Article(id=1319726191993532775, tenantId=1146029695717560320, journalId=1263187385517883426, issueId=1319726164160139662, articleNumber=null, orderNo=null, doi=10.14062/j.issn.0454-5648.20240657, pmid=null, cstr=null, oa=null, hot=null, price=null, onlineType=0, articleFormat=0, articleType=null, articleTypeStr=null, receivedDate=1729008000000, receivedDateStr=2024-10-16, revisedDate=1731945600000, revisedDateStr=2024-11-19, acceptedDate=null, acceptedDateStr=null, onlineDate=1792576843498, onlineDateStr=2026-10-21, pubDate=1752940800000, pubDateStr=2025-07-20, doiRegisterDate=null, doiRegisterDateStr=null, onlineIssueDate=1792576843498, onlineIssueDateStr=2026-10-21, onlineJustAcceptDate=null, onlineJustAcceptDateStr=null, onlineFirstDate=null, onlineFirstDateStr=null, sourceXml=null, magXml=null, createTime=1792576843498, creator=13701087609, updateTime=1792576843498, updator=13701087609, issue=Issue{id=1319726164160139662, tenantId=1146029695717560320, journalId=1263187385517883426, year='2025', volume='53', issue='7', pageStart='1777', pageEnd='2078', issueExtLink='null', onlineDate='null', pubDate='1752940800000', pubDateStr='2025-07-20', beforeIssueId=null, nextIssueId=null, price=null, status=1, issueComplete=1, articleOrder=1, issueType=-1, specialIssue=null, createTime=1792576836862, creator='13701087609', updateTime=1792577335628, updator='13701087609', preIssue=null, nextIssue=null, articleTotal=null, ext={EN=IssueExt(id=1319728256174117458, tenantId=1146029695717560320, journalId=1263187385517883426, issueId=1319726164160139662, language=EN, specialIssueTitle=, coverIllustrator=null, specialIssueEditor=, specialIssueAbout=), CN=IssueExt(id=1319728256174117459, tenantId=1146029695717560320, journalId=1263187385517883426, issueId=1319726164160139662, language=CN, specialIssueTitle=, coverIllustrator=null, specialIssueEditor=, specialIssueAbout=)}, issueFiles=null, downloadFileDto=null}, startPage=1952, endPage=1961, ext={EN=ArticleExt(id=1319726192220025192, articleId=1319726191993532775, tenantId=1146029695717560320, journalId=1263187385517883426, language=EN, title=Effect of Calcination Atmosphere on Catalytic Reduction Denitrification Performance of V-Mo-P/TiO
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Introduction Selective catalytic reduction (SCR) technology is widely used due to the advantages of high denitrification efficiency and low operating cost. The existing commercial SCR catalysts are mainly vanadium-based catalysts with V2O5 as an active component, metal oxides WO3 and MoO3 as additives, and anatase TiO2 as a carrier. They have a good denitrification activity at 320-420 ℃, but have a poor activity at a low temperature. The denitrification activity of vanadium-based catalysts is mainly related to their redox capacity, acidic sites, and chemisorbed oxygen. In order to improve their denitrification activity, in this work, V-Mo-P/TiO2 catalysts were prepared by an impregnation-roasting method. The effect of roasting atmospheres (i.e., air, hydrogen, and nitrogen) on the active components and denitrification performance of vanadium-molybdenum-titanium catalysts (V-Mo-P/TiO2) was investigated.
Methods A certain amount of oxalic acid was added into deionized water and dissolved under stirring., Ammonium metavanadate was then added into the solution, heated at 100 ℃ and stirred until the solution became dark blue. Afterwards, ammonium molybdate and diammonium hydrogen phosphate were added into the solution. TiO2 was added and impregnated into the solution under stirring for 2 h, and then dried in an oven at 108 ℃ for 12 h to obtain a precursor of V-Mo-P/TiO2 catalysts. The precursor was ground, pressed, and sieved to 40-60 mesh and placed in a fixed-bed reactor, and then roasted in different gases (i.e., air, nitrogen, and hydrogen) at 450 ℃ for 4 h to obtain different catalyst samples, which were named Air-450 ℃, N2-450 ℃, and H2-450 ℃, respectively.
The structure of the catalysts was analyzed by a model PANalytical X-Pert PRO MPD X-ray diffractometer (XRD, PANALYTEC Co., the Netherlands). The pore structure of the catalysts was determined by a model NOVA2200e specific surface area analyzer (Kantar Instruments Co., USA). The surface elemental valence of the catalysts was characterized by a model ESCALAB250Xi Instrument (Thermo Co., USA). The elemental valence states on the catalyst surface were determined by an X-ray photoelectron spectroscope (XPS). The redox capacity and surface acidity of the catalysts were characterized with H2-TPR and NH3-TPD, respectively, and the NO adsorption on the catalyst surface was determined with NO-TPDe. Pyridine adsorption test (Py-FT IR) was performed using a model PE Spectrum II infrared spectrometer (PerkinElmer Co., USA) to characterize the types and strengths of the acidic sites on the catalyst surface.
The catalyst activity was tested in a fixed-bed reactor at a gas flow rate of 1400 mL/min, a NO concentration of 500 mg-Nm3, an O2 concentration of 8%, and an NH3∶NO volume ratio of 1∶1 at 80-300 ℃. The catalysts were used in a fixed-bed reactor with a gas flow rate of 1400 mL/min, a NO concentration of 500 mg-Nm3, an O2 concentration of 8%, and an NH3∶NO volume ratio of 1∶1. The denitrification tail gas was examined by a model OPTIMA7 flue gas analyzer (MRU Co., Germany) to calculate the denitrification efficiency of the catalyst.
