Solid State Reactions in the Na2CO3, CaF2 and CaSiO3 System. The Case of a Bifurcation Point Marco Alloni, Riccardo Carli (Prosimet S.p.A., Filago (BG), Italy) Abstract: Different studies have been conducted, beginning in 1979, on mineralogical phases which evolve in mold powders during their use in continuous casting of steel. Literature reports many studies which focus on melting, crystallization or devitrification processes and on equilibrium of mineralogical phases formed by fluxes. Most of these studies point out that, depending on different composition factors such as the basicity index, CaO/SiO2 wt %/wt%, alkali or fluorine content, these systems evolve to different silicate and fluoro-silicate phases. In many publications the most common identified phase is cuspidine, Ca4Si2O7F2, which is also an important phase in controlling thermal exchange between steel strand and mold wall. In the present work, while data available in open literature on these systems have been qualitatively confirmed, the conditions which lead, during melting process, to formation of the different crystalline fluoro-silicate phases such as cuspidine, Ca4Si2O7F2 and dicalcium sodium fluoro-silicate, Ca2SiO4.NaF, have been deeply investigated using hot stage microscope, x-ray difractometry, DSC-TGA and SEM. This study led to identification of a well-defined bifurcation point which has been found to be correlated with existence of an eutectic point in the pseudo binary system CaF2 and Na2CO3. Solid state reaction paths have been considered to explain the observed phenomena pointing out the crucial role of the liquid phase formed by this eutectic in melting process of mold fluxes and crystalline phases formation. Key words: mold flux, melting behavior, cuspidine formation, Na2CO3-CaF2 pseudo-binary system, eutectic reaction an eutectic reaction in the pseudo – binary system Na2CO3-CaF2[10]. The present study aims to further investigate chemical conditions for formation of fluorosilicate phases in mold fluxes during melting and their correlation to existence of the eutectic reaction. 1. Introduction Modern continuous casting technology takes advantage of slag formed by melting of mold fluxes to provide lubrication in the mold/solidying strand shell system. Mold fluxes may be considered as high temperature lubricants which rheological properties are controlled through chemical formulation[1]. Melting of mold flux producing this lubricating liquid slag requires heat and time. Development of a method to control this period of time, i.e. reduction of the melting rate, has been one of most important advance in this technology[2]. More recently the appeal of higher casting speeds led to requirement for faster melting fluxes. This has been achieved through use of large amounts of fluxing components and through use of low temperature melting glasses which allow to inject heat into the system as chemical energy. Studies on melting of mold fluxes and on phase transformation induced by heating when mold fluxes are molten down, have been carried out by many research groups[3-7]. In our previous works [8,9,10], in situ HTC-XRD analyses showed that melting process of mold fluxes goes through formation of cuspidine before melting. Cuspidine, Ca4Si2O7F2, is a calcium fluorosilicate phase which is responsible for the heat transfer properties of recrystallized mold fluxes into mold-strand gap[11]. While many studies have been devoted on formation of cuspidine during recrystallization, only few researches can be found on the processes that leads to its formation in mold fluxes before melting. It has been shown that cuspidine starts developing at temperatures as low as 853K (580°C) seemingly correlated to the melting temperature of 2. Experimental Samples used in this work to investigate chemical conditions of formation of fluorosilicates were formulated using reagent grade CaSiO3, Na2CO3 and CaF2 (Table 1) milled and sieved through ASTM 170 mesh sieve, dried 24 hours at 393 K (120°C) and mixed in a proper lab mixer for two hours. The samples were then inserted in a platinum crucible and heated in an oven at 1173 K for 24 hours with six intergrindings. When last collected the mixtures were cooled on a copper plate and grinded for the subsequent analyses. Chemical analysis was conducted on each calcinated sample, a PW 2400 XRF Sequential Spectrometer with VCR-2540 sample changer equipment by PANalytical was used to determinate Ca, Si, Na. An electrochemical method was used to determinate fluorine content. The phases formed after heating treatment have been studied with the X-Ray Diffractometer described in previous works[8,9]. DSC-TGA analyses were also conducted by means of a STA F3 Jupiter instrument by Netzsch on some of the samples before heat treatment to identify the reaction temperatures involved in formation of the different phases in the ternary system and also on mixtures of CaF2-Na2CO3 to identify the melting point at different ratios and the carbonate decomposition temperature. Table 1 Compositions of the samples before calcination and main fluorinated phase at 1173 K Sample Na2CO3 CaF2 CaSiO3 Main fluorinated phase 1 55,1 39,9 5,1 liquid 2 52,2 37,8 10,0 liquid 3 49,3 35,7 14,9 liquid 4 14,1 10,4 75,5 dicalcium sodium fluorosilicate 5 12,1 12,6 75,3 cuspidine 6 16,3 7,8 75,9 cuspidine 7 9,9 13,2 76,9 cuspidine 8 17,6 12,7 69,7 dicalcium sodium fluorosilicate 9 45,3 12,7 42,0 dicalcium sodium fluorosilicate 10 13,0 33,3 53,7 cuspidine 11 21,7 9,3 69,0 dicalcium sodium fluorosilicate 12 25,8 15,7 58,5 dicalcium sodium fluorosilicate 13 10,5 36,8 52,6 cuspidine 14 34,6 26,9 38,5 dicalcium sodium fluorosilicate 15 14,4 1,0 83,6 