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Journal of Nanomaterials
Volume 2013 (2013), Article ID 836281, 9 pages
Chlorination of Carbon Nanotubes Obtained on the Different Metal Catalysts
1Institute of Chemical and Environmental Engineering, West Pomeranian University of Technology in Szczecin, Pułaskiego 10, 70-310 Szczecin, Poland
2Institute of Organic Chemical Technology, West Pomeranian University of Technology in Szczecin, Pułaskiego 10, 70-310 Szczecin, Poland
3Institute of Physics, Polish Academy of Sciences, Al. Lotnikow 32/46, 02-668 Warsaw, Poland
Received 10 October 2013; Accepted 29 November 2013
Academic Editor: Chunyi Zhi
Copyright © 2013 Iwona Pełech et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
In this paper, a chlorination method is proposed for simultaneous purification and functionalization of carbon nanotubes, thus increasing their ability to use. Carbon nanotubes were obtained by CVD method through ethylene decomposition on the nanocrystalline iron or cobalt or bimetallic iron-cobalt catalysts. The effects of temperature (50, 250, and 450°C) in the case of carbon nanotubes obtained on the Fe-Co catalyst and type of catalyst (Fe, Co, Fe/Co) on the effectiveness of the treatment and functionalization were tested. The phase composition of the samples was determined using the X-ray diffraction method. The quantitative analysis of metal impurity content was validated by means of the thermogravimetric analysis. Using X-ray Photoelectron Spectroscopy (XPS), Energy Dispersive Spectroscopy (EDS) analysis, and also Mohr titration method, the presence of chlorine species on the surface of chlorinated samples was confirmed.
Carbon nanotubes (CNTs), since their discovery in 1991, constantly incite an immense interest owing to their special physical and chemical properties. Due to unique mechanical, thermal, and electrical properties, these materials are not only an ideal candidate for many applications but also a very interesting material from a scientific point of view. Concerning industrial applications carbon nanotubes can be used, for example, as electron emitters, filtration membranes, drug carriers, energy containers, or catalyst supports [1–6]. A particular interest is connected with the application of carbon nanotubes as fillers for polymers. The presence of carbon nanotubes as an additive to a polymer can improve such properties of the composite such as tensile strength , tensile modulus , toughness , glass transition temperature , thermal conductivity , resistance to solvents , optical properties , and electrical conductivity .
The main bottleneck in the application of carbon nanotubes as fillers for polymers is their insufficient dispersion in a polymer matrix, because CNTs have a tendency to agglomerate due to the Van der Waals forces. Recently there are several methods improving the dispersion of carbon nanotubes in a polymer matrix. One of the very promising methods preventing an aggregation of nanotubes and facilitating a good dispersion in a polymer matrix is their chemical functionalization, involving changes of the surface of nanotubes through an addition of various functional groups.
The most popular method of carbon nanotubes functionalization is their oxidation using oxygen [15, 16] or KMnO4, H2O2, or O3 [17, 18]. To oxidize carbon nanotubes, it is also possible to apply strong acids in liquid environment, as, for example, HNO3, HClO4, H2SO4 + K2Cr2O7, or H2SO4 + KMnO4 [19–21]. Such reactions can cause an addition of many functional groups, as, for example, of carboxyl, alcohols, ketones, or esters (–COOH, –OH, >C=O, or –COO–, resp.) to the external walls of tubes. It should be highlighted that hydroxyl or carboxyl groups are often used as precursors for further reactions of silanisation , esterification , or alkylation and arylation .
Functionalization of carbon nanotubes can be also conducted using other ways as, for example, fluorination, chlorination, or attachment of compounds with longer chains. Fluorination of nanotubes involves the attachment of fluorine to the carbon structure which improves the solubility of carbon nanotubes in polar solvents, for example, alcohols, resulting in the creation of hydrogen bond between the molecule of attached fluorine and the molecule of alcohol . To chemically attach fluorine to the tubes, various sources of fluorine can be applied, as atomic fluorine, gaseous fluorine and inorganic fluorides, as BrF3 or XeF2 [25, 26]. The attachment of the fluorine molecule enables in further reactions (similarly as in the case of other functional groups) the replacement of fluorine with more complicated substituents. The covalent bond of fluorine can be replaced by, for example, alkyl group through an alkylation reaction . The reactants in this reaction can be alkylolite or reactants of the Grignard reaction, for example, RMgX (where R—alkyl group, X—Cl, or Br, I).
