摘要
The content of noble metal loading and the reduction process of the catalysts are important factors influence the economic indicator and catalytic perfo rmance for industrial catalysis.In the present work,Pd/CeO_2 NT(Pd supported on the CeO_2 nanotubes)catalysts are prepared with the hydrothermal synthesized CeO_2 NT and glutathione(GSH)reduced Pd nanoparticles via imp regnation.The content of Pd loading as well as the catalysts reduction temperature are optimized to the CO oxidation reduction.Our results show that the best Pd loading is 1.5%Pd/CeO2 NT.The catalysts reduced at 350 ℃ for 2 h prior to catalytic reaction perform the best toward CO oxidation,which reaches completely CO conversion at70℃.The XRD,Raman,H_2-TPR,TEM,BET and XPS characterization reveal that the excellent catalytic perfo rmance of 350 ℃ 1.5%Pd/CeO_2 NT sample can be attributed the high Pd~0 species and oxygen vaca ncy in the sample,which are important factors influence the activity of the catalysts.
The content of noble metal loading and the reduction process of the catalysts are important factors influence the economic indicator and catalytic perfo rmance for industrial catalysis.In the present work,Pd/CeO_2 NT(Pd supported on the CeO_2 nanotubes)catalysts are prepared with the hydrothermal synthesized CeO_2 NT and glutathione(GSH)reduced Pd nanoparticles via imp regnation.The content of Pd loading as well as the catalysts reduction temperature are optimized to the CO oxidation reduction.Our results show that the best Pd loading is 1.5%Pd/CeO2 NT.The catalysts reduced at 350 ℃ for 2 h prior to catalytic reaction perform the best toward CO oxidation,which reaches completely CO conversion at70℃.The XRD,Raman,H_2-TPR,TEM,BET and XPS characterization reveal that the excellent catalytic perfo rmance of 350 ℃ 1.5%Pd/CeO_2 NT sample can be attributed the high Pd~0 species and oxygen vaca ncy in the sample,which are important factors influence the activity of the catalysts.
引文
[1]M.Haruta,.T.Kobayashi,H.Sano,N.Yamada,Chem.Lett.16(1987)405-408.
[2]J.Li,Y.Tang,Y.Y.Ma,Z.Y.Zhang,ACS Appl.Mater.Int.10(2018)38134-38140.
[3]X.Hong,Y.Sun,Catal.Lett.146(2016)2001-2008.
[4]A.Abd El-Moemen,A.M.Abdel-Mageed,J.Bansmann,et al.,J.Catal.341(2016)160-179.
[5]S.Y.Wang,N.Li,R.M,et al.,J.Mol.Catal.A:Chem.374-375(2013)53-58.
[6]X.Zhang,Z.Qu,F.Yu,Y.Wang,Chin.J.Catal.34(2013)1277-1290.
[7]J.Wu,L Zeng,D.Cheng,et al.,Chin.J.Catal.37(2016)83-90.
[8]J.R.Gonzalez-Velasco,A.Aranzabal,J.I.Gutierrez-Ortiz,et al.,Appl.Catal.B 19(1998)189-197.
[9]M.Zhou,M.H.Li,C.J.Hou,et al.,Chin.Chem.Lett 29(2018)787-790.
[10]S.Watson,J. Catal.210(2002)295-312.
[11]R.B.Zhang,K.Lu,L.J.Zong,et al.,Appl.Surf.Sci.416(2017)183-190.
[12]Y.Ryou,J.Lee,H.Lee,et al.,Catal.Today 258(2015)518-524.
[13]L.H.Xiao,K.P.Sun,X.L.Xu,X.N.Li,Catal.Commun.6(2005)796-801.
[14]Y.Ryou,J.Lee,H.Lee,C.H.Kim,D.H.Kim,Catal.Today 307(2018)93-101.
[15]S.Yang,L.Gao,J.Am.Chen.Soc.128(2006)9330-9331.
[16]Y.Chen,T.Liu,C.Chen,et al.,Ceram.Int.39(2013)6607-6610.
[17]A.I.Y.Tok,F.Y.C.Boey,Z.Dong,X.L.Sun,J.Mater.Process.Technol.190(2007)217-222.
[18]G.Shen,Q.Wang,Z.Wang,Y.Chen,Mater.Lett.65(2011)1211-1214.
[19] K.L.Yu,G.L.Ruan,Y.H.Ben,J.J.Zou,Mater.Sci.Eng.B 139(2007)197-200.
[20]D.Liu,K.Nakashima,Inorg.Chem.48(2009)3898-3900.
[21] Z.L.Wu,D.R.Mullins,L.F.Allard,Q.F.Zhang,L.S.Wang,Chin.Chem.Lett. 29(2018)795-799.
[22]R.B.Zhang,K.Lu, L.J.Zong,et al.,Mol.Catal.442(2017)173-180.
[23]G.Chen,S.Sun, X.Sun,W.Fan, T.You,Inorg.Chem.48(2009)1334-1338.
[24]C.Wang,C.Wen,J.Lauterbach,E.Sasmaz,Appl.Catal.B 206(2017)1-8.
[25] L.F. Yang,C.K.Shi,X.E.He,J.X.Cai,Appl.Catal.B 38(2002)117-125.
[26]T.Y.Guo,J.P.Du,J.P.Li,J.Mater.Sci.51(2016)10917-10925.
[27] L Liu,Z.Yao,Y.Deng,et al.,ChemCatChem 3(2011)978-989.
[28] Z.Hu,X.Liu,D.Meng,et al.,ACS Catal.6(2016)2265-2279.