NaF 16 45,0 5,0 50,0 NaF 17 60,0 6,7 33,3 NaF 18 4,3 10,3 85,5 cuspidine 19 9,1 22,7 68,2 cuspidine 64,3 dicalcium sodium fluorosilicate 50,0 dicalcium sodium fluorosilicate 20 28,6 7,1 21 40,0 10,0 3. Results and Discussion Table 1 reports composition of samples and main fluorinated phases formed by the CaSiO3 Na2CO3 - CaF2 mixtures after heating at 1173 K which are also plotted in Fig. 1. X-ray diffraction measurement pointed out presence of three main fluorinated phases formed during heating of the prepared mixtures. Two of these phases were fluorosilicates (cuspidine and dicalcium sodium fluorosilicate, Ca2SiO4.NaF) while the third one was villiaumite (NaF). ! Fig. 1 Main fluorinated phase at different compositions A liquid slag region (dark blue dots) still existed for a content of CaSiO3 up to 15% in weight. DSC-TGA analyses have been conducted on binary mixtures of sodium carbonate and fluorspar to determinate the extension of this liquid phase on the CaF2 – Na2CO3 plane. a b Endothermic peak temperature and carbonate decomposition temperature in Fig. 2b agree with endothermic peak temperature in Fig. 2a and with reportedand in calcium previousfluoride works[8,9,10] for Fig. 2a - 2b – 2c DSC-TGA analyses of a 60%-40% mixture temperatures of sodium carbonate and DSCcuspidine formation proving that the reaction is TGA of sample 8 and sample 16 c associated with formation of liquid phase. It has been possible to prove that liquid slag On the contrary in Fig. 2c the endothermic peak was forming at a temperature of 850 K for CaF2/ had an higher temperature, 1125 K, and carbonate Na2CO3 ratios (wt./wt.) going from 1:5 to 1:1 and decomposition started at 1032 K. These that carbonate decomposition occurred at an higher temperatures are consistent with data on temperature, 1012 K. decomposition of sodium carbonate when mixed If content of wollastonite was above 15% in with silicon dioxide[12]. In this case no interaction weight, the system was solid and cuspidine (red between calcium fluoride and sodium carbonate to dots) and dicalcium sodium fluorosilicate (light blue produce liquid slag at 850 K has been observed, dots) were main phases containing fluorine formed. combined with a lack of fluorosilicate phases in the However in the region where the CaF2/Na2CO3 ratio sample. was lower than 1:5 the main fluorinated phase found Based on this results it may be said that eutectic by XRD was NaF (black dots) and no fluorosilicate reaction between Na 2 CO 3 and CaF 2 is the phases were found. bifurcation point in the reaction paths responsible DSC-TGA measurements carried out on a 60% for formation of intermediate phase, such as - 40% Na2CO3 - CaF2 mixture and CaF2 - Na2CO3 cuspidine, that allows the system to melt down. CaSiO3 mixes with same proportions as sample #8 and sample #16 are reported in Fig. 2a, 2b and 2c. These last two compositions were chosen 4. Conclusions because the CaF2/Na2CO3 ratios were respectively in and out of the range found for the eutectic An investigation on fluorinated phases formed reaction. in the ternary system Na2CO3 – CaF2 – CaSiO3 was carried out emphasizing the correlation existing between a liquid phase in the Na2CO3 – CaF2 forming at a relatively low temperature and the generation of these phases. Furthermore a region of compositions at an higher sodium carbonate – calcium fluoride ratio compared to the low temperature liquid phase has been observed in which major fluorinated phase found was villiaumite. The phenomenon has been studied in depth through use of DSC-TGA analyses which confirmed that an endothermic reaction, which involves carbonate decomposition and which generates fluorosilicate phases, occur in the ternary mixture at the same temperature as the eutectic reaction in the pseudo-binary system. Samples, which did not show presence of fluorosilicates phases during XRD analyses, were same samples that during DSC-TGA analyses did not display an endothermic peak at 878 K. The data obtained in this research suggest that eutectic reaction between Na2CO3 and CaF2 is the bifurcation point in the reaction paths responsible for formation of intermediate phase that allows the system to melt down. References: [1] A. Del Moro, R. Carli, C. Righi, Proc of 31° convegno nazionale AIM – Convegno del 60° AIM, AIM, Milan. [2] R. Carli, A. Del Moro, C. Righi, Metall. Ital. ,2008, 99 (5) :13 [3] T. Hiromoto, R. Sato, T. Shima, Proc. Of 62nd AIME Steelmaking conference, Pittsburg, 1979, 40 [4] P. Grievson, S. Bagha, N. Machingawuta, K. Liddel, K. C. Mills, Ironmaking Steelmaking ,1988, 15 (4) :18 [5] A. Cruz, F. Chavez, A. Romero, E. Palacio,V. Arrendono, J. Mater. Process, Tech. ,2007, 182 :157 [6] I. Marschall, N. Koelbl, H. Harmuth, 6th European Conference on Continuous Casting, Riccione ,2008, 17 [7] N. Koelbl, I. Marschall, H. Harmuth, Proceed. of Molten 2009 – VIII International Conference on Molten Slags, Fluxes and Salts, ed. By M. Sanchez, r. Parra, G. Riveros and C. Diaz, Santiago of Chile ,2009, 1031 [8] R. Carli, C. Righi, M. Dapiaggi, Proc. Of Molten 2009– VIII International Conference on Molten Slags, Fluxes and Salts, ed. By M. Sanchez, r. Parra, G. Riveros and C. Diaz, Santiago of Chile ,2009, 1121 [9] M. Dapiaggi, G. Artioli, C. Righi, R. Carli, J. Non-Cryst. Solids ,2007, 353 :2852 [10] R. Carli, C. Righi, M. Dapiaggi, 7th European Conference on Continuous Casting, Dusseldorf ,2011 [11] R. Taylor, K. Mills, Physical Properties of Casting Powders 3. Thermal Conductivities of Casting Powders. Ironmaking and Steelmaking, 1988, 15, 187-194 [12] J.-W. Kim, Y.-D. Lee, H.-G. Lee, ISIJ Int. ,2001, 41 (2) : 116
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