硅源对蒸氨法制备Cu/SiO_2催化剂催化甲醇裂解制氢的影响
详细信息    查看全文 | 推荐本文 |
  • 英文篇名:Catalytic performance of methanol decomposition on Cu/SiO_2 catalyst with different silica sources prepared with ammonia evaporation method
  • 作者:杜泽宇 ; 朱明 ; 包喆宇 ; 史大佑 ; 陈晓蓉 ; 许岩 ; 梅华
  • 英文作者:DU Ze-yu;ZHU Ming;BAO Zhe-yu;SHI Da-you;CHEN Xiao-rong;XU Yan;MEI Hua;College of Chemistry and Chemical Engineering,Nanjing University of Technology;Catalytic Hydrogenation Engineering Technology Research Center,Nuomeng Chem;
  • 关键词:甲醇裂解 ; 蒸氨法 ; Cu/SiO_2催化剂
  • 英文关键词:methanol decomposition;;ammonia evaporation method;;Cu/SiO_2 catalyst
  • 中文刊名:RLHX
  • 英文刊名:Journal of Fuel Chemistry and Technology
  • 机构:南京工业大学化工学院;南京(诺盟化工)催化氢化工程技术研究中心;
  • 出版日期:2018-06-15
  • 出版单位:燃料化学学报
  • 年:2018
  • 期:v.46
  • 语种:中文;
  • 页:RLHX201806007
  • 页数:8
  • CN:06
  • ISSN:14-1140/TQ
  • 分类号:63-70
摘要
采用蒸氨法制备Cu/SiO_2催化剂,分别考察气相二氧化硅(SiO_2-aer)、硅胶(SiO_2-gel)和碱性硅溶胶(SiO_2-sol)对Cu/SiO_2催化剂催化甲醇裂解制氢性能的影响,并采用N2吸附-脱附、N2O化学吸附、电感耦合等离子体原子发射光谱法(ICP-AES)、X射线衍射(XRD)、H_2程序升温还原(H_2-TPR)、透射电子显微镜(TEM)和X射线光电子能谱(XPS)等方法对催化剂进行表征。结果表明,硅源对Cu/SiO_2催化剂的活性具有较大影响。以碱性硅溶胶作为硅源制得的Cu/SiO_2-sol催化剂比表面积较大,活性中心粒径较小且分散均匀,这些使得其制氢性能优于其他两种硅源为载体所制备的催化剂。在反应温度280℃,反应压力1 MPa,甲醇质量空速0.6 h-1的条件下,相较于Cu/SiO_2-aer和Cu/SiO_2-gel催化剂,Cu/SiO_2-sol催化剂的甲醇转化率分别提高10%和7%,气相副产物CH_4和CO_2浓度也有所降低,该催化剂上的甲醇转化率和气体收率分别达到98.4%和96.7%。
        Cu/SiO_2 catalysts were prepared via ammonia evaporation method,using fumed silica( SiO_2-aer),silica gel( SiO_2-gel) and alkaline silica sol( SiO_2-sol) as the silica sources and their catalytic performance in methanol decomposition were investigated. The catalysts were characterized by N_2 adsorption-desorption,N_2O chemisorption,inductively coupled plasma atomic emission spectroscopy( ICP-AES), X-ray diffraction( XRD),H_2 temperature programmed reduction( H_2-TPR),transmission electron microscope( TEM) and X-ray photoelectron spectroscopy( XPS). The results indicate that silica source can affect the decomposition activity of Cu/SiO_2 catalysts. The Cu/SiO_2-sol catalyst prepared with alkaline silica sol exhibits larger surface area,smaller active site size and more uniform dispersion of Cu. Therefore,it gives Cu/SiO_2-sol a better decomposition performance than other catalysts. Methanol conversion on Cu/SiO_2-sol is 10% higher than that on Cu/SiO_2-aer,and 7% higher than that on Cu/SiO_2-gel. Additionally,byproducts concentration on Cu/SiO_2-sol is considerably lower than other catalysts. Under the reaction conditions of 280 ℃,1 MPa and 0. 6 h~(-1) of WHSV,methanol conversion of 98.4% and gas yield of 96.7% can be achieved.
引文
[1]TONELLI F,GORRIZ O,TARDITI A,CORNAGLIA L,ARRUA L,ABELLO M C.Activity and stability of a Cu O/Ce O2catalyst for methanol steam reforming[J].Int J Hydrogen Energy,2015,40(39):13379-13387.
