Journal of Nanomaterials

Journal of Nanomaterials / 2019 / Article

Research Article | Open Access

Volume 2019 |Article ID 9189525 | 13 pages |

Thermodynamic Simulation and Experimental Investigation of Plasma Preparation of Nanosized Carbon Using Propane

Academic Editor: Ilaria Armentano
Received12 Dec 2018
Accepted21 Feb 2019
Published17 Apr 2019


Carbon black was prepared by pyrolysis of propane under different plasma conditions. The effects of the flow ratio of the carbon precursor, discharge current, and plasma gases (including argon, nitrogen, and hydrogen) on the morphology and structure of carbon black were investigated by a series of physical characterizations. The equilibrium components were computed based on the minimization of the Gibbs free energy. The theoretical analysis and experimental results confirmed that HCN is the inevitable byproduct in the tail gas from the nitrogen plasma process, indicating that nitrogen is inappropriate as the carrier gas for the preparation of carbon black. The effects of discharging current, discharging spacing, and proportions of propane were also symmetrically studied by the evaluation of HCN concentration. Moreover, the graphene was generated when using argon as the plasma gas mixed with a small amount of hydrogen.

1. Introduction

Carbon black is one of the most commonly used carbon nanomaterials and has nowadays been widely applied as electrically conductive materials and reinforcing fillers in the areas of rubbers, plastics, elastomers, and batteries due to its peculiar and tunable chemical, physical, and electrical properties [16].

The different kinds of carbon black are generally manufactured by calcination in furnace, channel and lamp processes, thermal pyrolysis, or acetylene method [7]. These processes are usually categorized into incomplete combustion and thermal decomposition of hydrocarbon, depending on the participation of oxygen [8]. Although more than 95% of carbon black products are fabricated by furnace and channel processes, the increasing environmental issues and pollution emission caused by these mainstream approaches cause serious human health problems. Thus, alternative and sustainable technologies are highly desirable for the preparation of carbon black [9].

The plasma processes have gained increasing attention in the development of a renewable method to overcome these drawbacks during the existing processes. Considered as the fourth state of matter apart from solid, liquid, and gas, plasma usually consists of molecules, atoms, ions, electrons, and radicals [10]. Plasma could be obtained via various methods, such as combustion, flame technique, electrical heating, and electrical discharge [11]. Researchers have developed several plasma processes such as plasmatron [12], dielectric barrier discharge [13], gliding arc discharge [14, 15], corona technique [16], microwave method [1719], pulse discharge [20], and direct current discharge [21]. Considering its energy level, temperature, and electronic density during the discharging process, plasma is categorized as thermal and nonthermal [22] ones. The temperatures of electrons in nonthermal plasma can reach the range from 10000 to 100000 K, while the gas temperature remains as low as room temperature. This high electron temperature leads to the unusual chemical and physical properties of nonthermal plasma. However, in the thermal plasma, the temperatures of electron and ambient gas are considered to be close to each other. Therefore, thermal plasma exhibits higher chemical reactivity than the nonthermal one.

Thermal plasma technology was initially investigated in the early times of the twentieth century and has been extensively studied thereafter. Plasma preparation of carbon black was first demonstrated by Rose [23] in 1920. In his work, electrodes were installed on the ends of a cylindrical reactor and carbon black was prepared through pyrolysis of hydrocarbon. Later on, Ryan [24] put different hydrocarbons into the same plasma reactor and found that the prepared carbon black showed semblable properties. This finding also confirmed the feasible preparation of carbon black by plasma. Thus, research on the plasma preparation of carbon black has focused on optimizing technological process and reaction conditions.

The thermal plasma technology has attracted much interest recently mainly because of its potential in the large-scale production of carbon black through the pyrolysis of hydrocarbon. This technology obviates harsh conditions such as acid, base, or catalysts, thereby being considered to be easily controllable and environmentally friendly.

The pyrolysis of hydrocarbon by thermal plasma is a complex and dynamic process. In a closed system, the conversion reaction among components will reach equilibrium after a certain period of time. The principle of computing the equilibrium composition is mainly thermodynamics. The thermodynamics deals only with the problem of equilibrium, not the equilibrium reaction rate. Although there are few phenomena indicating that the process is completely under equilibrium, it is still important to study the equilibrium process. First, the equilibrium determines the limitation that the given reaction can be achieved. Second, the equilibrium predicts the changing trend of product composition as the reaction conditions (temperature, pressure, etc.) change and provides the processing conditions for the desirable products [2528].

