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将等离子体还原法和常规焙烧还原法制备的Ni基催化剂用于制备太阳能催化活性吸收体,在氙灯模拟的太阳光聚光反应系统中,考察了其催化CH4-CO2重整反应活性.结果表明,等离子体还原法制备的Ni/MgO-A12O3催化活性吸收体的低温活性最高,在光辐照平均能流密度为61 kW/m2,空速36 dm3/(g·h),CH4和CO2的转化率分别为72.7%和54.5%,光能转化为化学能的效率达到42.8%.X射线衍射和透射电镜结果表明,等离子体还原的催化剂中活性组分Ni的分散性最好,平均粒径为5nm,明显小于常规催化剂.另外,助剂MgO的加入增强了载体碱性,同时降低了CH4深度裂解产生积炭的可能性.

参考文献

[1] Ji H B;Feng D Y;He Y B .[J].Journal of Natural Gas Chemistry,2010,19:575.
[2] Levy M;Levitan R;RosinH;Rubin R .[J].Journal of Solar Energy Engineering,1993,50:179.
[3] W(o)rner A;Tamme R .[J].Catalysis Today,1998,46:165.
[4] Buck R;Muir J F;Hogan R E .[J].Solar Energy Materials,1991,24:449.
[5] Muir J F;Hogan R E;Skocypec R D;Buck R .[J].Journal of Solar Energy Engineering,1994,52:467.
[6] Kodama T;Kiyama A;Moriyama T;Mizuno O .[J].Journal of Solar Energy Engineering,Transactions of the ASME,2004,126:808.
[7] Berman A;Karn R K;Epstein M .[J].Eneryg Fuels,2006,20:455.
[8] Kodama T;Ohtake H;Shimizu K I;Kitayama Y .[J].Energy & Fuels,2002,16:1016.
[9] Gokon N;Yamawaki Y;Nakazawa D;Kodama T .[J].International Journal of Hydrogen Energy,2010,35:7441.
[10] 张月萍,祝新利,潘云翔,刘昌俊.等离子体处理制备对甲烷重整Ni基催化剂抗积炭性能的改进[J].催化学报,2008(10):1058-1066.
[11] Castro Luna A E;Iriarte M E .[J].Applied Catalysis A:General,2008,343:10.
[12] (O)zdemir H;Faruk (O)ksüz(o)mer M A;Ali Gürkaynak M .[J].International Journal of Hydrogen Energy,2010,35:12147.
[13] Wang Z J;Liu Y;Shi P;Liu C J Liu Y .[J].Applied Catalysis B:Environmental,2009,90:570.
[14] Shi P;Liu C J .[J].Catalysis Letters,2009,133:112.
[15] Shang S Y;Liu G H;Chai X Y;Tao X M Li X Bai M G Chu W Dai X Y Zhao Y X Yin Y X .[J].Catalysis Today,2009,148:268.
[16] 刘改焕,储伟,龙华丽,戴晓雁,印永祥.用常压高频冷等离子体射流还原Ni/γ-Al2O3催化剂的新方法[J].催化学报,2007(07):582-584.
[17] 李代红,习敏,陶旭梅,石新雨,戴晓雁,印永祥.常压等离子体还原的Ni/γ-Al2O3催化剂的程序升温脱附研究[J].催化学报,2008(03):287-291.
[18] Liu G H;Li Y L;Chu W;Shi X Y Dai X Y Yin Y X .[J].Catalyst Communication,2008,9:1087.
[19] Moulder J F;Stickle W F;Sobol P E;Bomben K D.Handbook of X-Ray Photoelectron Spectroscopy[M].Eden Prairie:Perkin-Elmer Co,1992
[20] Daza C E;Moreno S;Molina R .[J].International Journal of Hydrogen Energy,2011,36:3886.
[21] Boukha Z;Kacimi M;Pereira MFR;Faria JL;Figueiredo JL;Ziyad M .Methane dry reforming on Ni loaded hydroxyapatite and fluoroapatite[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2007(1):299-309.
[22] Horiuchi T;Sakuma K;Fukui T;Kubo Y Osaki T Mori T .[J].Applied Catalysis A:General,1996,144:111.
[23] García V;Femández J J;Ruíz W;Mondragón F Moreno A .[J].Catalyst Communication,2009,11:240.
[24] Guo J J;Lou H;Mo L Y;Zheng X M .[J].Journal of Molecular Catalysis A:Chemical,2010,316:1.
[25] Bartholomew C H;Farrauto R J.Fundamentals of Industrial Catalytic Processes[M].New York:wiley,2006
[26] 刘水刚,李军平,赵宁,魏伟,孙予罕.介孔Ni/CaO-ZrO2纳米复合物催化甲烷和二氧化碳重整[J].催化学报,2007(11):1019-1023.
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