Development of corrosion of steel bars embedded in mortar made with slag from secondary metallurgy

The aim of this work is to study the evolution of the corrosion rate of reinforcements embedded in mortar specimens that have been partly or fully replaced by the sand ladle furnace white slag. Prisms are manufactured mortar 6cm x 8cm x 2cm in which are embedded reinforcing steel bars of 6mm diameter B500SD. At the time of mixing were added varying amounts of chloride ion content by weight of cement (0%, 0.4%, 0.8%, 1.2%, 2%). The specimens were made totally or partially replacing the white slag, getting four different mixes depending on the degree of substitution. After curing the specimens for 28 days in moist chambers proceeded to dry up naturally. Here are gradually dampened by its conservation in a moist chamber, periodically measuring the corrosion rate of the bars using the technique of polarization curve. The results, in terms of corrosion current and corrosion potential, were compared with those obtained on standard samples, without replacement by slag aggregate. The analysis of results allows us to know, depending on the type of mortar used, the chloride threshold with the depassivation produced steel and the corrosion rates achieved in steels in the active state in terms of mortar moisture, obtained from qualitatively using gravimetric techniques. The results achieved to date support the conclusion that no significant differences in the behavior against corrosion induced by chloride ions, between the steel bars embedded in standard samples and the steel bars embedded in samples including with aggregates from slag. Both the chloride threshold resulting in the depassivation steel as the corrosion rate reached through the bars in an active state are very similar in both types of mortars when they have the same moisture content.

Ligantes de baixo impacto ambiental e baixo custo, baseados na ativação química de escórias de aciaria

Dissertação de mestrado integrado em Engenharia Civil

Use of steel slag to neutralize acid mine drainage (AMD) in sulfidic material from a uranium mine

Acid Mine Drainage (AMD) is one of the main environmental impacts caused by mining. Thus, innovative mitigation strategies should be exploited, to neutralize acidity and prevent mobilization of trace elements in AMD. The use of industrial byproducts has been considered an economically and environmentally effective alternative to remediate acid mine drainage. Therefore, the objective of this study was to evaluate the use of steel slag to mitigate acid mine drainage in a sulfidic material from a uranium mine, as an alternative to the use of limestone. Thus, increasing doses of two neutralizing agents were applied to a sulfidic material from the uranium mine Osamu Utsumi in Caldas, Minas Gerais State. A steel slag from the company ArcelorMittal Tubarão and a commercial limestone were used as neutralizing agents. The experiment was conducted in leaching columns, arranged in a completely randomized, [(2 x 3) + 1] factorial design, consisting of two neutralizing agents, three doses and one control, in three replications, totaling 21 experimental units. Electrical conductivity (EC), pH and the concentrations of Al, As, Ca, Cd, Cu, Fe, Mn, Ni, S, Se, and Zn were evaluated in the leached solutions. The trace element concentration was evaluated by ICP-OES. Furthermore, the CO2 emission was measured at the top of the leaching columns by capturing in NaOH solution and titration with HCl, in the presence of BaCl2. An increase in the pH of the leachate was observed for both neutralizing agents, with slightly higher values for steel slag. The EC was lower at the higher lime dose at an early stage of the experiment, and CO2 emission was greater with the use of limestone compared to steel slag. A decrease in trace element mobilization in the presence of both neutralizing agents was also observed. Therefore, the results showed that the use of steel slag is a suitable alternative to mitigate AMD, with the advantage of reducing CO2 emissions to the atmosphere compared to limestone.

Characterization of mixed waste of granite and LD slag

This study focuses on the technical feasibility of the utilization of waste from the cutting of granite to adjust the chemical composition of slag from steelworks LD, targeting the addition of clinker Portland cement. For this, chemical characterization of the waste, its mixture and fusion was performed, obtaining a CaO/SiO(2) relationship of around 0.9 to 1.2 for the steelworks slag. We selected samples of the waste, mixed, melted and cooled in water and in the oven. Samples cooled in water, after examining with X-ray difractrograms, had been predominantly amorphous. For samples cooled in the furnace, which had vitreous, there was the presence of mineralogical phases Akermanita and Gehlenita, which is considered as the ideal stage for the mineral water activity of the slag. The adjustment of the chemical composition of the slag from steel works by the addition of waste granite was efficient, transforming the waste into a product that is the same as blast furnace slag and can be used in the manufacture of cement.

