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Simultaneous purification and functionalization of carbon nanotubes using chlorination

Published online by Cambridge University Press:  31 July 2012

Iwona Pełech*
Affiliation:
Faculty of Chemical Engineering, Institute of Chemical and Environmental Engineering, West Pomeranian University of Technology in Szczecin, 70-310 Szczecin, Poland
Urszula Narkiewicz
Affiliation:
Faculty of Chemical Engineering, Institute of Chemical and Environmental Engineering, West Pomeranian University of Technology in Szczecin, 70-310 Szczecin, Poland
Dariusz Moszyński
Affiliation:
Faculty of Chemical Engineering, Institute of Chemical and Environmental Engineering, West Pomeranian University of Technology in Szczecin, 70-310 Szczecin, Poland
Robert Pełech
Affiliation:
Faculty of Chemical Engineering, Institute of Organic Chemical Technology, West Pomeranian University of Technology in Szczecin, 70-310 Szczecin, Poland
*
a)Address all correspondence to this author. e-mail: ipelech@zut.edu.pl

Abstract

Multiwalled carbon nanotubes (MWCNTs) obtained using ethylene as a carbon source and nanocrystalline iron as a catalyst were used as the initial material. The functionalization of MWCNTs was carried out using chlorine in the liquid and gas phase. In the second case, the reaction was conducted in the temperature range from 50 to 450 °C for 2 h. The presence of chlorine species on the surface of chlorinated samples was confirmed by x-ray photoelectron spectroscopy (XPS). A quantitative analysis of metal impurity content was validated by means of thermogravimetric analysis. Better results of metal removal were achieved when the chlorination process was conducted in the gas phase and the ratio of metal in samples amounted from 2.3% to 5.1%.

Information

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Articles
Copyright
Copyright © Materials Research Society 2012
Figure 0

FIG. 1. The scheme of chlorination process.

Figure 1

FIG. 2. TEM images of the samples after chlorination at 150 °C (a–b) and 250 °C (c–d).

Figure 2

FIG. 3. XRD spectra of the raw sample (6) and the samples after chlorination process in the gas phase at 50 °C (1), 150 °C (2), 250 °C (3), 450 °C (4), and in the liquid phase (5).

Figure 3

TABLE I. Interplanar distance, graphitization degree, and catalyst’s content for the sample before and after chlorination process.

Figure 4

FIG. 4. TG curves of the raw sample (1), samples after chlorination in the liquid (2) and gas phase at 50 °C (3), 150 °C (4), 250 °C (5), 450 °C (6).

Figure 5

FIG. 5. XPS Cl 2p lines for samples chlorinated under gas chlorine at temperatures 50, 150, 250, and 450 °C as well as for sample chlorinated in CCl4.

Figure 6

FIG. 6. XPS C 1s lines for nonchlorinated sample, for samples chlorinated under gas chlorine at temperatures 50, 150, 250, and 450 °C as well as for sample chlorinated in CCl4.

Figure 7

TABLE II. Surface composition of the samples after chlorination at gas and liquid phase calculated upon XPS data.

Figure 8

FIG. 7. Dispersion of the raw sample (1), the samples after chlorination in the gas phase at 50 °C (2), 150 °C (3), 250 °C (4), 450 °C (5), and liquid phase (6) in ethylene (a) and butylene (b) glycol.