vol %) increase the PAH-42 concentration from 14.1 to 559.7 μg/Nm3. This is supported by the simulations, where increased formation of all PAHs species was observed at high levels of FGR, especially for the lighter aromatic species (like benzene and naphthalene), due to the lower availability of oxygen and the reduction in temperature. Residence time was identified as another key parameter to promote complete combustion of PAHs. Benzene oxidation can be prevented with temperatures lower than 1000 K and residence times smaller than 1 s, while complete oxidation is found at temperatures of around 1500 K.
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