Hydrometallurgical recovery of valuable metals from secondary raw materials

Wastes and side streams in the mining industry and different anthropogenic wastes often contain valuable metals in such concentrations their recovery may be economically viable. These raw materials are collectively called secondary raw materials. The recovery of metals from these materials is also environmentally favorable, since many of the metals, for example heavy metals, are hazardous to the environment. This has been noticed in legislative bodies, and strict regulations for handling both mining and anthropogenic wastes have been developed, mainly in the last decade. In the mining and metallurgy industry, important secondary raw materials include, for example, steelmaking dusts (recoverable metals e.g. Zn and Mo), zinc plant residues (Ag, Au, Ga, Ge, In) and waste slurry from Bayer process alumina production (Ga, REE, Ti, V). From anthropogenic wastes, waste electrical and electronic equipment (WEEE), among them LCD screens and fluorescent lamps, are clearly the most important from a metals recovery point of view. Metals that are commonly recovered from WEEE include, for example, Ag, Au, Cu, Pd and Pt. In LCD screens indium, and in fluorescent lamps, REEs, are possible target metals. Hydrometallurgical processing routes are highly suitable for the treatment of complex and/or low grade raw materials, as secondary raw materials often are. These solid or liquid raw materials often contain large amounts of base metals, for example. Thus, in order to recover valuable metals, with small concentrations, highly selective separation methods, such as hydrometallurgical routes, are needed. In addition, hydrometallurgical processes are also seen as more environmental friendly, and they have lower energy consumption, when compared to pyrometallurgical processes. In this thesis, solvent extraction and ion exchange are the most important hydrometallurgical separation methods studied. Solvent extraction is a mainstream unit operation in the metallurgical industry for all kinds of metals, but for ion exchange, practical applications are not as widespread. However, ion exchange is known to be particularly suitable for dilute feed solutions and complex separation tasks, which makes it a viable option, especially for processing secondary raw materials. Recovering valuable metals was studied with five different raw materials, which included liquid and solid side streams from metallurgical industries and WEEE. Recovery of high purity (99.7%) In, from LCD screens, was achieved by leaching with H2SO4, extracting In and Sn to D2EHPA, and selectively stripping In to HCl. In was also concentrated in the solvent extraction stage from 44 mg/L to 6.5 g/L. Ge was recovered as a side product from two different base metal process liquors with Nmethylglucamine functional chelating ion exchange resin (IRA-743). Based on equilibrium and dynamic modeling, a mechanism for this moderately complex adsorption process was suggested. Eu and Y were leached with high yields (91 and 83%) by 2 M H2SO4 from a fluorescent lamp precipitate of waste treatment plant. The waste also contained significant amounts of other REEs such as Gd and Tb, but these were not leached with common mineral acids in ambient conditions. Zn was selectively leached over Fe from steelmaking dusts with a controlled acidic leaching method, in which the pH did not go below, but was held close as possible to, 3. Mo was also present in the other studied dust, and was leached with pure water more effectively than with the acidic methods. Good yield and selectivity in the solvent extraction of Zn was achieved by D2EHPA. However, Fe needs to be eliminated in advance, either by the controlled leaching method or, for example, by precipitation. 100% Pure Mo/Cr product was achieved with quaternary ammonium salt (Aliquat 336) directly from the water leachate, without pH adjustment (pH 13.7). A Mo/Cr mixture was also obtained from H2SO4 leachates with hydroxyoxime LIX 84-I and trioctylamine (TOA), but the purities were 70% at most. However with Aliquat 336, again an over 99% pure mixture was obtained. High selectivity for Mo over Cr was not achieved with any of the studied reagents. Ag-NaCl solution was purified from divalent impurity metals by aminomethylphosphonium functional Lewatit TP-260 ion exchange resin. A novel preconditioning method, named controlled partial neutralization, with conjugate bases of weak organic acids, was used to control the pH in the column to avoid capacity losses or precipitations. Counter-current SMB was shown to be a better process configuration than either batch column operation or the cross-current operation conventionally used in the metallurgical industry. The raw materials used in this thesis were also evaluated from an economic point of view, and the precipitate from a waste fluorescent lamp treatment process was clearly shown to be the most promising.

