Volume 46 Issue 2
Feb.  2018
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YANG Shu-qian, HE Jian-ping, ZHANG Na, SUI Xiao-wei, ZHANG Lei, YANG Zhan-xu. Effect of rare-earth element modification on the performance of Cu/ZnAl catalysts derived from hydrotalcite precursor in methanol steam reforming[J]. Journal of Fuel Chemistry and Technology, 2018, 46(2): 179-188.
Citation: YANG Shu-qian, HE Jian-ping, ZHANG Na, SUI Xiao-wei, ZHANG Lei, YANG Zhan-xu. Effect of rare-earth element modification on the performance of Cu/ZnAl catalysts derived from hydrotalcite precursor in methanol steam reforming[J]. Journal of Fuel Chemistry and Technology, 2018, 46(2): 179-188.

Effect of rare-earth element modification on the performance of Cu/ZnAl catalysts derived from hydrotalcite precursor in methanol steam reforming

Funds:

the National Natural Science Foundation of China 21671092

the National Natural Science Foundation of China 21376237

the Doctoral Scientific Research Foundation of Liaoning Province 2016013022

More Information
  • Corresponding author: ZHANG Lei, E-mail:lnpuzhanglei@163.com; YANG Zhan-xu, E-mail:zhanxuy@126.com
  • Received Date: 2017-08-09
  • Rev Recd Date: 2017-12-13
  • Available Online: 2021-01-23
  • Publish Date: 2018-02-10
  • Zn-Al layered double hydroxides (ZnAl-LDHs) were prepared on γ-Al2O3 by an in-situ synthesis method; with ZnAl-LDHs as the supports, a series of rare-earth element M (M=Y, La, Ce, Sm and Gd) doped M/Cu/ZnAl catalysts were then obtained through sequential wet impregnation method and used in the methanol steam reforming to produce hydrogen. The M/Cu/ZnAl catalysts were characterized by XRD, SEM-EDS, N2 sorption, H2-TPR, XPS and N2O titration and the effect of rare-earth metal doping on their catalytic performance in the methanol steam reforming was then investigated. The results showed that the activity of Cu/ZnAl catalyst is closely related to the copper surface area and the reducibility; larger copper surface area and lower reduction temperature lead to a higher catalytic activity in methanol steam reforming. The addition of rare-earth elements including Ce, Sm and Gd can improve the copper dispersion, surface copper area and the catalyst reducibility, which is helpful to enhance the activity of M/Cu/ZnAl catalysts. Especially, the Ce/Cu/ZnAl catalyst exhibits the highest activity; over it, the methanol conversion is 100% (about 40% higher than that over the Cu/ZnAl catalyst) and the CO concentration in the product is only 0.39%, for the methanol steam reforming at 250℃.
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  • [1]
    JACOBSON M Z, COLELLA W G, GOLDEN D. Cleaning the air and improving health with hydrogen fuel-cell vehicles[J]. Science, 2005, 308(5730):1901-1905. doi: 10.1126/science.1109157
    [2]
    FIHRI A, ARTERO V, RAZAVET M, BAFFERT C, LEIBL W, FONTECAVE M. Cobaloxime-based photocatalytic devices for hydrogen production[J]. Angew Chem Int Ed, 2008, 47(3):564-567.
    [3]
    KUC J, NEUMANN M, ARMBRUSTER M, YOON S, ZHANG Y, ERNI R, WEIDENKAFF A, MATAM S K. Methanol steam reforming catalysts derived by reduction of perovskite-type oxides LaCo1-x-yPdx ZnyOδ[J]. Catal Sci Technol, 2016, 6:1455-1468. doi: 10.1039/C5CY01410G
    [4]
    MA Y, GUAN G, PHANTHONG P, LI X, CAO J, HAO X, WANG Z, ABUDULA A. Steam reforming of methanol for hydrogen production over nanostructured wire-like molybdenum carbide catalyst[J]. Int J Hydrogen Energy, 2014, 39(33):18803-18811. doi: 10.1016/j.ijhydene.2014.09.062
    [5]
    SA S, SILVA H, BRANDAO L, SOUSA J M, MENDES A. Catalysts for methanol steam reforming-A review[J]. Appl Catal B:Environ, 2010, 99(1/2):43-57. https://www.sciencedirect.com/science/article/pii/S0926337310002584
    [6]
    张磊, 潘立卫, 倪长军, 赵生生, 王树东, 胡永康, 王安杰, 蒋凯.甲醇水蒸气重整制氢反应条件的优化[J].燃料化学学报, 2013, 41(1):116-122. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract18110.shtml

