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锰负载钛锆和钛锡复合氧化物催化剂烟气脱汞实验研究
引用本文:董璐,黄亚继,袁琦,程好强,丁守一,王圣,段钰锋.锰负载钛锆和钛锡复合氧化物催化剂烟气脱汞实验研究[J].燃料化学学报,2020,48(6):741-751.
作者姓名:董璐  黄亚继  袁琦  程好强  丁守一  王圣  段钰锋
作者单位:东南大学 能源热转换及其过程测控教育部重点实验室,江苏 南京 210096;东南大学 能源热转换及其过程测控教育部重点实验室,江苏 南京 210096;光大环保技术研究院, 江苏 南京 210000;国电环境保护研究院,江苏 南京 210031
基金项目:国家重点研发计划(2016YFC0201105),江苏省研究生科研创新计划(KYCX17_0079)和东南大学优秀博士论文培育基金(3203009703)项目资助
摘    要:采用共沉淀法制备了TiO_2、TiZr和TiSn载体,浸渍锰制备了10%MnO_2的MnTi、MnTiZr和MnTiSn催化剂。采用BET、XRD、H_2-TPR、FT-IR和XPS等对样品进行表征,并对三种催化剂进行固定床脱汞性能实验。结果表明,在100-300℃,MnTiZr和MnTiSn催化剂脱汞性能均优于MnTi催化剂,这归因于Sn和Zr的引入提升了催化剂比表面积和低温氧化还原性能增加了催化剂表面的酸性位点数量、高价态锰离子和O~*含量;在反应温度为150-300℃,MnTiSn催化剂脱汞效率均高于MnTiZr催化剂这是由于前者具有更好的氧化还原性能,表面具有更多含量的高价态锰离子、O~*含量和酸性位点数量;在Hg~0脱除过程中催化剂表面活性组分如高价态锰离子和O~*均消耗,参与了Hg~)氧化为Hg~(2+)的反应且MnTiSn催化剂表面活性组分的消耗量更多。

关 键 词:    TiO2  ZrO2  SnO2
收稿时间:2020-04-14

Experimental study on the mercury removal from flue gas using manganese modified titanium-zirconium and titanium-tin composite oxide catalysts
DONG Lu,HUANG Ya-ji,YUAN Qi,CHENG Hao-qiang,DING Shou-yi,WANG Sheng,DUAN Yu-feng.Experimental study on the mercury removal from flue gas using manganese modified titanium-zirconium and titanium-tin composite oxide catalysts[J].Journal of Fuel Chemistry and Technology,2020,48(6):741-751.
Authors:DONG Lu  HUANG Ya-ji  YUAN Qi  CHENG Hao-qiang  DING Shou-yi  WANG Sheng  DUAN Yu-feng
Abstract:In this study, TiO2, TiZr and TiSn supports were prepared using co-precipitation method, and MnTi, MnTiZr, and MnTiSn catalysts with MnO2 content of 10%were prepared by the wet impregnation method. BET, XRD, H2-TPR, FT-IR, and XPS were employed to characterize the prepared samples. The Hg0 removal performance tests over the three catalysts were conducted in a fixed-bed reactor apparatus. The results indicated that the Hg0 removal performance of MnTiZr and MnTiSn catalysts was better than that of MnTi catalyst in the temperature range of 100-300℃. This could be attributed to the introduction of Sn and Zr, which increased the specific surface area of the catalyst, improved the low-temperature redox performance of the catalyst, and elevate the number of acid sites, the high valence manganese ions concentration and O* content on the catalyst surface. The mercury removal efficiency of the MnTiSn catalyst was higher than that of MnTiZr catalyst at reaction temperature of 150-300℃, which could be ascribed to the higher redox performance of the MnTiSn catalyst and more content of the high valence manganese ions, O*, and surface acid sites on its surface. During the removal of Hg0 in flue gas by MnTiZr and MnTiSn catalysts, active ingredients on the catalyst surface such as high-valence manganese ions and O* were consumed and participated in the reaction of Hg0 oxidation to Hg2+. And the consumed amount of active ingredients on the surface of MnTiSn catalyst was more than that on the MnTiZr catalyst.
Keywords:mercury  manganese  TiO2  ZrO2  SnO2  
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