Heavy Metals Extracted by DTPA and Organic Acids from Soil Amended with Urban or Industrial Residues

Understanding soil responses to the application of urban or industrial residues is necessary. In the current experiment, both sources of residues were applied to the soil surface of a Hapludox soil for 8 years. The four residues studied were biodigested and centrifuged sewage sludge (LB and LC, respectively), steel slag from the metallurgic industry (E), and limed mud from the pulp and cellulose industry (LCal). The residues were applied at 0, 2, 4, and 8 Mg ha(-1) four times from 2002 to 2010 when soybean was cultivated in the summer and lopsided oat and sorghum were cultivated during the winter. The contents of heavy metals were evaluated with diethylenetriaminepentaacetic acid (DTPA) and organic acids. The LB was the residue that increased the contents of soil micronutrients and heavy metals to their greatest levels, although within limits that impair the risks of environmental contamination.

Reatividade de uma escória de siderurgia em um latossolo vermelho distrófico

O presente trabalho objetivou estudar a reatividade de uma escória de siderurgia de aciaria, em diferentes frações granulométricas, aplicada em uma amostra de um Latossolo Vermelho distrófico, ácido, em condições de laboratório. Utilizou-se um fatorial 4 x 3 + 2 com quatro repetições, sendo quatro granulometrias (material retido entre as peneiras ABNT 5-10; 10-20; 20-50 e < 50), três doses de escória, correspondentes a 0,00, 5,04 e 10,08 t ha-1, ou seja, 0,00, 1,01 e 2,02 g por copo com 0,40 dm³ de solo e duas testemunhas (escória e calcário dolomítico, na dose correspondente a V = 70 %, ou seja, 1,01 e 0,60 g por copo, respectivamente). Para definir as doses, adotou-se o método da saturação por bases, considerando-se o valor do PRNT da escória e do calcário, obtidos na granulometria correspondente. O solo foi mantido na capacidade de campo e incubado durante os períodos de três, seis e nove meses. As frações granulométricas da escória influiram diferentemente na acidez do solo. A fração retida entre as peneiras ABNT 5-10 mostrou-se ineficiente, enquanto a fração que passa pela peneira ABNT 50 foi a que conferiu o maior efeito na neutralização da acidez. A reatividade das partículas da escória retidas nas peneiras intermediárias, ABNT 10-20 e 20-50, foi proporcional aos valores vigentes na legislação brasileira para calcários. Portanto, a taxa de reatividade obtida para a escória foi de: ABNT nº 5-10 = 0 %; 10-20 = 22 %; 20-50 = 58 % e < 50 = 100 %.

Incorporación de escorias de aluminio en la fabricación de productos de Arcilla cocida

