Experimental study on catalytic decomposition of simulated biogas for carbon nanotubes
WANG Dong-dong;XIE Hao;PIAO Gui-lin;ZHANG Ju-bing;CHEN Li-fang(School of Energy and Mechanical Engineering;
Abstract:
Using 96 percent Ni-based catalyst,prepared carbon nanotubes(CNTs) by simulating biogas catalytic decomposition.The effects of gas component,temperature and CO2 concentration on catalytic decomposition were investigated in moving-bed.The results show that,carbon deposition rate of catalyst with CH4/CO2 is much lower than that of CH4/N2 from 500 ℃ to 680 ℃ because of carbon elimination activity from CO2,the influence is eliminated when reaction temperature is between 680 ℃ and 900 ℃.With the increase of CO2 concentration,carbon deposition rate decrease gradually.For simulated biogas(60 percent CH4,40 percent CO2),the most suitable decomposition temperature is 650 ℃,carbon deposition rate reaches 215.2 percent.The samples are characterized by SEM and TEM,the carbon nanotubes gained by CH4/CO2 and CH4/N2 are essentially similar.It is beneficial for improving the service life of catalyst,producing higher purity carbon nano material under low temperature condition.
Key Words: simulated methane;Ni-based catalyst;carbon nanotubes;catalytic cracking
Foundation: 江苏省自然科学基金资助项目(BK2012851)
Author: WANG Dong-dong;XIE Hao;PIAO Gui-lin;ZHANG Ju-bing;CHEN Li-fang(School of Energy and Mechanical Engineering;
DOI: 10.13226/j.issn.1006-6772.2013.02.005
References:
- [1]杨德敏.活性炭催化分解甲烷制氢研究进展[J].洁净煤技术,2010,16(2):84-88.
- [2]Marban G,Valdes-Solis T.Towards the hydrogeneconomy[J].Int J Hydrogen Energy,2007,32(12):1625-1637.
- [3]S Paul,S K Samdarshi.A green precursor for carbonnanotube synthesis[J].New Carbon Materials,2011,26(2):85-88.
- [4]李峰,白朔,成会明.纳米碳管及其应用[J].燃料化学学报,2001,29(1):95-96.
- [5]康利荣,张建民,连辉.天然气-煤集成共转化制备合成气新工艺[J].洁净煤技术,2006,12(4):22-26.
- [6]刘少文,叶志华,梁罚,等.流化床中甲烷裂解制氢与催化剂再生过程研究[J].燃料化学学报,2006,34(5):567-571.
- [7]Iijima S.Helical Microtubules of graphitic carbon[J].Nature,1991(354):56-58.
- [8]S D Robertson.Graphite formation from low temperaturepyrolysis of methane over some transition metal surfaces[J].Nature,1969(221):1044-1046.
- [9]刘颖,王浩静,周公立,等.热等离子体裂解天然气研究进展[J].天然气化工,2003(1):31-34.
- [10]Bjom Gaudemack,Steinar Lynum.Hydrogen from naturalgas without release of CO2 to the atmosphere[J].Int JHydrogen Energy,1998,23(12):1087-1093.
- [11]Lewandowski A.Performance characterization of theSERI high-flux solar furnace[J].Solar EnergyMarterials,1991,24(1-4):550-663.
- [12]Dahl J K,Buechler K J,Finley R,et al.Rapid solar-thermal dissociation of natural gas in an aerosol flow re-actor[J].Energy,2004,29(5):715-725.
- [13]Kogan M,Kogan A.Production of hydrogen and carbonby solar thermal methane splitting.I.The unseededreactor[J].International Journal of Hydrogen Energy,2003,28(11):1187-1198.
- [14]Ermakova M A,Ermakov D Y.Ni/SiO2 and Fe/SiO2catalysts for production of hydrogen and filamentous car-bon via methane decomposition[J].Catalysis Today,2002,77(3):225-235.
- [15]Koerts T,Declen M.J.A.G,Santen R.A.Hydrogen for-mation from methane by a low-temperature two-step re-action sequence[J].Journal of Catalysis,1992,138(1):101-104.
- [16]吴国涛,朱光明,尤金跨,等.催化裂解CH4制备不同形貌的碳纳米管[J].高等学校化学学报,2002,23(1):98-101.
- [17]崔一尘,杨旸,蔡宁,等.甲烷在活性炭上催化裂解的热重分析[J].燃料科学与技术,2005,11(5):480-485.
- [18]Suelves I,Lázaro M J,Moliner R,et al.Hydrogen pro-duction by thermo catalytic decomposition of methane onNi-based catalysts:influence of operating conditions oncatalyst deactivation and carbon characteristics[J].In-ternational Journal of Hydrogen Energy,2005,30(15):1555-1567.
- [19]惠战强.硝酸镍催化裂解制备碳纳米管[J].激光杂志,2008,29(4):65-69.
- [20]徐泽夕,吴晋沪,王洋,等.甲烷在褐煤煤焦上的裂解反应研究[J].燃料化学学报,2009,37(3):277-281.
- WANG Dong-dong
- XIE Hao
- PIAO Gui-lin
- ZHANG Ju-bing
- CHEN Li-fang(School of Energy and Mechanical Engineering
- Nanjing Normal University
- Nanjing 210042
- China)
- WANG Dong-dong
- XIE Hao
- PIAO Gui-lin
- ZHANG Ju-bing
- CHEN Li-fang(School of Energy and Mechanical Engineering
- Nanjing Normal University
- Nanjing 210042
- China)