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Stabilization of basic oxygen furnace slag by hot-stage carbonation treatment

机译:热阶段碳化处理稳定碱性氧气炉渣

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摘要

Treatment and disposal of Basic Oxygen Furnace (BOF) slag, a residue of the steel production process characterized by high basicity and propensity for heavy metal leaching, is a costly burden on metallurgical plants; a sustainable valorization route is desired. The stabilization of BOF slag utilizing hot-stage carbonation treatment was investigated; this approach envisions carbonation during the hot-to-cold pathway followed by the material after the molten slag is poured and solidified. Three experimental methodologies were employed: (i) in-situ thermogravimetric analyzer (TGA) carbonation was used to assess carbonation reaction kinetics and thermodynamic equilibrium at high temperatures; (ii) pressurized basket reaction carbonation was used to assess the effects of pressurization, steam addition and slag particle size; and (iii) atmospheric furnace carbonation was used to assess the effect of carbonation on the mineralogy, basicity and heavy metal leaching properties of the slag. Free lime was found to be the primary mineral participating in direct carbonation of BOF slag. Initial carbonation kinetics were comparable at temperatures ranging from 500 to 800 °C, but higher temperatures aided in solid state diffusion of CO2 into the unreacted particle core, thus increasing overall CO2 uptake. The optimum carbonation temperature of both BOF slag and pure lime lies just below the transition temperature between carbonation stability and carbonate decomposition: 830-850 °C and 750-770 °C at 1 atm and 0.2 atm CO2 partial pressures, respectively. Pressurization and steam addition contribute marginally to CO2 uptake. CO2 uptake progressively decreases with increasing particle size, but basicity reduction is similar independent of particle size. The solubility of some heavy metals reduced after carbonation (barium, cobalt and nickel), but vanadium and chromium leaching increased.
机译:碱性氧气炉渣(BOF)渣的处理和处置是钢铁生产过程中的残渣,其特征是碱度高且重金属浸出倾向高,这对冶金厂来说是沉重的负担;需要一种可持续的增值途径。研究了采用热阶段碳化处理对转炉渣的稳定作用。该方法设想在热冷路径中碳化,随后在倒入熔融炉渣并固化后进行材料碳化。采用了三种实验方法:(i)原位热重分析仪(TGA)碳化用于评估高温下的碳化反应动力学和热力学平衡; (ii)使用加压篮式反应碳酸化来评估加压,添加蒸汽和炉渣粒度的影响; (iii)常压炉碳化用于评估碳化对炉渣的矿物学,碱度和重金属浸出性能的影响。发现游离石灰是参与BOF炉渣直接碳化的主要矿物。初始碳酸化动力学在500到800°C的温度范围内是可比的,但是较高的温度有助于CO2固态扩散到未反应的颗粒核中,从而增加了总的CO2吸收量。 BOF炉渣和纯石灰的最佳碳化温度都刚好低于碳化稳定性和碳酸盐分解之间的转变温度:分别在1 atm和0.2 atm CO2分压下为830-850°C和750-770°C。加压和添加蒸汽对吸收二氧化碳的贡献很小。随着颗粒尺寸的增加,CO 2吸收逐渐降低,但碱度降低与颗粒尺寸无关。碳化后,某些重金属(钡,钴和镍)的溶解度降低,但钒和铬的浸出增加。

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