Las sociedades desarrolladas generan una gran cantidad de residuos, que necesitan una adecuada gestión. Esta problemática requiere, de este modo, una atención creciente por parte de la sociedad, debido a la necesidad de proteger el medio ambiente. En este sentido, los esfuerzos se centran en reducir al máximo la generación de residuos y buscar vías de aprovechamiento de aquellos que son inevitables, soluciones mucho más aconsejables desde el punto de vista técnico, ecológico y económico que su vertido o destrucción. Las industrias deben adoptar las medidas precisas para fomentar la reducción de estos residuos, desarrollar tecnologías limpias que permitan el ahorro de los recursos naturales que poseemos, y sobre todo buscar métodos de reutilización, reciclado, inertización y valorización de los residuos generados en su producción. La industria de la construcción es un campo muy receptivo para el desarrollo de nuevos materiales en los que incorporar estos residuos. La incorporación de diferentes residuos industriales en matrices cerámicas se plantea como una vía barata de fijar las diferentes especies metálicas presentes en transformación de rocas ornamentales, lodos de galvanización o metalúrgicos, etc. En todos los casos, la adición de estos residuos requiere su caracterización previa y la optimización de las condiciones de conformado y cocción en el caso de su incorporación a la arcilla cocida. Entre los residuos incorporados en materiales de construcción se encuentran las escorias de aluminio. La industria metalúrgica produce durante sus procesos de fusión diferentes tipos de escorias. Su reciclado es una de las líneas de interés para estas industrias. En el caso de las escorias de aluminio, su tratamiento inicial consiste en una recuperación del aluminio mediante métodos mecánicos seguido de un tratamiento químico, o plasma. Este método conduce a que la escoria final apenas contenga aluminio y sea rica en sales solubles lo que limita su almacenamiento en escombreras. La escoria es una mezcla de aluminio metal y productos no metálicos como óxidos, nitruros y carburos de aluminio, sales y otros óxidos metálicos. En este estudio se ha analizado la posibilidad de la adición de escorias de aluminio procedentes de la metalurgia secundaria en materiales de construcción, de forma que tras un procesado de las mismas permita la obtención de materiales compuestos de matriz cerámica. En la presente Tesis Doctoral se ha analizado la viabilidad técnica de la incorporación de las escorias de aluminio procedentes de la metalurgia secundaria en una matriz de arcilla cocida. Para ello se han aplicado diferentes tratamientos a la escoria y se han aplicado diferentes variables en su procesado como la energía de molienda o la temperatura de sinterizacion, además del contenido de escoria. Su compactación con agua entre el 5-10 %, secado y sinterización permite obtener piezas rectangulares de diverso tamaño. Desde el punto de vista del contenido de la escoria, se incorporó entre un 10 y 40% de escoria TT, es decir sometida una calcinación previa a 750ºC en aire. Los mejores resultados alcanzados corresponden a un contenido del 20% ESC TT, sinterizada a 980ºC, por cuanto altos contenidos en escoria condicen a piezas con corazón negro. Los productos obtenidos con la adición de 20% de escoria de aluminio a la arcilla, presentan una baja expansión tras sinterización, mejores propiedades físicas y mecánicas, y mayor conductividad térmica que los productos obtenidos con arcilla sin adiciones. Aumenta su densidad, disminuye su absorción y aumenta sus resistencias de flexión y compresión, al presentar una porosidad cerrada y una interacción escoria-matriz. En todos los casos se produce una exudación superficial de aluminio metálico, cuyo volumen está relacionado con la cantidad de escoria adicionada. Mediante la incorporación de este contenido de escoria, tras un tratamiento de disolución de sales y posterior calcinación (ESC TTQ), se mejoran las propiedades del material compuesto, no sólo sobre la de la escoria calcinada (ESC TT), sino también, sobre la escoria sin tratamiento (ESC). Si además, la adición del 20% de escoria añadida, está tratada, no sólo térmicamente sino también químicamente (ESC TTQ), éstas mejoran aún más las propiedades del material compuesto, siendo el producto más compacto, con menos poros, por lo que los valores de densidad son más elevados, menores son las absorciones y mayores resistencias de flexión y compresión, que los productos obtenidos con la adición de escoria sólo tratada térmicamente. Alcanzando valores de resistencias características a compresión del orden de 109 MPa. Los valores de conductividad térmica obtenidos también son mayores. Los ensayos tecnológicos con piezas de 160 x 30 x 5 mm y el material compuesto optimizado de arcilla+ 20%ESCTTQ, consistieron en la determinación de su expansión por humedad, eflorescencia y heladicidad, mostrando en general un mejor comportamiento que