无机材料学报 ›› 2014, Vol. 29 ›› Issue (7): 687-694.DOI: 10.3724/SP.J.1077.2014.13494 CSTR: 32189.14.SP.J.1077.2014.13494
徐 润1, 李忻达1, 李志强1, 赵仁宇1, 范根莲1, 熊定邦1, 唐 婕1, 许 勇2, 张 荻1
收稿日期:2013-09-29
修回日期:2013-12-25
出版日期:2014-07-20
网络出版日期:2014-06-20
作者简介:徐 润(1991-), 男, 博士研究生. E-mail: x.r.my.mail@gmail.com
基金资助:XU Run1, LI Xin-Da1, LI Zhi-Qiang1, ZHAO Ren-Yu1, FAN Gen-Lian1, XIONG Ding-Bang1, TANG Jie1, XU Yong2, ZHANG Di1
Received:2013-09-29
Revised:2013-12-25
Published:2014-07-20
Online:2014-06-20
About author:XU Run. E-mail: x.r.my.mail@gmail.com
Supported by:摘要:
采用聚合物热解化学气相沉积(PP-CVD)法, 通过聚乙二醇(PEG)的原位热解提供碳源、柠檬酸(CA)和硝酸钴反应产生催化剂纳米粒子, 在微纳米级的片状铝粉基底上原位生长碳纳米管(CNTs)。通过实验和反应动力学建模研究了PP-CVD反应机理, 揭示了PEG热解气相成分和催化剂纳米粒子表面气-固反应对CNTs生长速率的影响规律。CO初始分压和反应温度提高, CNTs生长速率提高; H2初始分压和催化剂密度提高, CNTs生长速率降低。模型预测的CNTs平均长度随反应温度和反应时间的变化趋势符合实验结果。因此, 本研究为进一步优化CNTs/铝复合粉末制备工艺提供了新的理论依据。
中图分类号:
徐 润, 李忻达, 李志强, 赵仁宇, 范根莲, 熊定邦, 唐 婕, 许 勇, 张 荻. 聚合物热解法制备碳纳米管/铝复合粉末及其反应动力学研究[J]. 无机材料学报, 2014, 29(7): 687-694.
XU Run, LI Xin-Da, LI Zhi-Qiang, ZHAO Ren-Yu, FAN Gen-Lian, XIONG Ding-Bang, TANG Jie, XU Yong, ZHANG Di. Preparation and Reaction Kinetics of Carbon Nanotubes/Aluminum Composite Powders Using Polymer Pyrolysis Method[J]. Journal of Inorganic Materials, 2014, 29(7): 687-694.
图1 PP-CVD生长CNTs示意图
Fig. 1 Schematic drawing of CNTs grown by PP-CVD (a) The temperature and pressure monitoring system; (b) The closed batch reactor; (c) Al nanoflakes with Co nanoparticles and CNTs as grown; (d) The gas-solid reaction pathway and tip growth mode of CNTs. The dashed arrows represent collision of gaseous species and the solid arrows represent surface diffusion of carbon atoms around the Co nanoparticle
| Symbols | Definition |
|---|---|
| Cp | Encapsulating carbon |
| (S) | Surface species |
| C(S) | Active carbon atom |
| | The forward (f ) reaction rate constant of the i th reaction |
| | The reverse (r) reaction rate constant of the i th reaction |
| A | The Arrhenius pre-exponential factor |
| | The Arrhenius temperature coefficient |
| Ei | The activation energy of the i th reaction |
| R | The universal gas constant |
| | The change in the Gibbs free energy of formation as a result of the reaction |
| | The net stoichiometric coefficient for species j in i th reaction |
| qi | The rate of progress of the i th reaction |
| Rj | The net rate of production of species j |
| Cj | The volumetric concentration of species j |
| Vdeposited | The volume of deposited carbon atoms |
| | The volume of encapsulating carbon |
| VC | The volume of a carbon atom |
| | The density of Co nanoparticles |
| | CNTs growth rate |
| d | The diameter of Co nanoparticles |
| NA | Avogadro constant |
| Do | The surface diffusion coefficient of carbon atoms |
表1 模型中使用的符号定义
Table 1 Nomenclature of the symbols used in the modeling
| Symbols | Definition |
|---|---|
| Cp | Encapsulating carbon |
| (S) | Surface species |
