非金属矿
非金屬礦
비금속광
NON-METALLIC MINES
2014年
5期
57-60
,共4页
杜卫刚%蒋金龙%石莹莹%杨勇%陈韬宇%钱运华%固旭%陈静
杜衛剛%蔣金龍%石瑩瑩%楊勇%陳韜宇%錢運華%固旭%陳靜
두위강%장금룡%석형형%양용%진도우%전운화%고욱%진정
凹凸棒石黏土%沸石%活性炭%脱硝%催化剂
凹凸棒石黏土%沸石%活性炭%脫硝%催化劑
요철봉석점토%비석%활성탄%탈초%최화제
palygorskite%zeolite%activated carbon%denitriifcation%catalyst
稻壳经炭化、添加NaOH和NaAlO2水热合成A型沸石-活性炭复合材料,加入凹凸棒石黏土(凹土)成型后采用浸渍法制备CuO-沸石-活性炭-凹土复合烟气脱硝催化剂(CuO-ZCP)。采用XRD、SEM、N2吸附-脱附和NH3-TPD对材料进行了表征,考察了载体类型、反应温度、CuO含量对催化剂脱硝性能的影响。结果显示,沸石-活性炭的引入提高了复合载体的孔隙以及对NH3和NO的吸附,CuO-ZCP脱硝率高于凹土以及商品活性炭和凹土混合制备的脱硝催化剂的活性。催化剂脱硝率随CuO含量的增加而增加。反应温度越高,催化剂脱硝率越高,但温度过高(280℃)会导致活性炭氧化,最佳温度为250℃。
稻殼經炭化、添加NaOH和NaAlO2水熱閤成A型沸石-活性炭複閤材料,加入凹凸棒石黏土(凹土)成型後採用浸漬法製備CuO-沸石-活性炭-凹土複閤煙氣脫硝催化劑(CuO-ZCP)。採用XRD、SEM、N2吸附-脫附和NH3-TPD對材料進行瞭錶徵,攷察瞭載體類型、反應溫度、CuO含量對催化劑脫硝性能的影響。結果顯示,沸石-活性炭的引入提高瞭複閤載體的孔隙以及對NH3和NO的吸附,CuO-ZCP脫硝率高于凹土以及商品活性炭和凹土混閤製備的脫硝催化劑的活性。催化劑脫硝率隨CuO含量的增加而增加。反應溫度越高,催化劑脫硝率越高,但溫度過高(280℃)會導緻活性炭氧化,最佳溫度為250℃。
도각경탄화、첨가NaOH화NaAlO2수열합성A형비석-활성탄복합재료,가입요철봉석점토(요토)성형후채용침지법제비CuO-비석-활성탄-요토복합연기탈초최화제(CuO-ZCP)。채용XRD、SEM、N2흡부-탈부화NH3-TPD대재료진행료표정,고찰료재체류형、반응온도、CuO함량대최화제탈초성능적영향。결과현시,비석-활성탄적인입제고료복합재체적공극이급대NH3화NO적흡부,CuO-ZCP탈초솔고우요토이급상품활성탄화요토혼합제비적탈초최화제적활성。최화제탈초솔수CuO함량적증가이증가。반응온도월고,최화제탈초솔월고,단온도과고(280℃)회도치활성탄양화,최가온도위250℃。
Zeolite A-activated carbon composite (ZC) was prepared from carbonized rice husk by hydrothermal treatment after adding NaOH and NaAlO2. CuO-zeolite-carbon-palygorskite composite denitration catalyst (CuO-ZCP) was then synthesized after mixing zeolite-carbon, palygorskite and copper nitrate followed by calcination in nitrogen. The samples were characterized by XRD, SEM, N2 adsorption-desorption and NH3-TPD. The effects of the type of support, reaction temperature, and CuO content on the catalytic properties of denitration catalyst were also investigated. The results indicated that ZC could increase the porosity of the composite support and adsorption capacities of CuO-ZCP for NH3 and NO. The NO conversion of CuO-ZCP was higher than that of CuO-palygorskite denitration catalyst and CuO-palygorskite-activated carbon composite denitration catalyst. The catalytic properties of CuO-ZCP increased with the CuO content and reaction temperature. Activated carbon in the catalyst could be oxidized at high reaction temperature (280℃). A proper reaction temperature was 250℃.