INSTITUTE OF PHYSICS PUBLISHING NANOTECHNOLOGY Nanotechnology 16 (2005) 532–535 doi:10.1088/0957-4484/16/4/033 Effect of temperature, pressure, and gas ratio of methane to hydrogen on the synthesis of double-walled carbon nanotubes by chemical vapour deposition G Y Xiong1 , Y Suda2 , D Z Wang1 , J Y Huang1 and Z F Ren1,3 1 Department of Physics, Boston College, Chestnut Hill, MA 02467, USA Division of Electronics and Information Engineering, Graduate School of Engineering, Hokkaido University, Sapporo 060-8628, Japan 2 E-mail: [email protected] Received 5 November 2004, in final form 23 December 2004 Published 21 February 2005 Online at stacks.iop.org/Nano/16/532 Abstract Double-walled carbon nanotubes (DWCNTs) were synthesized by chemical vapour deposition using Fe–Mo catalyst supported on magnesium oxide particles. A mixture of gases of methane and hydrogen was used for the growth. The effect of gas pressure, ratio of methane to hydrogen, and growth temperature on the structure, purity, and yield of DWCNTs has been studied in detail. Transmission electron microscope studies revealed that the growth temperature is the crucial factor determining the size of the catalyst particles. Scanning electron microscope studies were also carried out to provide information on the purity and diameter of DWCNTs synthesized under various conditions. 1. Introduction Ever since the first observation of double-walled carbon nanotubes (DWCNTs) [1], they have received great attention because of their unique structure [2–4] and promising applications in microelectronic devices such as field emitters [5]. In this report, the chemical vapour deposition (CVD) method has been employed to synthesize DWCNTs on Fe–Mo catalyst [6] supported on magnesium oxide (MgO) particles. Many growth conditions affect the CVD growth of carbon nanotubes (CNTs). Among them, the growth temperature, gas pressure, and ratio of the carbon source gas to the carrying gas are the most important factors in determining the structure, purity, and yield of multi-walled carbon nanotubes [7, 8]. In the present report, we have studied how these three factors affect the growth of DWCNTs. 2. Experimental details The experiments were carried out in a horizontal tube furnace with a quartz tube of 2 inch diameter. The catalyst used 3 Author to whom any correspondence should be addressed. 0957-4484/05/040532+04$30.00 © 2005 IOP Publishing Ltd in this study is Fe–Mo nanoparticles supported on MgO particles. MgO powders are used as catalyst support because they have a relatively large surface area and are porous [9]. To load the Fe–Mo catalyst onto the MgO powder, first, a certain amount of iron sulfate heptahydrate (FeSO4 ·7H2 O) was dissolved in 100 ml distilled water by magnetic stirring for about 30 min, then a certain amount of ammonium molybdate ((NH4 )6 Mo7 O24 ·7H2 O) was added, and the mixture was stirred for 2 h. Second, MgO powder was immersed in the solution by sonicating for 30 min and then stirred for 3 h to form a uniform suspension. Third, the suspension was continuously stirred and dried at 80 ◦ C on a heated plate until the water was completely vaporized, followed by baking at 130 ◦ C for 15 h to eliminate any remaining moisture. Finally, the dried bulk catalyst was ground into fine powder in a mortar. The final catalyst has a planned atomic ratio of Fe/Co/MgO = 5:1:60. For DWCNT growth, a two-step procedure was used. After the catalyst (100 mg) was spread onto a Mo boat, it was first reduced at 820–900 ◦ C for 10 min in flowing gas of H2 (100 sccm) at a pressure of 100 Torr to generate Fe–Mo nanoparticles on the supporting MgO particles, immediately followed by growth at 820–900 ◦ C for 1 h in flowing gases of Printed in the UK 532 Effect of temperature, pressure, and gas ratio of methane to hydrogen on the synthesis of DWCNTs by CVD Scanning electron microscopes (SEM, JEOL JSM-6340F and JEOL JSM-7400F) and a transmission electron microscope (TEM, JEOL 2010F) were used to characterize the catalyst and CNTs. 3. Results and discussion Figure 1. High-magnification backscattering SEM image of Fe–Mo catalyst supported on MgO (reduced at 860 ◦ C for 10 min with flowing 100 sccm H2 gas at 100 Torr) to show the distribution of Fe–Mo nanoparticles. The bright spots represent nanosized Fe–Mo particles, whereas the background is porous MgO particles. H2 and CH4 with different ratios at various pressures of 60– 120 Torr. The amount of product (defined as the net weight gain divided by the sum of the remaining catalyst and MgO support) was carefully monitored with the growth conditions. Figure 1 shows the backscattering SEM image of the Fe– Mo catalyst reduced at 860 ◦ C for 10 min with flowing 100 sccm H2 gas at 100 Torr. The background is porous MgO particles. The bright spots represent nanosized Fe–Mo particles in the range of 2–10 nm measured under TEM in an independent experiment. It is clearly shown that after the reduction procedure lots of nanoparticles (bright spots) were generated and distributed fairly uniformly on the supporting MgO particles. To study the effect of growth temperature on catalyst particle formation, we preformed several growths without supplying carbon-containing gas. Figures 2(a)–(c) show the TEM images of the catalysts reduced at temperatures of 820, 860, and 900 ◦ C for 10 min with flowing 100 sccm