1983
DOI: 10.1002/srin.198305221
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Thermodynamics of Na2CO3-CaCO3-CaO slags for use in hot metal refining

Abstract: Thennodynamics of Na 2 C0 3 -CaC0 3 -CaO slags for use in hot metal refining Information from the Max-Planck-lnstitut fur Eisenforschung, paper 1426 (Abhandlung 1426) Measurements on the solubility of CaC0 3 and CaO in molten Na 2 C0 3 -CaC0 3 mixtures at 950-1400°C and Pco 2 = 1 bar. Solution thermodynamics of Na 2 C0 3 -CaC0 3 slags for use in the refining of hot metal.Thennodynamik von Na 2 COa-CaCOa-CaO-Schlacken zur Anwendung bei der Roheisenraffination Messungen der Loslichkeit von CaC0 3 und CaO in Na 2… Show more

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Cited by 4 publications
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“…According to the thermodynamic calculations of Taskinen and Janke, [49] it is evident that in the presence of hot metal saturated with carbon, the stable form of Na 2 CO 3 is Na in a gaseous form. [49] However, as suggested by Kim et al, [50] in the presence of SiO 2 , Na 2 CO 3 is thermodynamically favored to decompose into Na 2 SiO 3 and only a small fraction of initial Na 2 CO 3 is decomposed into Na-gas if no carbon is available for the reaction, which is consistent with the results of Pak et al [32] In addition to this, as the rate of evaporation is controlled by either the rate of mass transfer or chemical reaction, the effect Na 2 O-loss on the sulfide capacity is rather small, but assumedly not negligible. [2,3,51,52] The evaporation rate of Na 2 O from the slag in the presence of carbon was studied by Li et al [51] in temperatures between 1300°C (1573.15 K) and 1500°C (1773.15 K).…”
Section: B Experimental Designmentioning
confidence: 99%
“…According to the thermodynamic calculations of Taskinen and Janke, [49] it is evident that in the presence of hot metal saturated with carbon, the stable form of Na 2 CO 3 is Na in a gaseous form. [49] However, as suggested by Kim et al, [50] in the presence of SiO 2 , Na 2 CO 3 is thermodynamically favored to decompose into Na 2 SiO 3 and only a small fraction of initial Na 2 CO 3 is decomposed into Na-gas if no carbon is available for the reaction, which is consistent with the results of Pak et al [32] In addition to this, as the rate of evaporation is controlled by either the rate of mass transfer or chemical reaction, the effect Na 2 O-loss on the sulfide capacity is rather small, but assumedly not negligible. [2,3,51,52] The evaporation rate of Na 2 O from the slag in the presence of carbon was studied by Li et al [51] in temperatures between 1300°C (1573.15 K) and 1500°C (1773.15 K).…”
Section: B Experimental Designmentioning
confidence: 99%