首页> 外文期刊>Energy & fuels >Adsorption Mechanism and Regeneration Performance of 13X for H_2S and SO_2
【24h】

Adsorption Mechanism and Regeneration Performance of 13X for H_2S and SO_2

机译:13X对H_2S和SO_2的吸附机理及再生性能

获取原文
获取原文并翻译 | 示例
       

摘要

Claus tail gas including 1-2 vol % sulfur compounds in forms of H2S and SO2 requires to be purified for discharging. However, there are few research studies focusing on simultaneous removal performance and mechanism of H2S and SO2 mixed gases with high water vapor. In this paper, 13X was used as a sorbent to simultaneously remove H2S and SO2 in the simulated Claus tail gas. Desulfurization and regeneration performance of 13X in a fixed bed were studied. Meanwhile, the removal mechanism and the decline in regeneration efficiency of 13X in the thermal N-2-purging process were investigated by using characterization techniques of X-ray fluorescence, X-ray diffraction, transmission electron microscopy, N-2 adsorption-desorption, Raman spectroscopy, thermogravimetry-differential thermal analysis, and X-ray photoelectron spectroscopy. The results showed that the breakthrough sulfur capacity of 13X was 179.7 mg S/g sorbent, three times more than that of activated carbon (64.3 mg S/g sorbent). The adsorption removal mechanism of 13X for H2S and SO2 mixed gases was an adsorption- redox process, and crystal planes (111) and (220) in 13X were the main active centers. Under the oxygen-containing atmosphere, H2S was oxidized to elemental sulfur and SO2 was oxidized to sulfuric acid adsorbed on 13X. Meanwhile, H2S and SO2 also produced elemental sulfur through Claus reaction. Sulfur species in 13X existed in forms of elemental sulfur (ca. 40 atom %) and sulfate species (ca. 60 atom %) after the adsorption process. The proportion of elemental sulfur in 13X-E was twice as much as that of activated carbon (20 atom %). After five adsorption-regeneration cycles, the specific surface area of 13X-R decreased by 24.5% because of a small amount of sulfate residues in the pores of 13X, leading to the incomplete recovery of crystal planes (111) and (220) and the decrease of strength of crystallization which resulted in the slight decrease of micropore volume and specific surface area.
机译:需要净化含有1-2%(体积)H2S和SO2形式的硫化合物的克劳斯尾气,以进行排放。但是,很少有研究关注具有高水蒸气的H2S和SO2混合气体的同时去除性能和机理。在本文中,使用13X作为吸附剂同时去除模拟克劳斯尾气中的H2S和SO2。研究了固定床中13X的脱硫和再生性能。同时,利用X射线荧光,X射线衍射,透射电镜,N-2吸附-脱附,X射线荧光,X射线荧光等表征技术,研究了热N-2净化过程中13X的去除机理和再生效率的下降。拉曼光谱,热重分析-差热分析和X射线光电子能谱。结果表明,13X的突破硫容量为179.7 mg S / g吸附剂,是活性炭(64.3 mg S / g吸附剂)的三倍。 13X对H2S和SO2混合气体的吸附去除机理是吸附-氧化还原过程,而13X中的晶面(111)和(220)是主要的活性中心。在含氧气氛下,H2S被氧化成元素硫,SO2被氧化成被13X吸附的硫酸。同时,H2S和SO2也通过克劳斯反应生成元素硫。吸附过程之后,13X中的硫物质以元素硫(约40原子%)和硫酸盐(约60原子%)的形式存在。 13X-E中元素硫的比例是活性炭(20原子%)的两倍。经过五个吸附-再生循环后,由于13X孔中少量硫酸盐残留,使13X-R的比表面积下降了24.5%,导致晶面(111)和(220)的晶面回收不完全。结晶强度的降低导致微孔体积和比表面积的略微降低。

著录项

  • 来源
    《Energy & fuels》 |2018年第12期|12742-12749|共8页
  • 作者单位

    Nanjing Tech Univ, Coll Chem Engn, Nanjing 210009, Jiangsu, Peoples R China;

    Nanjing Tech Univ, Coll Chem Engn, Nanjing 210009, Jiangsu, Peoples R China;

    Nanjing Tech Univ, Coll Chem Engn, Nanjing 210009, Jiangsu, Peoples R China;

    Nanjing Tech Univ, Coll Chem Engn, Nanjing 210009, Jiangsu, Peoples R China;

    Nanjing Tech Univ, Coll Chem Engn, Nanjing 210009, Jiangsu, Peoples R China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

  • 入库时间 2022-08-18 04:13:57

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号