la arcilla sin adiciones. Así, se han obtenido nuevos materiales compuestos de matriz cerámica para la construcción, mejorando sus propiedades físicas, mecánicas y térmicas, utilizando escorias de aluminio procedentes de la metalurgia secundaria, como opción de valorización de estos residuos, evitando así, que se viertan a vertederos y contaminen el medio ambiente. ABSTRACT Developed societies generate a lot of waste, which need proper management. Thus, this problem requires increased attention from the society, due to the need to protect the environment. In this regard, efforts are focused on to minimize the generation of waste and find ways of taking advantage of those who are inevitable, much more advisable solutions from the technical, ecological and economic viewpoint to disposal or destruction. Industries should adopt precise measures to promote waste reduction, develop clean technologies that allow the saving of natural resources that we possess, and above all seek methods of reuse, recycling, recovery and valorisation of the waste generated in their production. The industry of the construction is a very receptive field for the development of new materials in which to incorporate these residues. The incorporation of different industrial residues in ceramic counterfoils appears as a cheap route to fix the different metallic present species in transformation of ornamental rocks, muds of galvanization or metallurgical, etc. In all the cases, the addition of these residues needs his previous characterization and the optimization of the conditions of conformed and of baking in case of his incorporation to the baked clay. Residues incorporated into construction materials include aluminium slag. The metallurgical industry produces during their fusion processes different types of slags. Recycling is one of the lines of interest to these industries. In the case of aluminium slag, their initial treatment consists of a recovery of the aluminium using mechanical methods followed by chemical treatment, or plasma. This method leads to that final slag just contains aluminium and is rich in soluble salts which limits storage in dumps. The slag is a mixture of aluminium metal and non-metallic such as oxides, nitrides and carbides of aluminium salts products and other metal oxides. The present Doctoral thesis has analysed the technical viability of the incorporation of aluminium slag from secondary Metallurgy in an array of baked clay. So they have been applied different treatments to the slag and have been applied different variables in its processing as the temperature of sintering, in addition to the content of slag or energy grinding. Its compaction with water between 5-10%, drying and sintering allows rectangular pieces of different size. From the point of view of the content of the slag, it is incorporated between 10 and 40% slag TT, that is to say, submitted a calcination prior to 750 ° C in air. The best results achieved correspond to 20% ESC TT, sintered at 980 ° C, as high levels of slag in accordance to pieces with black heart. The products obtained with the addition of 20% of slag from aluminium to clay, present a low expansion after sintering, better physical properties and mechanical, and higher thermal conductivity than the products obtained with clay, without addictions. Its density increases, decreases its absorption and increases its resistance to bending and compression, introducing a closed porosity and slag-matrix interaction. In all cases there is a superficial exudation of metallic aluminium, whose volume is related to the amount of slag added. By incorporating this content of slag, following a treatment of salt solution and subsequent calcination (ESC TTQ), are improved the properties of composite material not only on the calcined slag (ESC TT), but also in the slag without treatment (ESC). If the addition of 20% of slag added, is also treated, not only thermally but also chemically (ESC TTQ), they further improve the properties of the composite material, the product is more compact, less porous, so the values are higher density, minors are absorptions and greater resistance in bending and compression, to the products obtained with the addition of slag only treated thermally. Reaching values of compressive resistance characteristic of the order of 109 MPa. The thermal conductivity values obtained are also higher. Testing technology with pieces of 160 x 30 x 5 mm and optimized composite material of clay 20% ESCTTQ, consisted in the determination of its expansion by moisture, efflorescence and frost resistance, in general, showing a better performance than the clay without additions. Thus, we have obtained new ceramic matrix composite materials for construction, improving its physical, mechanical and thermal properties, using aluminium slag secondary metallurgy, as an option Valuation of these wastes, thus preventing them from being poured to landfills and pollute environment.