    ZHANG Lei, PAN Li-wei, NI Chang-jun, ZHAO Sheng-sheng, WANG Shu-dong, HU Yong-kang, WANG An-jie, JIANG Kai. Optimization of methanol steam reforming for hydrogen[J]. J Fuel Chem Technol, 2013, 41(1):116-122. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract18110.shtml
    [7]
    KIM W, MOHAIDEEN K K, SEO D J, YOON L Y. Methanol-steam reforming reaction over Cu-Al-based catalysts derived from layered double hydroxides[J]. Int J Hydrogen Energy, 2017, 42(4):2081-2087. doi: 10.1016/j.ijhydene.2016.11.014
    [8]
    ZHOU J J, ZHANG Y, WU G S, MAO D S, LU G Z. Influence of the component interaction over Cu/ZrO2 catalysts induced with fractionated precipitation method on the catalytic performance for methanol steam reforming[J]. RSC Adv, 2016, 6:30176-30183. doi: 10.1039/C5RA24163D
    [9]
    DAS D, LLORCA J, DOMINGUEZ M, COLUSSI S, TROVARELLI A, GAYEN A. Methanol steam reforming behavior of copper impregnated over CeO2-ZrO2 derived from a surfactant assisted coprecipitation route[J]. Int J Hydrogen Energy, 2015, 40(33):10463-10479. doi: 10.1016/j.ijhydene.2015.06.130
    [10]
    LYTKINA A A, ZHILYAEVA N A, ERMILOVA M M, OREKHOVA N V, YAROSLAVTSEO A B. Influence of the support structure and composition of Ni-Cu-based catalysts on hydrogen production by methanol steam reforming[J]. Int J Hydrogen Energy, 2015, 40(31):9677-9684. doi: 10.1016/j.ijhydene.2015.05.094
    [11]
    HUANG Y H, WANG S F, TSAI A P, KAMEOKA S. Catalysts prepared from copper-nickel ferrites for the steam reforming of methanol[J]. J Power Sources, 2015, 281:138-145. https://www.sciencedirect.com/science/article/pii/S0378775315001962
    [12]
    BUSCA G, COSTANTINO U, MARMOTTINI F, MONTANARI T, PATRONO P, PINZARI F, RAMIS G. Methanol steam reforming over ex-hydrotalcite Cu-Zn-Al catalysts[J]. Appl Catal A:Gen, 2006, 310:70-78. doi: 10.1016/j.apcata.2006.05.028
    [13]
    YAO C Z, WANG L C, LIU Y M, WU G S, CAO Y, DAI W L, FAN K N. Effect of preparation method on the hydrogen production from methanol steam reforming over binary Cu/ZrO2 catalysts[J]. Appl Catal A:Gen, 2006, 297(2):151-158. doi: 10.1016/j.apcata.2005.09.002
    [14]
    PATEL S, PANT K K. Influence of preparation method on performance of Cu(Zn)(Zr) -alumina catalysts for the hydrogen production via steam reforming of methanol[J]. Porous Mater, 2006, 13(3):373-378. https://www.sciencedirect.com/science/article/pii/S0360319911004186
    [15]
    SHEN J P, SONG C S. Influence of preparation method on performance of Cu/Zn-based catalysts for low-temperature steam reforming and oxidative steam reforming of methanol for H2 production for fuel cells[J]. Catal Today, 2002, 77(1):89-98. https://www.sciencedirect.com/science/article/pii/S0920586102002353
    [16]
    HAMMOUD D, GENNEQUIN C, ABOUKAIS A, AAD E A. Steam reforming of methanol over x% Cu/Zn-Al 400500 based catalysts for production of hydrogen:Preparation by adopting memory effect of hydrotalcite and behavior evaluation[J]. Int J Hydrogen Energy, 2015, 40(2):1283-1297. doi: 10.1016/j.ijhydene.2014.09.080
    [17]
    CAI Y C, LIU S W, XU X L, LI S B. team reforming of methanol over CuO-ZnO-La2O3-Al2O3 catalyst[J]. Mol Catal, 2002, 2(15):152-154.
    [18]
    PATEL S, PANT K K. Activity and stability enhancement of copper-alumina catalysts using cerium and zinc promoters for the selective production of hydrogen via steam reforming of methanol[J]. J Power Sources, 2006, 159(1):139-143. doi: 10.1016/j.jpowsour.2006.04.008
    [19]
    TROVARELLI A. Catalytic properties of ceria and CeO2-containing materials[J]. Catal Rev Sci Eng, 1996, 38(4):439-520. doi: 10.1080/01614949608006464
    [20]
    HE J P, YANG Z X, ZHANG L, LI Y, PAN L W. Cu supported on ZnAl-LDHs precursor prepared by in-situ synthesis method on γ-Al2O3 as catalytic material with high catalytic activity for methanol steam reforming[J]. Int J Hydrogen Energy, 2017, 42(15):9930-9937. doi: 10.1016/j.ijhydene.2017.01.229
    [21]
    XIE R F, FAN G L, YANG L, LI F. Solvent-free oxidation of ethylbenzene over hierarchical flower-like core-shell structured Co-based mixed metal oxides with significantly enhanced catalytic performance[J]. Catal Sci Technol, 2015, 5(1):540-548. https://www.sciencedirect.com/science/article/pii/S1385894715016617
    [22]
    AGARWAL V, PATEL S, PANT K K. H2 production by steam reforming of methanol over Cu/ZnO/Al2O3 catalysts:Transient deactivation kinetics modeling[J]. Appl Catal A:Gen, 2005, 279(1):155-164. http://www.doc88.com/p-4754410122489.html
    [23]
    ZHANG L, PAN L W, NI C J, SUN T J, ZHAO S S, WANG S D, WANG A J, HU Y K. CeO2-ZrO2-promoted CuO/ZnO catalyst for methanol steam reforming[J]. Int J Hydrogen Energy, 2013, 38(11):4397-4406. doi: 10.1016/j.ijhydene.2013.01.053
    [24]
    ZHANG L, PAN L W, NI C J, SUN T J, WANG S D, WANG A J, HU Y K, ZHAO S S. Effect of precipitation aging time on the performance of CuO/ZnO/CeO2-ZrO2 for methanol steam reforming[J]. J Fuel Chem Technol, 2013, 41(7):883-888. doi: 10.1016/S1872-5813(13)60038-9
    [25]
    HURST N W, GENTRY S J, JONES A, MCNICOL B D. Temperature programmed reduction[J]. Catal Rev Sci Eng, 1982, 24(2):233-309. doi: 10.1080/03602458208079654
    [26]
    SHIM J O, NA H S, JHA A, JANG W J, JEONG D W, NAH I W, JEON B H, ROH H S. Effect of preparation method on the oxygen vacancy concentration of CeO2-promoted Cu/γ-Al2O3 catalysts for HTS reactions[J]. Chem Eng J, 2016, 306:908-915. doi: 10.1016/j.cej.2016.08.030
    [27]
    WANG C, CHENG Q P, WANG X L, MA K, BAI X Q, TAN S R, TIAN Y, TONG D, ZHENG L R, ZHANG J, LI X G. Enhanced catalytic performance for CO preferential oxidation over CuO catalysts supported on highly defective CeO2 nanocrystals[J]. Appl Surf Sci, 2017, 422:932-943. doi: 10.1016/j.apsusc.2017.06.017
    [28]
    张磊, 雷俊腾, 田园, 胡鑫, 白金, 刘丹, 杨义, 潘立卫.前驱体和沉淀剂浓度对CuO/ZnO/CeO2-ZrO2甲醇水蒸气重整制氢催化剂性能的影响[J].燃料化学学报, 2015, 43(11):1366-1374. doi: 10.3969/j.issn.0253-2409.2015.11.012

