Catalyst deactivation in CVD synthesis of carbon nanotubes

被引:90
作者
Kuwana, K
Endo, H
Saito, K
Qian, DL
Andrews, R
Grulke, EA
机构
[1] Univ Kentucky, Dept Mech Engn, Lexington, KY 40506 USA
[2] Univ Kentucky, Ctr Appl Energy Res, Lexington, KY 40511 USA
[3] Univ Kentucky, Dept Chem & Mat Engn, Lexington, KY 40506 USA
基金
美国国家科学基金会;
关键词
carbon nanotubes; chemical vapor deposition; modeling; carbon yield; catalytic properties;
D O I
10.1016/j.carbon.2004.09.008
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A computational fluid dynamics (CFD) model with multistep chemical reactions was applied to predict the yield of multiwalled carbon nanotubes produced from our xylene-based chemical vapor deposition (CVD) reactor. Two-step xylene decomposition in the gas phase and catalytic decomposition of hydrocarbons to nanotubes on the growth surfaces were adopted based on exhaust-gas composition measurements. Using the experimentally obtained exhaust-gas concentrations, we conducted inverse calculations to determine apparent rate constants of the catalytic surface reactions. During the CVD process, catalyst deactivation was observed probably due to carbon formation on the catalyst surface. Its effect on the apparent rate constant was empirically correlated with a simple exponential equation. Applying the CFD model, we predicted the local yielding rate of nanotubes along the axis of the reactor. The total yield was then computed by integrating the local yielding rate over the growth surfaces and compared favorably (similar to95%) with the experimental results. The proposed model is expected to help researchers optimize the process parameters to achieve the maximum nanotube yield. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:253 / 260
页数:8
相关论文
共 15 条
[1]   Continuous production of aligned carbon nanotubes: a step closer to commercial realization [J].
Andrews, R ;
Jacques, D ;
Rao, AM ;
Derbyshire, F ;
Qian, D ;
Fan, X ;
Dickey, EC ;
Chen, J .
CHEMICAL PHYSICS LETTERS, 1999, 303 (5-6) :467-474
[2]   KINETICS AND MECHANISM OF HYDROGENOLYSES . ADDITION OF HYDROGEN ATOMS TO PROPYLENE TOLUENE AND XYLENE [J].
BENSON, SW ;
SHAW, R .
JOURNAL OF CHEMICAL PHYSICS, 1967, 47 (10) :4052-&
[3]   REACTIVITY OF THE 1ST TRANSITION ROW METALLOCENES IN THERMAL-DECOMPOSITION REACTION [J].
DYAGILEVA, LM ;
MARIN, VP ;
TSYGANOVA, EI .
JOURNAL OF ORGANOMETALLIC CHEMISTRY, 1979, 175 (01) :63-72
[4]   CFD prediction of carbon nanotube production rate in a CVD reactor [J].
Endo, H ;
Kuwana, K ;
Saito, K ;
Qian, D ;
Andrews, R ;
Grulke, EA .
CHEMICAL PHYSICS LETTERS, 2004, 387 (4-6) :307-311
[5]   Flame synthesis of single-walled carbon nanotubes [J].
Height, MJ ;
Howard, JB ;
Tester, JW ;
Sande, JBV .
CARBON, 2004, 42 (11) :2295-2307
[6]   PREPARATION OF VAPOR-GROWN CARBON-FIBERS IN STRAIGHT FORM BY FLOATING CATALYST METHOD IN LINZ-DONAWITZ CONVERTER GAS [J].
ISHIOKA, M ;
OKADA, T ;
MATSUBARA, K .
CARBON, 1993, 31 (01) :123-127
[7]  
Kuwana K, 2002, MATER RES SOC SYMP P, V706, P61
[8]   BOND-DISSOCIATION ENERGIES IN FERROCENE [J].
LEWIS, KE ;
SMITH, GP .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1984, 106 (16) :4650-4651
[9]   Catalyst deactivation: is it predictable? What to do? [J].
Moulijn, JA ;
van Diepen, AE ;
Kapteijn, F .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :3-16
[10]  
Poling B. E., 2001, PROPERTIES GASES LIQ