Results and discussion At 100-250 ℃, the NO conversion of Air, N2, and H2 catalysts increases with the increase of temperature. Clearly, the denitrification performance of the catalysts obtained by roasting in three atmospheres is different, and the denitrification activity in different gases follows an order of Air > N2 > H2, in which the catalysts roasted in air have the optimum low-temperature catalytic activity.
The ratios of V4+/(V4++V5+) in the catalysts roasted in air, nitrogen, and hydrogen are 0.440, 0.482, and 0.538, respectively, indicating that more V4+ is produced in a reducing atmosphere. Roasting in air can oxidize V4+ to V5+ to a certain extent, thus increasing the percentage of V5+ on the catalyst surface and the amount of chemisorbed oxygen Oα. From the results of H2-TPR reduction, the corresponding integral area sizes are Air-450 ℃> N2-450 ℃> H2-450 ℃, indicating that polymerized vanadium is more easily formed in air. From the results of the NH3-TPD desorption, the NH3 desorption of the Air-450 ℃ catalyst is more than that of other two catalysts, and the number of acidic sites is in the following order of Air-450 ℃> N2-450 ℃> H2-450 ℃. The results of Py-FT IR further show that the acidic sites on the surfaces of the three catalysts are mainly of B-acid and L-acid. Roasting in air can increase the number of B- and L-acidic sites of the catalysts simultaneously, in which the B-acidic sites increased integrated areas of the catalysts roasted in air, nitrogen, and hydrogen are 1695, 1254 and 481, respectively, which are also basically consistent with the results of the NH3-TPD characterization. The results of NO-TPD desorption indicate that the catalyst surface at Air-450 ℃ is more prone to forming highly active bridged or double-toothed nitrates. The V—O bond and B acidic sites in polymerized vanadium make it easier for the catalyst to adsorb and activate NH3 species, which then reacts rapidly with the bridged or double-dentate nitrates to generate N2 and H2O. The reaction process mainly follows the L-H mechanism. The abundant Oα on its surface accelerates the formation of NO oxidized to NO2, promoting a rapid SCR reaction. The V-Mo-P/TiO2 catalysts roasted in air are superior to those roasted in nitrogen and hydrogen in terms of NO removal in the low-temperature section.
Conclusions V-Mo-P/TiO2 catalysts for low-temperature denitrification were prepared by an impregnation method, and the denitrification activities of V-Mo-P/TiO2 catalysts roasted in air, nitrogen, and hydrogen atmospheres were investigated. The order of their catalytic activities was as follows: air > nitrogen > hydrogen. The results of H2-TPR and XPS revealed that the catalysts roasted in air had a larger proportion of exposed V5+ on their surfaces, and contained abundant chemisorbed oxygen Oα, which further accelerated the oxidation of NO to NO2, and participated in the "fast SCR" reaction of denitrification. Moreover, the catalysts roasted in air at 450 ℃ were characterized by NH3-TPD, Py-FT IR and NO-TPD, and the results indicated that the catalysts possessed more abundant B acid sites, and the B acid and polymerized vanadium were more prone to adsorption of activated NH3 species, which further reacted with the bridged and double-toothed nitrate formed on the surface of the catalysts to generate N2 and H2O, thus promoting the SCR denitrification reaction by L-H mechanism.
, authors=Xuelian WU
1, Hui CHENG
1, Tong YU
1, Zhaojun ZHANG
1, Qi WANG
1, Fengyu WEI
1, Mengyu WANG
2, authorsList=Xuelian WU, Hui CHENG, Tong YU, Zhaojun ZHANG, Qi WANG, Fengyu WEI, Mengyu WANG, authorCompany=null, correspAuthors=Qi WANG, authorNote=
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2催化还原脱硝性能的影响, columnId=1263922770220560512, journalTitle=硅酸盐学报, columnName=研究论文, runingTitle=null, highlight=null, articleAbstract=
为探究不同性质的气体对V-Mo-P/TiO2催化剂催化活性的影响,采用浸渍-焙烧法制备了V-Mo-P/TiO2催化剂,考察了空气、氮气和氢气3种焙烧氛围对脱硝活性的作用,并对3种气氛焙烧催化剂进行了表征。结果表明:在空气氛围中焙烧的催化剂通过提高V5+含量的占比,进一步增加活性组分聚合钒的含量,来提高其氧化还原能力;通过促进催化剂表面形成V5+-OH结构来提高B酸酸性位点数量,这两者均能提高催化剂表面对NH3吸附并活化,使其再与催化剂表面形成桥式或双齿硝酸盐迅速反应生成N2和H2O,从而使其反应过程主要遵循L-H机理。其表面丰富的化学吸附氧Oα能加速NO氧化成NO2的形成,从而促进快速选择性催化还原。这些因素使空气氛围下焙烧的V-Mo-P/TiO2催化剂在低温段的NO脱除率优于氮气和氢气氛围下焙烧的催化剂。
, authors=吴雪莲
1, 程会
1, 余通
1, 张昭军
1, 王琪
1, 魏凤玉
1, 王梦瑜
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王琪(1978—),男,博士,副教授。
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