Utilization of steelmaking waste materials for production of calcium carbonate (CaCO3)

The steel industry produces, besides steel, also solid mineral by-products or slags, while it emits large quantities of carbon dioxide (CO2). Slags consist of various silicates and oxides which are formed in chemical reactions between the iron ore and the fluxing agents during the high temperature processing at the steel plant. Currently, these materials are recycled in the ironmaking processes, used as aggregates in construction, or landfilled as waste. The utilization rate of the steel slags can be increased by selectively extracting components from the mineral matrix. As an example, aqueous solutions of ammonium salts such as ammonium acetate, chloride and nitrate extract calcium quite selectively already at ambient temperature and pressure conditions. After the residual solids have been separated from the solution, calcium carbonate can be precipitated by feeding a CO2 flow through the solution. Precipitated calcium carbonate (PCC) is used in different applications as a filler material. Its largest consumer is the papermaking industry, which utilizes PCC because it enhances the optical properties of paper at a relatively low cost. Traditionally, PCC is manufactured from limestone, which is first calcined to calcium oxide, then slaked with water to calcium hydroxide and finally carbonated to PCC. This process emits large amounts of CO2, mainly because of the energy-intensive calcination step. This thesis presents research work on the scale-up of the above-mentioned ammonium salt based calcium extraction and carbonation method, named Slag2PCC. Extending the scope of the earlier studies, it is now shown that the parameters which mainly affect the calcium utilization efficiency are the solid-to-liquid ratio of steel slag and the ammonium salt solvent solution during extraction, the mean diameter of the slag particles, and the slag composition, especially the fractions of total calcium, silicon, vanadium and iron as well as the fraction of free calcium oxide. Regarding extraction kinetics, slag particle size, solid-to-liquid ratio and molar concentration of the solvent solution have the largest effect on the reaction rate. Solvent solution concentrations above 1 mol/L NH4Cl cause leaching of other elements besides calcium. Some of these such as iron and manganese result in solution coloring, which can be disadvantageous for the quality of the PCC product. Based on chemical composition analysis of the produced PCC samples, however, the product quality is mainly similar as in commercial products. Increasing the novelty of the work, other important parameters related to assessment of the PCC quality, such as particle size distribution and crystal morphology are studied as well. As in traditional PCC precipitation process, the ratio of calcium and carbonate ions controls the particle shape; a higher value for [Ca2+]/[CO32-] prefers precipitation of calcite polymorph, while vaterite forms when carbon species are present in excess. The third main polymorph, aragonite, is only formed at elevated temperatures, above 40-50 °C. In general, longer precipitation times cause transformation of vaterite to calcite or aragonite, but also result in particle agglomeration. The chemical equilibrium of ammonium and calcium ions and dissolved ammonia controlling the solution pH affects the particle sizes, too. Initial pH of 12-13 during the carbonation favors nonagglomerated particles with a diameter of 1 μm and smaller, while pH values of 9-10 generate more agglomerates of 10-20 μm. As a part of the research work, these findings are implemented in demonstrationscale experimental process setups. For the first time, the Slag2PCC technology is tested in scale of ~70 liters instead of laboratory scale only. Additionally, design of a setup of several hundreds of liters is discussed. For these purposes various process units such as inclined settlers and filters for solids separation, pumps and stirrers for material transfer and mixing as well as gas feeding equipment are dimensioned and developed. Overall emissions reduction of the current industrial processes and good product quality as the main targets, based on the performed partial life cycle assessment (LCA), it is most beneficial to utilize low concentration ammonium salt solutions for the Slag2PCC process. In this manner the post-treatment of the products does not require extensive use of washing and drying equipment, otherwise increasing the CO2 emissions of the process. The low solvent concentration Slag2PCC process causes negative CO2 emissions; thus, it can be seen as a carbon capture and utilization (CCU) method, which actually reduces the anthropogenic CO2 emissions compared to the alternative of not using the technology. Even if the amount of steel slag is too small for any substantial mitigation of global warming, the process can have both financial and environmental significance for individual steel manufacturers as a means to reduce the amounts of emitted CO2 and landfilled steel slag. Alternatively, it is possible to introduce the carbon dioxide directly into the mixture of steel slag and ammonium salt solution. The process would generate a 60-75% pure calcium carbonate mixture, the remaining 25-40% consisting of the residual steel slag. This calcium-rich material could be re-used in ironmaking as a fluxing agent instead of natural limestone. Even though this process option would require less process equipment compared to the Slag2PCC process, it still needs further studies regarding the practical usefulness of the products. Nevertheless, compared to several other CO2 emission reduction methods studied around the world, the within this thesis developed and studied processes have the advantage of existing markets for the produced materials, thus giving also a financial incentive for applying the technology in practice.