    [2]AMIRI T Y,MOGHADDAS J.Cogeled copper-silica aerogel as a catalyst in hydrogen production from methanol steam reforming[J].Int J Hydrogen Energy,2015,40(3):1472-1480.
    [3]SIRIRUANG C,CHAROJROCHKUL S,TOOCHINDA P.Hydrogen production from methanol-steam reforming at low temperature over CuZn/Zr O2-doped Al2O3[J].Monatsh Chem,2016,147(7):1143-1151.
    [4]VERENDEL J J,DINER P.Efficient,low temperature production of hydrogen from methanol[J].Chem Cat Chem,2013,5(10):2795-2797.
    [5]LYTKINA A A,ZHILYAEVA N A,ERMILOVA M M,OREKHOVA N V,YAROSLAVTSEV 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.
    [6]YANG R X,CHUANG K H,WEY M Y.Hydrogen production through methanol steam reforming:Effect of synthesis parameters on Ni-Cu/Ca O-Si O2catalysts activity[J].Int J Hydrogen Energy,2014,39(34):19494-19501.
    [7]MATSUMURA Y,TANAKA K,TODE N,YAZAWA T,HARUTA M.Catalytic methanol decomposition to carbon monoxide and hydrogen over nickel supported on silica[J].J M ol Catal A:Chem,2000,152(1/2):157-165.
    [8]张雄伟,储伟,王晓东,杨维慎,盛世善,张涛.氧化铝担载的贵金属铱基催化剂的制备及其对甲醇裂解反应的催化性能[J].催化学报,2006,27(10):863-867.(ZHANG Xiong-wei,CHU Wei,WANG Xiao-dong,YANG Wei-shen,SHENG Shi-shan,ZHANG Tao.Preparation of alumina-supported nobel metal iridium catalysts and their catalytic performance for methanol decomposition[J].Chin J Catal,2006,27(10):863-867.)
    [9]YONG S T,OOI C W,CHAI S P,YU F,WU X S.Review of methanol reforming-Cu-based catalysts,surface reaction mechanisms,and reaction schemes[J].Int J Hydrogen Energy,2013,38(22):9541-9552.
    [10]YAAKOB Z,KAMARUDIN S K,DAUD W R W,YOSFIAH M R,LIM K L,KAZEMIAN H.Hydrogen production by methanol-steam reforming using Ni-M o-Cu/gamma-alumina trimetallic catalysts[J].Asia-Pac J Chem Eng,2010,5(6):862-868.
    [11]李雪,王晓文,赵明,刘建英,龚茂初,陈耀强.钙改性的Pd/Ce O2-Zr O2-Al2O3催化剂催化甲醇裂解反应[J].催化学报,2011,32(11):1739-1746.(LI Xue,WANG Xiao-wen,ZHAO Ming,LIU Jian-ying,GONG Mao-chu,CHEN Yao-qiang.Ca-modified Pd/Ce O2-Zr O2-Al2O3catalysts for methanol decomposition[J].Chin J Catal,2011,32(11):1739-1746.)
    [12]倪哲明,毛江洪,潘国祥,胥倩,李小年.Pd催化甲醇裂解制氢的反应机理[J].物理化学学报,2009,25(5):876-882.(NI Zhe-ming,MAO Jiang-hong,PAN Guo-xiang,XU Qian,LI Xiao-nian.Mechanism of palladium-catalyzed methanol decomposition for hydrogen production[J].Acta Phys-Chim Sin,2009,25(5):876-882.)
    [13]WANG G C,ZHOU Y H,MORIKAWA Y,NAKAMURA J,CAI Z S,ZHAO X Z.Kinetic mechanism of methanol decomposition on Ni(111)surface:A theoretical study[J].Phys Chem B,2005,109(25):12431-12442.
    [14]GREELEY J,MAVRIKAKIS M.Methanol decomposition on Cu(111):A DFT study[J].J Catal,2002,208(2):291-300.
    [15]陈红梅,朱玉雷,丁国强,郑洪岩,李永旺.草酸二甲酯气相催化加氢合成乙二醇的研究[J].燃料化学学报,2011,39(7):519-526.(CHEN Hong-mei,ZHU Yu-lei,DING Guo-qiang,ZHENG Hong-yan,LI Yong-wang.Study on hydrogenation of dimethyl oxalate to ethylene glycol[J].J Fuel Chem Technol,2011,39(7):519-526.)
    [16]HUANG Z W,LIU H L,CUI F,ZUO J L,CHEN J,XIA C G.Effects of the precipitation agents and rare earth additives on the structure and catalytic performance in glycerol hydrogenolysis of Cu/Si O2catalysts prepared by precipitation-gel method[J].Catal Today,2014,234(4):223-232.