An alternative method of carbon nanotubes functionalization is their chlorination. Chlorine applied in the functionalization of carbon nanotubes can originate from liquid precursors as thionyl chloride, chloroform, trichloromethane, tetrachloroethylene , or hydrochloric acid  or solid as dichlorocarbene  or gaseous precursors as Cl2 . In the result of the chlorination reaction the following groups can be attached to the external walls of carbon nanotubes: –CCl2, –CCl, or –COCl .
In this paper, modification of carbon nanotubes obtained on the iron, cobalt, and bimetallic iron/cobalt catalyst using chlorination method in the gas phase is presented. Chlorination reaction is very interesting and promising because it may be an intermediate stage that allows for the subsequent fixation of more complex functional groups. The effect of the temperature on the modification of carbon nanotubes obtained on the iron-cobalt catalyst and the influence of chlorination treatment on the removal of iron, cobalt, and iron-cobalt particles as well as on the attachment of functional groups were investigated. The amount of chlorine species was confirmed using Energy Dispersive Spectroscopy (EDS) analysis and X-ray photoelectron spectroscopy (XPS). Removal degree of metal particles was determined on the basis of thermogravimetric analysis.
Nanocrystalline iron, cobalt, and iron/cobalt were obtained from cobalt (II) or iron (III) nitrates together with a small amount of calcium and aluminum nitrates. The salts were dissolved in water and 20% NH4OH was added as a precipitating agent continuously, to obtain a pH of 8. Metal hydroxides were precipitated from the solution and the deposit was washed with water, filtered, and dried at 75°C. The next step was calcination at 500°C for 1 h to obtain the precursors of nanocrystalline metals-cobalt and iron oxides with a small amount of structural promoters –CaO and Al2O3. In the last stage of preparation, the precursors of nanocrystalline metals were reduced under hydrogen atmosphere polythermally at the temperature rising from 20°C to 500°C (for cobalt and iron/cobalt oxides) and from 20°C to 600°C for iron oxide. For all catalysts, reduction processes were conducted until the mass was stable for at least 90 min. The details of the catalysts preparation are presented in .
Multiwalled carbon nanotubes (MWCNTs) were obtained by decomposition of ethylene on the nanocrystalline iron, cobalt, and bimetallic iron-cobalt catalyst at 700°C in the high temperature furnace (Carbolite, STF 16/180). The details of carbon nanotubes preparation are presented in .
The chlorination processes were performed in the gas phase for 2 hours. For this purpose, the sample was placed in the furnace and chlorine gas was supplied. Temperature of the process was kept at 50°C, 250°C, or 450°C. After two hours the supply of chlorine was cut off and the sample was cooled to the room temperature under vacuum. In the next stage, the sample was washed with acetone and distilled water several times and dried under vacuum at 120°C.
The raw samples were named as Fe or Co or FeCo and the samples after chlorination as FeCo50Cl, FeCo250Cl, FeCo450Cl, or Fe450Cl, Co450Cl. The number indicates chlorination temperature. For example, FeCo50Cl is carbon material obtained using Fe-Co catalyst and submitted to chlorination at 50°C.
The phase composition of the sample before and after chlorination was determined using the X-ray diffraction method (X’Pert PRO Philips diffractometer), a CuKα radiation. The morphology of carbon nanomaterials was studied using Transmission Electron Microscopy (HRTEM-FEI Tecnai F20). The amount of the catalyst in the samples after chlorination process was determined based on thermogravimetric analysis, which was performed on DTA-Q600 SDT TA Instruments apparatus with the heating rate of 10°C/min from room temperature to 900°C in air. The X-ray photoelectron spectra were obtained using Mg Kα (hν= 1253.6 eV) radiation with an SES 2002 spectrometer operating at constant transmission energy (EP = 50 eV). Chemical composition analysis was performed on the Scanning Electron Microscope Hitachi SU-70 equipped with Thermo EDS system using 15 kV of electron beam accelerating voltage.