| C(S) | Active carbon atom |
| | The forward (f ) reaction rate constant of the i th reaction |
| | The reverse (r) reaction rate constant of the i th reaction |
| A | The Arrhenius pre-exponential factor |
| | The Arrhenius temperature coefficient |
| Ei | The activation energy of the i th reaction |
| R | The universal gas constant |
| | The change in the Gibbs free energy of formation as a result of the reaction |
| | The net stoichiometric coefficient for species j in i th reaction |
| qi | The rate of progress of the i th reaction |
| Rj | The net rate of production of species j |
| Cj | The volumetric concentration of species j |
| Vdeposited | The volume of deposited carbon atoms |
| | The volume of encapsulating carbon |
| VC | The volume of a carbon atom |
| | The density of Co nanoparticles |
| | CNTs growth rate |
| d | The diameter of Co nanoparticles |
| NA | Avogadro constant |
| Do | The surface diffusion coefficient of carbon atoms |
| The initial pressure /(1.013×105, Pa) | The initial partial pressure /(1.013×105, Pa) | ||||
|---|---|---|---|---|---|
| CH4 | CO | CO2 | H2O | H2 | |
| 22 | 1.61 | 6.24 | 6.18 | 5.65 | 1.53 |
表2 密闭反应器中PEG-CA-Co(II)热解气体组成
Table 2 Composition of the PEG-CA-Co(II) pyrolysis gases in the batch reactor
| The initial pressure /(1.013×105, Pa) | The initial partial pressure /(1.013×105, Pa) | ||||
|---|---|---|---|---|---|
| CH4 | CO | CO2 | H2O | H2 | |
| 22 | 1.61 | 6.24 | 6.18 | 5.65 | 1.53 |
| Species | CH4 | CO | CO2 |
|---|---|---|---|
| Projected areaa | 2.43×10-2 | 2.01×10-2 | 3.45×10-2 |
| Ratiob | 3656 | 4388 | 2531 |
| Active site density c | 1.72×10-9 | 2.06×10-9 | 1.19×10-9 |
Table 3 The ratio of Co nanoparticle surface area to the projected area of carbon source gas molecules
| Species | CH4 | CO | CO2 |
|---|---|---|---|
| Projected areaa | 2.43×10-2 | 2.01×10-2 | 3.45×10-2 |
| Ratiob | 3656 | 4388 | 2531 |
| Active site density c | 1.72×10-9 | 2.06×10-9 | 1.19×10-9 |
图3 不同尺度下的CNTs形貌
Fig. 3 Morphologies of CNTs at different scales (a) SEM image of the Al flake substrates; (b) SEM image of the CNTs; (c) TEM image of the CNTs; (d) HRTEM image of the CNTs and SEAD pattern of catalyst particle
图4 模型中各项变量对于CNTs生长速率的影响(60 min内)
Fig.4 Effects of different vatiables in the modeling on the CNT growth rates in 60 min (a) Partial pressure of CO; (b) Partial pressure of H2; (c) Co nanoparticles density; (c) Reaction temperature
图6 在873 K反应(a)0 min、(b)30 min、(c)60 min后CNTs的SEM形貌和长度分布以及(d)不同反应时间CNTs/Al复合粉末的拉曼光谱
Fig.6 SEM images with length and normalized frequency statistic (inset) of the CNTs after grown at 873 K for (a) 0 min, (b) 30 min and (c) 60 min. (d) Raman spectra of the CNT/Al composite powders The lengths of CNTs were measured on the corresponding SEM images randomly, and 120 CNTs were counted at each reaction time
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