Kinetics of reduction of FeO from slag by graphite and coal chars

The rates of reduction of FeO from iron-saturated FeO-CaO-Al2O3-SiO2 slags by graphite, coke, bituminous coal and anthracitic coal chars at temperatures in the range 1 673-1873 K have been measured using a sessile drop technique. The extents of reaction were determined using EPMA analysis of quenched samples, and on line gas analysis using a quadrupole mass spectrometer. The reaction rates have been shown to be dependent critically on carbon type. For the reaction geometry used in this investigation the reduction rates of graphite and coke are observed to be faster than with coal chars. This unexpected finding is shown to be associated with differences in the dominant chemical and mass transfer mechanisms occurring at the reaction interface. High reaction rates are observed to occur with the formation of liquid Fe-C alloy product and the associated gasification of carbon from the alloy. The rates of reduction by coal chars are determined principally by the chemical reaction at the carbon/gas interface and slag phase mass transfer.

Observations of the reduction of FeO from slag by graphite, coke and coal char

The reduction of FeO from iron-saturated FeO-CaO-Al2O3-SiO2 slags by graphite, coke and coal char at 1 673 K has been investigated using a sessile drop technique. Metallographic analysis of samples quenched from the reaction temperature, and in situ observations of the reaction interface, reveal significant differences in the slag/carbon contact, and in the morphologies of the product iron and its composition; these differences were found to depend on the carbon type used in the reduction. In particular it has been shown that, in the case of graphite and coke, liquid Fe-C droplets were rapidly formed at the slag/C interface. Reactions of the slag with coal chars, in contrast, result predominantly in the formation of solid iron. These observations indicate that the reaction pathways, and hence reaction kinetics, are dependent on carbon type.

Short-term experimental data of drying shrinkage of ground granulated blast-furnace slag cement concrete

This paper presents results of laboratory testing of unrestrained drying shrinkage during a period of 154 days of different concrete mixtures from the Brazilian production line that utilize ground granulated blast-furnace slag in their compositions. Three concrete mixtures with water/cement ratio of 0.78(M1), 0.41(M2), and 0.37(M3) were studied. The obtained experimental data were compared with the analytical results from prediction models available in the literature: the ACI 209 model (ACI), the B3 model (B3), the Eurocode 2 model (EC2), the GL 2000 model (GL), and the Brazilian NBR 6118 model (NBR), and an analysis of the efficacy of these models was conducted utilizing these experimental data. In addition, the development of the mechanical properties (compressive strength and modulus of elasticity) of the studied concrete mixtures was also measured in the laboratory until 126 days. From this study, it could be concluded that the ACI and the GL were the models that most approximated the experimental drying shrinkage data measured during the analyzed period of time.

Reduction of Chromium from Al(2)O(3)-CaO-SiO(2)-CrOx Slags by Carbon Dissolved in Liquid Iron

The goal of this work is to investigate the reduction of chromium from a quaternary slag by carbon dissolved in liquid steel. Laboratory scale experiments were conducted to study the reduction of chromium oxides in the slag by carbon dissolved in the melt. These experiments were made under different conditions of slag basicity and amount of added carbon. Thermodynamic calculations based on Double Sublattice model were applied using the commercial software Thermo-Calc, with the IRSID database. The results obtained showed good correlation with practical and calculated results, making it possible to predict equilibrium conditions of the system and to determine the activities of chromium oxides in the slag.

Reaction rate and product morphology in carbon composite iron ore pellets with and without Portland cement

The aim of this work is to study the reaction rate and the morphology of intermediate reaction products during iron ore reduction when iron ore and carbonaceous materials are agglomerated together with or without Portland cement. The reaction was performed at high temperatures, and used small size samples in order to minimise heat transfer constraints. Coke breeze and pure graphite were the carbonaceous materials employed. Portland cement was applied as a binder, and pellet diameters were in the range 5.6-6.5 mm. The experimental technique involved the measurement of the pellet weight loss, as well as the interruption of the reaction at different stages, in order to submit the partially reduced pellet to scanning electron microscopy. The experimental temperature was in the range 1423-1623 K, and the total reaction time varied from 240 to 1200 s. It was observed that above 1523 K the formation of liquid slag occurred inside the pellets, which partially dissolved iron oxides. The apparent activation energies obtained were 255 kJ mol(-1) for coke breeze containing pellets, and 230 kJ mol(-1) for those pellets containing graphite. It was possible to avoid heat transfer control of the reaction rate up to 1523 K by employing small composite pellets.