3. Results and Discussion
The morphology of the carbon material obtained on the bimetallic iron-cobalt catalyst using ethylene as a carbon source at 700°C was studied using transmission electron microscopy and TEM images are presented in Figures 1(a) and 1(b). It was found that the sample was mainly composed of multi walled carbon nanotubes with diameters in the range from 20 to 40 nm. CNTs were entangled due to the existence of carbon penta- and heptagons rings . Lack of catalyst crystallites on the ends of carbon nanotubes can suggest that their growth could take place according to the root mechanism presented in . TEM images of the carbon materials prepared on the nanocrystalline iron and cobalt catalysts are presented in Figures 1(c) and 1(d), respectively. Carbon filamentous structures were observed in both cases. It was also clearly visible that the diameters of the filaments obtained on the cobalt catalyst were smaller than those obtained on the iron catalyst. Additionally, the bigger particles encapsulated in carbon were observed, which were not active in the carbon nanotubes formation.
Carbon material obtained on the bimetallic iron-cobalt catalyst was submitted to chlorination in the gas phase at 50°C, 250°C, or 450°C. In order to compare the effectiveness of chlorination methods towards the removal of catalyst particles and introduction of functional groups on the carbon nanotubes surface, carbon materials obtained on the iron and cobalt catalyst were also tested.
The preliminary analysis of the samples was done using X-ray diffraction method. The XRD spectra of the raw carbon materials synthesized on the iron/cobalt catalysts (FeCo) and carbon materials after chlorination at 50°C and 450°C (samples FeCo50Cl and FeCo450Cl) are presented in Figure 2. On the basis of the XRD analysis, it was found that the raw carbon sample consisted of graphite and Fe-Co phase. For the samples after chlorination at different temperatures, the phase composition was almost the same. Simultaneously none of ferric chloride or cobalt chloride was detected. Significant changes were observed as for the intensity of the Fe-Co peaks. For the samples after chlorination at 50°C and at 250°C (not show here), the peaks from Fe-Co phase were decreased and at 450°C almost completely disappeared.
The efficiency of the chlorination method conducted at 450°C to the removal of iron and cobalt particles was also examined and X-ray diffraction spectra of the raw and chlorinated samples are presented in Figure 2. In the case of iron sample after synthesis, besides peaks characteristic for the graphite phase, peaks corresponding to iron carbide in the form of cementite were detected. After chlorination, these peaks were not noticed but it cannot be excluded that in the samples small amounts of Fe3C could be present. For the sample obtained on the cobalt catalyst, similar like in the case of iron or iron/cobalt material after synthesis, graphite peaks and additionally small intensity peaks corresponding to cobalt phase were present. Probably in the sample some amount of cobalt oxide also existed.
EDS results presented in Table 1 confirmed that the amount of iron continuously decreased from 2% in the raw sample (FeCo) to 0.3% in the sample chlorinated at 450°C (FeCo450Cl). At moderate temperatures, the values of iron were 1.5% and 1.4% for the sample chlorinated at 50°C (FeCo50Cl) and 250°C (FeCo250Cl), respectively. The amount of cobalt particles in the raw sample (FeCo) was about 1.4% and did not change in the sample after chlorination at 50°C (FeCo50Cl). At 250°C (FeCo250Cl), the amount of cobalt decreased and equalled about 0.7% and for the sample chlorinated at 450°C about 0.9% (FeCo450Cl).
The composition of the samples was also studied by means of XPS analysis. The results of the elemental quantitative analysis of the surface composition are presented in Table 2. In contrast to the EDS results only for samples FeCo50Cl and FeCo250Cl a small amount of iron was detected by XPS analysis. However, it must be kept in mind that XPS information depth reaches only several tens of nanometers from the surface while EDS technique gives the composition for a depth of several μm. Presumably the iron and cobalt particles detected by EDS analysis are covered by a carbon deposit which effectively screens XPS signal of these elements from detection. In the samples treated at 50°C and 250°C, the carbon deposit is supposedly thinner and small quantities of iron can be observed by XPS analysis.
