narrower nanofibers. At 600 °C, a wide distribution of CNF diameters in the range of 25–55 nm was observed. CNFs with a diameter of 36–55 nm were obtained when the Ni/HAp catalyst was reduced at 650 °C. The shift in the CNF diameter to larger values as the reduction temperature increases was due to an increase in the Ni crystallite size. CNFs with larger diameters were also grown by increasing the reaction temperature [38].
Figure 3.7 TEM images of CNFs with (a & b) herringbone structure without hollow core, synthesized over nickel catalyst using both methane and propane as carbon precursors respectively; (c) The platelet structure in which the graphene layers are aligned perpendicularly to the fiber axis, and (d) the thinnest among the synthesized nanocarbons, with diameters of 10–20 nm [38].
3.6 Synthesis of Carbon Nanofiber (CNF) Using Nanocatalysts
Different methods, such as incipient-wetness impregnation, ion exchange, organometallic grafting, electron beam evaporation, and deposition/precipitation followed by reduction, are used to prepare noble metal nanoparticles supported on carbon fibrous materials. In all cases, a delicate optimization of carbon surface chemistry is needed to achieve optimal interaction between the support and metal precursor.
Due to their unique nature, carbon nanofibers are considered as exciting supports for noble metal nanoparticles. Indeed, hollow nanotube cavities can be used to control a particle size and shape. High metal dispersion was obtained on CNTs even if the specific surface area of the support was only 25 m2/g. Nanotubes can be filled by metals during the arc-discharge synthesis in the presence of metals or through opening and filling the tubes by a metal precursor followed by reduction. It is also possible to remove unwanted metal particles from the outside surface of CNTs [39]. The process took place via reduction of [PdCl4]2~ anions and simultaneous encapsulation of Pd nanoparticles in CNTs during rolling of graphene sheets from the anode.
Cu particles supported on different types (fishbone, platelet, ribbon, and tubular) of CNFs were deposited from aqueous salt solutions [40]. If Cu nanoparticles were located on the edge sites of nanofibers, they adopted a thin faceted morphology, indicating a strong metal-support interaction. The particles formed in such a way were very stable with respect to sintering. However, the particles tended to acquire a globular geometry if the copper was supported on AC or the basal planes of graphite, showing a very weak interaction with the support. Thus, the fishbone and platelet CNFs were the best supports to provide small particles with a narrow size distribution. A precursor salt and carbon surface functionality also affect the particle size distribution and stability.
Supported Cu nanoparticles (<10 nm) were prepared using CNFs with a diameter ranging from 100 nm. Carbon nanofibers were impregnated with a copper salt solution, dried and treated by H2 (773 K). The electronic properties of the nanoparticles differed considerably from those of bulk copper. It was noticed that the size of Cu particles was dependent on the size of CNFs: the smaller the fiber diameter, the smaller the Cu nanoparticle size obtained. However, the nanoparticles were not strongly attached to the support and could be detached by ultrasonic treatment.
The Pd nanoparticles supported on CNFs exhibited a comparable activity in hydrogenation of nitrobenzene to aniline and increased activity in hydrogenation of C=C bond of cinnamaldehyde with respect to the commercial Pd catalyst based on AC. An important advantage of the CNF support is that surface area, size of fibrils, as well as mechanical strength can be controlled and mass transfer limitation can be decreased, because of the absence of micropores. A change of electronic properties of Pd particles provided by interaction with CNFs resulted in a change of their catalytic properties in 1,3-butadiene hydrogenation to butanes. An increase of the Pd2+ fraction in the catalysts decreases the activity and selectivity.
Pd supported on the fishbone-type CNFs was studied in hydrogen storage. The hydrogen loading of 1.5 wt% was reached at 10 MPa of H2 pressure for nanofibers with specific surface area of 400 m2/g and Pd:C mole ratio close to 1. Hydrogen of 3.1 wt% stored was reported for the 4.1 wt% Pd/MWNT material. However, all these values are well below the 6.5 wt% benchmark set by the U.S. Department of Energy for such kinds of materials.
Carbon nanofibers (CNFs) are hydrophobic, generally without significant functional groups. The diameter of a CNF ranges between 50 nm and 200 nm and that of the carbon nanotubes is usually less than 100 nm. Several methods have been used in the synthesis of CNF.
3.6.1 Laser Ablation Method
In laser ablation, a graphite target source with a small amount of catalysts (usually a transition metal) is exposed to a laser beam which vaporizes the graphite and initiates the growth of CNF just in front of the target [41].
3.6.2 Chemical Vapor Deposition (CVD)
The CVD method is the most common method for bulk production of carbon nanomaterials. Different hydrocarbons are used as precursor for CNM. At high temperature (between 500 and 1200 °C) under pyrolytic condition, carbon is deposited on various metal catalysts (Fe, Co, and Ni). This method is described in detail in Chapter 1 of this book. The process parameters that are important for the synthesis of CNF are the ratio of hydrogen to carbon source flow, reaction time, and temperature [42].
In the CVD process, CNFs are usually produced by catalytic pyrolysis of hydrocarbons in the presence of a transition metal catalyst and a trace amount of sulfur to promote the formation of CNF. Precursors that have been successfully used to synthesize CNF by CVD method are methane, carbon monoxide, synthesis gas (H2/CO), ethyne or ethane, acetylene, etc. The hydrocarbon or the precursor, along with the catalyst, hydrogen gas, and a sulfur source, are introduced into the reactor. Ferrocene (C10H10Fe), dissolved in a suitable solvent, and iron pentacarbonyl (Fe(CO)5) are commonly used catalyst sources. The organometallic catalyst decomposes, forming clusters of iron (Fe) particles that act as nuclei for the formation and further growth of CNFs. The fibers grow as they move along the reactor, and the diameter of fibers increases by the classic chemical vapor deposition (CVD) mechanism. Both horizontal and vertical reactor configurations have been employed. The fibers coming out of the reactor, along with the off-gases, are trapped and separated via a series of cyclone separators or trap mechanisms located downstream of the reactor. The entire reactor assembly is enclosed within an electric furnace to supply sufficient heat to maintain the pyrolysis temperature of 500 to 1,200 °C. The characteristics of the fibers, such as their thickness and length, are controlled through careful manipulation of the parameters, such as the catalyst concentration, reaction time, and size of the catalyst particles produced. The CNFs prepared by catalytic thermal chemical vapor deposition show different morphologies such as cup-stacked CNF [43] and platelet CNF. For the preparation of CNF by the catalytic vapor deposition growth approach, several types of metal or alloys, which are able to dissolve carbon to form metal carbide, have been used as the catalyst, including iron, cobalt and nickel; chromium, vanadium and molybdenum. Generally, the structures of the CNF are governed by the shapes of the catalytic nano-sized metal particles. The growth mechanism has been proven as the deposition of the hydrocarbons dissolved in the metal particle and precipitated on the metal surface as graphitic carbon.
Hydrogen: The role of hydrogen is to accelerate or suppress the formation of carbon by either decomposing the inactive metal carbides to form active metal [44], or by removing the surface carbon and precursors of carbon which leads to active site blocking.
Temperature: The diffusion and precipitation rates of carbon atoms and availability of carbon atoms are affected