Karthikeyan Rajan , Duygu Kocaefe , Yasar Kocaefe , Jonathan Bernier , Yoann Robert , Yves Dargis
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The morphological changes and presence of sulfur in different lime samples were analyzed by scanning electron microscopy and energy-dispersive X-ray spectroscopy. Brunauer–Emmett–Teller (BET) analysis showed changes in the surface properties of hydrated lime after desulfurization. X-ray photoelectron spectroscopy (XPS) analysis provided the phase and composition identification of the sulfur species on hydrated lime and the CaSO<sub>3</sub>/CaSO<sub>4</sub> product ratio. Based on the experimental results, the optimum catalyst surface area with a specific particle size is critical to the effective conversion of Ca(OH)<sub>2</sub> into CaSO<sub>3</sub> and CaSO<sub>4</sub>. The practicality of a Ca-based desulfurizer and its ability to convert into the required product may be the key to reducing the overall cost of desulfurization in aluminum industry.</div></div>","PeriodicalId":100254,"journal":{"name":"Cleaner Materials","volume":"14 ","pages":"Article 100278"},"PeriodicalIF":0.0000,"publicationDate":"2024-11-12","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Effects of the surface properties and particle size of hydrated lime on desulfurization\",\"authors\":\"Karthikeyan Rajan , Duygu Kocaefe , Yasar Kocaefe , Jonathan Bernier , Yoann Robert , Yves Dargis\",\"doi\":\"10.1016/j.clema.2024.100278\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>In the gas treatment center in smelters, hydrogen fluoride (HF) is separated from the outlet gases of electrolysis cells, which are used to produce aluminum from alumina. 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X-ray photoelectron spectroscopy (XPS) analysis provided the phase and composition identification of the sulfur species on hydrated lime and the CaSO<sub>3</sub>/CaSO<sub>4</sub> product ratio. Based on the experimental results, the optimum catalyst surface area with a specific particle size is critical to the effective conversion of Ca(OH)<sub>2</sub> into CaSO<sub>3</sub> and CaSO<sub>4</sub>. 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引用次数: 0
摘要
在冶炼厂的气体处理中心,氟化氢 (HF) 被从电解槽的出口气体中分离出来,电解槽用于从氧化铝中生产铝。然而,SO2 大部分仍留在废气中。必须开发另一种方法来分离这种对环境有害的气体。在这项研究中,使用熟石灰[Ca(OH)2]作为催化脱硫剂,在特定的湿度条件下,对低浓度二氧化硫气体进行了半干法脱硫。在相对湿度为 17% 的条件下,100 °C 的低反应温度和 Ca 基脱硫剂的最小使用量实现了 95% 以上的二氧化硫去除率。扫描电子显微镜和能量色散 X 射线光谱分析了不同石灰样品的形态变化和硫的存在。布鲁纳-艾美特-泰勒(BET)分析表明,脱硫后熟石灰的表面性质发生了变化。X 射线光电子能谱(XPS)分析提供了熟石灰上硫物种的相位和成分鉴定,以及 CaSO3/CaSO4 产物比。根据实验结果,具有特定粒度的最佳催化剂表面积对 Ca(OH)2 有效转化为 CaSO3 和 CaSO4 至关重要。钙基脱硫剂的实用性及其转化为所需产品的能力可能是降低铝工业脱硫总成本的关键。
Effects of the surface properties and particle size of hydrated lime on desulfurization
In the gas treatment center in smelters, hydrogen fluoride (HF) is separated from the outlet gases of electrolysis cells, which are used to produce aluminum from alumina. However, SO2 largely remains in the effluent gas. Another method has to be developed to separate this gas which is harmful to the environment. In this study, semi-dry desulfurization of a SO2 containing gas was performed at low SO2 concentrations using hydrated lime [Ca(OH)2] as a catalytic desulfurizer under specific humidity conditions. The low reaction temperature of 100 °C and minimal use of the Ca-based desulfurizer under 17 % relative humidity achieved more than 95 % removal of SO2. The morphological changes and presence of sulfur in different lime samples were analyzed by scanning electron microscopy and energy-dispersive X-ray spectroscopy. Brunauer–Emmett–Teller (BET) analysis showed changes in the surface properties of hydrated lime after desulfurization. X-ray photoelectron spectroscopy (XPS) analysis provided the phase and composition identification of the sulfur species on hydrated lime and the CaSO3/CaSO4 product ratio. Based on the experimental results, the optimum catalyst surface area with a specific particle size is critical to the effective conversion of Ca(OH)2 into CaSO3 and CaSO4. The practicality of a Ca-based desulfurizer and its ability to convert into the required product may be the key to reducing the overall cost of desulfurization in aluminum industry.