Argon and helium are the most commonly used carrier gas to generate ambient plasma [2932] because these monatomic gases are inert and easily maintain ambient plasma. However, argon and helium are expensive and unsuitable for large-scale manufacturing of carbon black. The preparation of carbon black using nitrogen plasma shows great advantages in terms of cost control, because nitrogen is relatively cheap and easy to ignite at atmospheric pressure.

In this study, carbon black is prepared by the thermal pyrolysis of propane using argon, hydrogen, and nitrogen as carrier gases. The essential properties of carbon black prepared through different processes were analyzed in both theoretical and experimental ways. Besides, the equilibrium compositions were obtained by the minimization of Gibbs free energy. It was found that HCN has been identified as the byproduct while using nitrogen as the carrier gas. The optimal conditions for reducing the concentration of HCN in the tail gas were also explored.

2. Materials and Methods

2.1. Materials and Devices

The reactor system in this study was designed based on the preliminary research of Zhao et al. [33]. As shown in Figure 1, this system consists of a power source, a plasma generator, a heat exchanger, and an HCN absorber. In the experimental conditions, propane and carrier gas were mixed in the buffer tank and flowed into the plasma reactor. The propane was decomposed into carbon black and hydrogen in the plasma environment. The gas-solid mixtures passed through the heat exchanger, and the obtained carbon black was filtered by the sintered disc. In order to determine the HCN concentration, the tail gas was collected and tested.

Propane (C3H8), nitrogen (N2), argon (Ar), and hydrogen (H2) were all industrial grade and purchased from Suzhou Jinhong Gas Co. Ltd. The sodium hydroxide (NaOH) and acetone (CH3COCH3) were obtained from Sinopharm Chemical Reagent Co. Ltd. Rhodanine (C12H12N2OS2) and silver nitrate (AgNO3) were provided by Shanghai Jinchun Biological Tech. Co. Ltd.

2.2. Preparation of Carbon Black

The thermal plasma was produced by an electric arc between tungsten electrodes connected to an AC power supply. The reactor was first purged with the carrier gas. Then, propane was poured in and the AC power was turned on. Discharging was maintained for 10 minutes to allow us to examine the experimental results. A rubber tube was connected to the end of the condenser, and the gas flowed out of the plasma zone was blown into the sodium hydroxide solution and the HCN was absorbed to obtain a sample solution. The sample solution was added with rhodanine and titrated by silver nitrate solution. When the color of the solution changed from yellow to orange, the titration reached the end point. The concentration of CN- was calculated according to the dosage of the silver nitrate solution using the following formula:

The concentration changes of CN- in the plasma system were determined and compared by changing the current and distance between electrodes and the propane flow ratio.

3. Results and Discussion

3.1. Single Factor Analysis for the Morphology of Carbon Black
3.1.1. Effect of Propane Flow Ratio

To examine the effect of the propane flow ratio on the morphology of the carbon black, the reaction was performed using tungsten electrode with a total gas flow of 1.5 m3/h (N2 as the carrier gas) and the propane flow ratio regulated at 10%, 20%, 30%, and 40%. Figure 2 shows the SEM images of carbon black prepared at different propane flow ratios. With the same total flow ratio, the average particle size of carbon black increases along with the increasing propane flow ratio. At a low propane flow ratio of 10%, the obtained carbon black exhibits good dispersibility with an average diameter of 30-40 nm as shown in Figure 2(a). When the propane flow ratio increased to 20%, it was obvious that the particle size of carbon black increased to 60-70 nm (Figure 2(b)) with relatively good dispersion. While further increasing the propane flow ratio to 30%, the carbon black shows agglomeration (Figure 2(c)). The higher propane flow ratio in the mixed gases leads to a higher nucleation rate and the formation of smaller subparticles within a short time. Subsequently, these small subparticles aggregated to form a large nanostructure. Figure 2(d) shows that a lot of carbon black generated by plasma was aggregated to form large spherical carbon black when the propane flow ratio is 40%. That is, the larger the propane flow ratio in the mixed gases, the higher the amount of carbon black prepared by the plasma [34]. These particles go through a microcosmic random walk and become interconnected in different directions. It is assumed that carbon black possibly agglomerated to a spherical structure according to the results shown in Figure 2(d). Therefore, a 20% propane flow ratio is the optimal condition for the preparation of carbon black.