H2 gas at 100 Torr, respectively. Clearly, at 820 ◦ C the Fe– Mo particles were just starting to form (figure 2(a)). At 860 ◦ C, lots of nanosized (2–5 nm) catalyst particles were formed (figure 2(b)). At 900 ◦ C, nanosized catalyst Fe–Mo particles have agglomerated into relatively large (8–10 nm) Figure 2. TEM images of Fe–Mo catalyst on MgO after being reduced at 820 ◦ C (a), 860 ◦ C (b), and 900 ◦ C (c) for 10 min with flowing 100 sccm H2 gas at 100 Torr. 533 G Y Xiong et al Figure 3. The amount of product as a function of growth temperature with different gas pressures of 60 Torr (), 80 Torr ( ), 100 Torr (), and 120 Torr ( ). • particles (figure 2(c)). It is well known that the size of catalyst particles decides the diameter of CNTs [1, 10–12]. Using TEM we demonstrated that the same diameter controlling mechanism works: growth temperature affects the diameter of the grown CNTs. It was found that the optimal growth temperature for the present catalyst is about 860 ◦ C based on the CNT diameter and amount of product. Figure 3 shows the amount of product at different growth temperatures and gas pressures with a fixed flowing gas of CH4 (300 sccm)/H2 (6 sccm). It is clear that higher growth temperature results in higher amount of product. The same is true for the gas pressure. The parameters including growth temperature, gas pressure, and ratio of methane to hydrogen not only have great effects on the amount of product, but also on the structure and purity of DWCNTs. There were few DWCNTs when the temperature was lower than 800 ◦ C, where the weight gain (figure 3) is mostly amorphous carbon. When the temperature was higher than 900 ◦ C, there were few DWCNTs too. At high temperature, the main part of the weight increment is amorphous and other forms of crystalline carbon. In general, during the growth, methane molecules decompose at the catalyst particles’ surface, with carbon dissolving into the catalyst particles; the dissolved carbon atoms diffuse either on the surface or through the bulk of the Fe–Mo particles upon supersaturation. The DWCNTs are then formed by precipitation of carbon atoms on the other side of the catalyst particle [13–16]. When the concentration of methane is too high, meaning more carbon source is provided than is needed, the decomposition rate of the carbon source is higher than the precipitating rate of carbon, which results in oversupply of carbon in the form of amorphous and/or crystalline carbon. In our experiment, the gas pressure inside the chamber determines the concentration of methane. Our result proves that higher gas pressure leads to abundant amorphous carbon, which is illustrated in the weight increment as shown in figure 3. 534 Figure 4. SEM images of DWCNTs grown at 860 ◦ C and 100 Torr with various ratios of hydrogen to methane. The ratio is (a) 0 sccm H2 and 300 sccm CH4 , (b) 6 sccm H2 and 300 sccm CH4 , and (c) 12 sccm H2 and 300 sccm CH4 . With TEM studies, we found a rapid increase of amorphous carbon when the gas pressure exceeds 100 Torr. With the temperature fixed at 860 ◦ C and pressure at 100 Torr, different combinations of methane to hydrogen (300/0, 300/6, and 300/12) were studied to see how this affects the growth of DWCNTs. Figure 4 shows the SEM images of DWCNTs grown at different ratios of methane to hydrogen. It is clearly shown that the concentration of hydrogen obviously affects DWCNT growth. There were few DWCNTs when 300 sccm methane without any hydrogen was used (figure 4(a)), but lots of DWCNTs when 300 sccm methane and 6 sccm hydrogen were supplied (figure 4(b)). When the hydrogen flow was increased to 12 sccm, the DWCNT growth (figure 4(c)) turns out to be less than that in figure 4(b). After growth we checked the samples using high resolution TEM. Figure 5(a) shows a bundle of CNTs grown at the optimal conditions of 860 ◦ C, 100 Torr, and 300/6 sccm (CH4 /H2 ). Figures 5(b) and (c) are the enlarged areas indicated in figure 5(a). It is clearly shown that most of the CNTs are DWCNTs. Effect of temperature, pressure, and gas ratio of methane to hydrogen on the synthesis of DWCNTs by CVD carbon nanotubes, mainly three- and/or four-walled CNTs. Our explanation here is that hydrogen acts as ‘the promoter of the catalyst’. Hydrogen helps to keep the activity of the Fe– Mo catalyst during the growth. When there is no hydrogen, the catalyst loses activity rapidly and few DWCNTs grow. With hydrogen being supplied, the catalyst keeps active so that the decomposition, diffusion, and precipitation of carbon atoms work smoothly. 4. Conclusions In summary, we have demonstrated how the growth parameters affect the synthesis of DWCNTs using the CVD method. The catalyst reducing temperature determines the average size of the final CNTs. The gas pressure and growth temperature dictate the purity and amount of product. The hydrogen concentration determines the final structure of the product. Acknowledgments The work is supported by NSF NIRT 0304506 and by DOE DE-FG02-00ER45805. References Figure 5. (a) TEM images of an as-synthesized DWCNT bundle, (b) HRTEM image of a bundle of two DWCNTs, and (c) HRTEM image of a bundle of a few DWCNTs. Under TEM and high magnification SEM, we observed that the diameter of DWCNTs increased when the concentration of hydrogen increased. 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