In order to determine the exact amount of metal particles which remained in the samples after the chlorination process, a thermogravimetric analysis was performed. On the basis of thermogravimetric curves (shown in the Figure 3), the percentage content of catalyst, in the samples was calculated and the values are presented in Table 3. For the materials obtained on the iron/cobalt catalyst, it was clearly observed that the increase of chlorination temperature resulted in reducing the catalyst amount in the sample. After chlorination at 50°C, the amount of metal particles equaled about 6.5%. At 250°C, the amount of catalyst particles decrease to 3.5% and at 450°C further decrease of the catalyst amount was observed. In this sample, only 2.9% of catalyst particles was noticed. The best results were achieved for the iron material chlorinated at 450°C. Only about 0.2% of metal particles remained in the sample. The most difficult to remove was cobalt catalyst and about 8.1% of these particles was still present in the sample after chlorination process.
TG curves clearly show that the chlorinated material obtained on the iron catalyst burned at higher temperature while the chlorinated samples prepared on the cobalt and iron/cobalt catalyst burned at lower temperature in comparison with the raw samples. It is known  that organic functional groups on multiwalled carbon nanotubes are thermally unstable; that is, most of them are decomposed before the onset of MWNTs weight loss. Fan et al.  explained burning of the sample at lower temperatures by the formation of oxygenated groups on the surface of MWCNTs during purification procedure, which are more reactive towards oxidation. Similar explanation is presented by Osorio et al.  and Murugesan et al. . The same behavior was observed by Shen et al.  during thermogravimetric analysis of aminofunctionalized multiwalled carbon nanotubes. In our case, attachment of the functional groups can give similar effect but only in the case of the carbon nanotubes obtained on the cobalt and iron/cobalt catalyst. In our opinion, higher thermal stability of the carbon nanotubes prepared on the iron catalyst may be due to the presence of very small quantities of metal particles in the carbon material after chlorination process (see Table 3). According to  metal particles embedded in the raw sample act as oxidation sites and initiate the oxidation reaction. In the same work, it was also reported that the metal impurity would lower the decomposition temperature and increase the decomposition rate. That is why the purified sample is thermally more stable towards oxidative destruction than the raw one.
The presence of chlorine in the obtained samples (Fe450Cl, Co450Cl, FeCo450Cl) has been confirmed using the Mohr titration method. The results are shown in Table 4. A significant increase of the content of active chlorine can be noted in the samples after the chlorination process compared to unmodified samples. The chlorine content in the samples after the modification was the same for all the studied samples. Slightly higher value was observed only for the sample obtained on the bimetallic catalysts (FeCo450Cl).
The presence of the chlorine species in carbon material obtained using iron, cobalt, and iron-cobalt catalysts was also confirmed by EDS and XPS analysis and the results of the quantitative analysis of the composition are presented in Tables 1 and 2, respectively.
The XPS analysis revealed the presence of chlorine species on the surface of all chlorinated samples. It was found that the amount of chlorine for the sample treated at the lowest temperature (FeCo50Cl) was about 1.3%. Similar concentration was obtained for the sample chlorinated at 250°C (FeCo250Cl). The increase of chlorine species concentration was noticed for the sample treated at 450°C (FeCo450Cl)—about 2.2%. The quantitative analysis of the surface composition using EDS was performed as well. The samples after chlorination at 50°C, 250°C, and 450°C included 0.5, 1.4, and 2.3% of chlorine, respectively. Therefore together with the increase of temperature, an increasing trend in chlorine concentration on the surface was seen like in the case of the results obtained using EDS.
The XPS spectra of Cl 2p lines for the samples containing FeCo catalyst and treated in gas in the temperatures 250°C and 450°C are shown in Figure 4. The other set of XPS spectra of Cl 2p lines compares the samples originating from three different catalysts treated at 450°C and are shown in Figure 5.
