淮阴工学院学报
淮陰工學院學報
회음공학원학보
JOURNAL OF HUAIYIN INSTITUTE OF TECHNOLOGY
2014年
5期
6-11
,共6页
陈韬宇%吴典%蒋金龙%杨勇%石莹莹
陳韜宇%吳典%蔣金龍%楊勇%石瑩瑩
진도우%오전%장금룡%양용%석형형
凹凸棒石黏土%稻壳%沸石%活性炭%烟气脱硝
凹凸棒石黏土%稻殼%沸石%活性炭%煙氣脫硝
요철봉석점토%도각%비석%활성탄%연기탈초
palygorskite%rice husk%zeolite%actived carbon%flue gas denitration
稻壳炭化后添加碱液和铝源分别合成了A型、A+X型和X型沸石-活性炭复合材料,加入凹凸棒石黏土成型,采用浸渍法负载V2 O5制备V2 O5-沸石-活性炭-凹土复合脱硝催化剂。采用XRD、SEM、N2吸附和EDX对样品进行表征,考察载体类型、V2 O5含量和反应温度对催化剂低温脱硝活性的影响。结果表明,二元载体和V2 O5协同催化脱硝,其脱硝率高于纯凹土制备的脱硝催化剂。催化剂脱硝活性随V2 O5含量的增加而降低。反应温度越高,催化剂脱硝活性越高,最佳的反应温度为250℃,温度大于280℃后活性炭被氧化。
稻殼炭化後添加堿液和鋁源分彆閤成瞭A型、A+X型和X型沸石-活性炭複閤材料,加入凹凸棒石黏土成型,採用浸漬法負載V2 O5製備V2 O5-沸石-活性炭-凹土複閤脫硝催化劑。採用XRD、SEM、N2吸附和EDX對樣品進行錶徵,攷察載體類型、V2 O5含量和反應溫度對催化劑低溫脫硝活性的影響。結果錶明,二元載體和V2 O5協同催化脫硝,其脫硝率高于純凹土製備的脫硝催化劑。催化劑脫硝活性隨V2 O5含量的增加而降低。反應溫度越高,催化劑脫硝活性越高,最佳的反應溫度為250℃,溫度大于280℃後活性炭被氧化。
도각탄화후첨가감액화려원분별합성료A형、A+X형화X형비석-활성탄복합재료,가입요철봉석점토성형,채용침지법부재V2 O5제비V2 O5-비석-활성탄-요토복합탈초최화제。채용XRD、SEM、N2흡부화EDX대양품진행표정,고찰재체류형、V2 O5함량화반응온도대최화제저온탈초활성적영향。결과표명,이원재체화V2 O5협동최화탈초,기탈초솔고우순요토제비적탈초최화제。최화제탈초활성수V2 O5함량적증가이강저。반응온도월고,최화제탈초활성월고,최가적반응온도위250℃,온도대우280℃후활성탄피양화。
Zeolite ( A and X)-activated carbon was prepared by carbonization using rice husk as a raw materi-al, followed by hydrothermal treatment after adding NaOH and NaAlO2 .V2 O5 -zeolite-activated carbon-pa-lygorskite composite denitration catalyst ( V2 O5 -Z-C-PAL) was prepared by mixing zolite-activated car-bon, palygorskite ( PAL) and ammonium metavanadate through an impregnation method.The samples were characterized by XRD, SEM, EDX, N2 adsorption methods.The effects of the support, reaction temperature and content of V2 O5 on the catalytic properties of the denitration catalysts were investigated.The results indica-ted that zeolite-activated carbon could increase the porosity of the support.The NO conversion of V2 O5 -Z-C-PAL was higher than that of V2 O5 -PAL denitration catalyst for the synergistic effect of two supporters and V2 O5 .The catalytic activity of V2 O5 -Z-C-PAL decreased with the V2 O5 content and increased with reaction temperature.Activated carbon in the catalyst could be oxidized at high reaction temperature (280℃) .A proper reaction temperature was 250℃.