    [17]JI D H,LIU G,JIA M J,ZHANG W X,WANG G J,WU T H,WANG Z L.Studies on dehydrogenation of 2-butanol over supported copper catalysts prepared by sol-gel and impregnation methods[J].Chem J Chin Univ,2007,28(8):1543-1546.
    [18]CHEN L F,GUO P J,QIAO M H,YAN S R,LI H X,SHEN W,XU H L,FAN K N.Cu/Si O2catalysts prepared by the ammoniaevaporation method:Texture,structure,and catalytic performance in hydrogenation of dimethyl oxalate to ethylene glycol[J].J Catal,2008,257(1):172-180.
    [19]WANG Z Q,XU Z N,PENG S Y,ZHANG M J,LU G,CHEN Q S,CHEN Y M,GUO G C.High-performance and long-lived Cu/Si O2nanocatalyst for CO2hydrogenation[J].ACS Catal,2015,5(7):4255-4259.
    [20]GONG J L,YUE H R,ZHAO Y J,ZHAO S,ZHAO L,LV J,WANG S P,MA X B.Synthesis of ethanol via syngas on Cu/Si O2catalysts w ith balanced Cu0-Cu+sites[J].J Am Chem Soc,2012,134(34):13922-13925.
    [21]ZHAO S,YUE H R,ZHAO Y J,WANG B,GENG Y C,LV J,WANG S P,GONG J L,MA X B.Chemoselective synthesis of ethanol via hydrogenation of dimethyl oxalate on Cu/Si O2:Enhanced stability with boron dopant[J].J Catal,2013,297(1):142-150.
    [22]ZHANG C C,WANG D H,ZHU M Y,YU F,DAI B.Effect of different nano-sized silica sols as supports on the structure and properties of Cu/Si O2for hydrogenation of dimethyl oxalate[J].Catalysts,2017,7(3):75.
    [23]DONG X H,MA X G,XU H Y,GE Q J.Comparative study of silica-supported copper catalysts prepared by different methods:Formation and transition of copper phyllosilicate[J].Catal Sci Technol,2016,6(12):4151-4158.
    [24]HUANG Z W,CUI F,XUE J J,ZUO J L,CHEN J,XIA C G.Cu/Si O2catalysts prepared by hom-and heterogeneous depositionprecipitation methods:Texture,structure,and catalytic performance in the hydrogenolysis of glycerol to 1,2-propanediol[J].Catal Today,2012,183(1):42-51.
    [25]王新雷,马奎,郭丽红,丁彤,程庆鹏,田野,李新刚.蒸氨法制备铜硅催化剂的二甲醚水蒸气重整制氢性能[J].物理化学学报,2017,33(8):1699-1708.(WANG Xin-lei,MA Kui,GUO Li-hong,DING Tong,CHENG Qing-peng,TIAN Ye,LI Xin-gang.Catalytic performance for hydrogen production through steam reforming of dimethyl ether over silica supported copper catalysts synthesized by ammonia evaporation method[J].Acta Phys-Chim Sin,2017,33(8):1699-1708.)
    [26]邱坤赞,郭文文,王海霞,朱玲君,王树荣.Cu/Si O2催化剂结构对乙酸甲酯加氢性能的影响[J].物理化学学报,2015,31(6):1129-1136.(QIU Kun-zan,GUO Wen-wen,WANG Hai-xia,ZHU Ling-jun,WANG Shu-rong.Influence of catalyst structure on performance of Cu/Si O2in hydrogenation of methyl acetate[J].Acta Phys-Chim Sin,2015,31(6):1129-1136.)
    [27]LI F J,WANG L G,HAN X,CAO Y,HE P,LI H Q.Selective hydrogenation of ethylene carbonate to methanol and ethylene glycol over Cu/Si O2catalysts prepared by ammonia evaporation method[J].Int J Hydrogen Energy,2017,42(4):2144-2156.
    [28]GHODSELAHI T,VESAGHI M A,SHAFIEKHANI A,BAGHIZADEH A,LAMEII M.XPS study of the Cu@Cu2O core-shell nanoparticles[J].Appl Surf Sci,2008,255(5):2730-2734.
    [29]YU X,ZHAI S B,ZHU W C,GAO S,YAN J B,YUAN H J,CHEN L L,LUO J,ZHANG W X,WANG Z L.The direct transformation of ethanol to ethyl acetate over Cu/Si O2catalysts that contain copper phyllosilicate[J].J Chem Sci,2014,126(4):1013-1020.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700