In case of all chlorinated samples, two components (each consisting of the 3/2 and 1/2 level with a spin-orbit splitting of 1.6 eV) are required to obtain a reasonable fit of the Cl 2p core level spectra. The binding energies of 3/2 components are 198.5 ± 0.1 eV and 200.0 ± 0.1 eV, respectively. The latter component corresponds well to chlorine atoms covalently bonded to sp2 carbon [39–41]. The low binding energy component at approximately 198.5 eV is in the range usually ascribed to chloride ions . However, there is a lack of metal cations in the surface of most of analyzed samples, which suggests another origin of the low binding energy component. In the literature, the position of 198.0 eV is also ascribed to the features associated with atomic chlorine adsorbed on the surface .
The relative intensity of the components observed in Cl 2p spectra changes with temperature of the chlorination (see Figure 4). In the sample chlorinated at 250°C, the low binding energy component at 198.5 eV amounts to 53% of the total intensity of Cl 2p peak, whereas this component found in the spectrum for the sample treated at 450°C equals to 38% of the intensity of Cl 2p peak. It suggests that the chemical species corresponding to the low binding energy component decompose or desorb with a temperature rise. At higher temperature, chlorine weakly bonded with the surface presumably desorbs, but covalently bonded chlorine, represented by XPS Cl 2p line at 200 eV, remains in the material, which corresponds well with the above observations.
The comparison of XPS spectra of Cl 2p lines coming from samples obtained with different catalysts (Figure 5) shows that the low energy component of this spectrum has the lowest contribution in the Co450Cl sample, only 16%. In the sample formed on the iron catalyst, Fe450Cl, its contribution increases to 22%, while on the surface of FeCo450Cl it accounts for 38% of whole Cl 2p line.
Most of the available papers are concerning the introduction of chlorine species using different reagents at liquid phase. Lee et al.  studied functionalization of single-walled carbon nanotubes using dichlorocarbene. It was found that chlorine atoms amounting to about 1.6 at.%. Yuan et al.  involved chlorine water and ammonia water to the treatment of multi walled carbon nanotubes. On the basis of EDS spectra, it was reported that some C–Cl bonds were introduced, but the amount of chlorine was rather low and equalled about 0.23 at.%. Duesterg et al.  studied chemical functionalization of single walled carbon nanotubes using hydrothermal treatment in aqueous acidic solutions. Depending on the oxidation strength of the acids, halogen surface groups, like chlorine, were introduced on the level <1 at.%. Barkauskas et al.  described the treatment of carbon nanotubes with tetrachloromethane, what facilitated increasing the amount of chlorine up to 6.8 at.% in the carbon phase. Barthos et al.  compared functionalization of single-walled carbon nanotubes using gas chlorine and alkyl-halides. Chlorine content determined by PIGE technique was in the range of 5.5–17.5 wt.% of chlorine. Kónya et al.  proposed mechanochemical modification of multiwall carbon nanotubes. They stated that the use of ball milling in chemically reactive atmosphere allows us to introduce functional groups like chlorine onto carbon nanotubes, but the quantitative analysis is not presented at work. In the light of these reports, the present results show that using chlorination method in the gas phase is possible to introduce the chlorine species to the equal or even higher concentration.
In this work, chlorination method in the gas phase to functionalization of carbon nanotubes is proposed. Using XPS and EDS method, the presence of chlorine species on the surface of chlorinated samples was revealed. The percentage content of chlorine species depended on chlorination temperature and equaled from about 0.5 at.% to 2.3 at.%. Simultaneously, removal of catalyst particles was observed. On the basis of thermogravimetric curves, it was calculated that the amount of remaining catalyst particles was in the range from 0.2 to 6.5%. In the light of this report, we can conclude that this method can be useful to incorporate functional groups on the carbon nanotubes surface and additionally can be applied to purification of carbon nanotubes from metal particles.
This work was supported by project: LIDER/25/58/l-3/11/NCBR/2012 financed by the National Centre for Research and Development.
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