    ZHANG Lei, LEI Jun-teng, TIAN Yuan, HU Xin, BAI Jin, LIU Dan, YANG Yi, PAN Li-wei. Effect of precursor and precipitant concentration on the performance of CuO/ZnO/CeO2-ZrO2 catalyst for methanol steam reforming[J]. J Fuel Chem Technol, 2015, 43(11):1366-1374. doi: 10.3969/j.issn.0253-2409.2015.11.012
    [29]
    DAS D, LLORCA J, DOMINGUEZ M, COLUSSI S, TROVARELLI A, GAYEN A. Methanol steam reforming behavior of copper impregnated over CeO2-ZrO2 derived from a surfactant assisted coprecipitation route[J]. Int J Hydrogen Energy, 2015, 40(33):10463-10479. https://www.sciencedirect.com/science/article/pii/S0360319916326787
    [30]
    张国强, 郭天玉, 郑华艳, 李忠.焙烧温度对CuCe/Ac催化剂甲醇氧化羰基化性能的影响[J].燃料化学学报, 2016, 44(6):674-679. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract18844.shtml

    ZHANG Guo-qiang, GUO Tian-yu, ZHENG Hua-yan, LI Zhong. Effect of calcination temperature on catalytic performance of CuCe/Ac catalysts for oxidative carbonylation of methanol[J]. J Fuel Chem Technol, 2016, 44(6):674-679. http://manu60.magtech.com.cn/rlhxxb/CN/abstract/abstract18844.shtml
    [31]
    XIAO S, ZHANG Y F, GAO P, ZHONG L S, LI X P, ZHANG Z Z, WANG H, WEI W, SUN Y H. Highly efficient cu-based catalysts via hydrotalcite-like precursors for CO2 hydrogenation to methanol[J]. Catal Today, 2017, 281:327-336. doi: 10.1016/j.cattod.2016.02.004
    [32]
    LIU L J, YAO Z J, DENG Y, GAO F, LIU B, DONG L. Nanoscale ceria on the activity of CuO/CeO2 for NO reduction by CO[J]. ChemCatChem, 2011, 3(6):978-989. https://www.sciencedirect.com/science/article/pii/S0926337309001039
    [33]
    LIANG F L, YU Y, ZHOU W, XU X Y, ZHU Z H. Highly defective CeO2 as a promoter for efficient and stable water oxidation[J]. J Mater Chem A, 2015, 3(2):634-640. doi: 10.1039/C4TA05770H
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