Figure 3 shows the X-ray diffraction (XRD) patterns of carbon black prepared under different propane flow ratios. It is observed that all the samples have remarkable (002) and (100) peaks with corresponding of 24° and 44°, respectively. The (002) peak represents the graphitized structure, and a higher and narrower peak indicates the higher graphitization of carbon black [35]. The (100) peak indicates that the CB possessed a disordered structure. The XRD curves of four samples indicate that increases and decreases with increasing propane flow ratios, and the (100) peak has no significant change when the flow ratio of propane is greater than 10%. This finding indicates a decrease in the graphitization of carbon black. Therefore, reducing the propane concentration can increase the graphitization of carbon black.

3.1.2. Effect of the AC Current

The reaction was performed using a tungsten electrode with an AC current of 2-8 A to determine the effect of the AC current on the morphology of the carbon black. The TEM images of carbon black prepared at different currents are shown in Figure 4. The average size of carbon black increases along with the increasing current. As shown in Figure 4(a), the clear outline of carbon black particles was seen for an AC current of 2 A. When the current increased to 4 A, it was found that the particles of carbon black started to agglomerate, but the basic appearance of carbon black particles can still be observed in Figure 4(b). As the current continues to increase, the severe agglomeration of carbon black particles can be observed obviously in Figures 4(c) and 4(d). It is suggested that the plasma temperature and growth rate of carbon black particles are influenced by the increase of the input current. According to the previous studies, the plasma gas temperature increases along with increasing energy input [36]. Thus, the corresponding plasma gas temperature increases when the AC current is increased from 2 to 8 A. Usually, a higher power enhances the endothermic decomposition of propane, leading to higher temperature and greater nonequilibrium driving force for the growth of carbon black. This result might be explained by the fact that the particle growth rate is more rapid than the nucleation rate at high reaction temperatures, which resulted in the production of particles with a larger size.

The Raman spectra of carbon black at different AC currents are shown in Figure 5. The carbon black exhibits intense and peaks at around 1330 cm-1 and 1580 cm-1, respectively. These peaks originate from the growth of carbon crystallites in size and number, leading to the formation of a partially ordered structure. This finding indicates the disordered random orientation of the tubes and the graphitic nature of the carbon materials [37], respectively. Cho et al. [38] reported that the partial ordering of amorphous carbon at high temperatures resulted in the appearance of intense and peaks in the Raman spectrum. The ratio of and peaks () determines the amount of disorder in the crystallinity [39]. The larger the ratio of , the lower the graphitization of carbon black that could be observed. The growth from amorphous carbon to nanocrystalline carbon generates a temperature increase from 1700 to 2000 K [40]. As shown in Figure 5, with the AC current increasing, the value of decreases and the graphitized degree of the carbon black increases. Therefore, increasing the AC current is conducive for the formation of an ordered high-graphitized carbon black structure [41].

3.1.3. Effect of the Different Types of Carrier Gases

To find out suitability of carrier gases, different carrier gases have been tested, and the morphology of carbon black must be investigated to determine which carrier gas is the most suitable.

Figure 6 shows the SEM images of carbon black prepared by a plasma process using different carrier gases. The figure depicted that carbon black prepared using argon plasma exhibits the biggest particle size of 120 nm (Figure 6(a)). Compared with argon, nitrogen as a kind of diatomic gas needs more energy to break its N≡N bond. Thus, during the discharging process, nitrogen uptakes more energy to form a plasma environment, which competes with the growth rate of carbon black.

The particle size from the nitrogen plasma is generally in the range of 80 to 100 nm (Figure 6(b)). Figure 6(c) reveals that carbon black from hydrogen plasma is around 50 nm, which is the smallest size among the three kinds of carrier gases. This is due to the hydrogen needing more energy than the nitrogen and argon to form plasma. The hydrogen radicals with ultrahigh activity generated during the discharging process bind to the carbon atoms at the outer surface of carbon black and were released in the form of hydrocarbon [42] during the growth process.

For further observations of the morphological and branching structure of carbon black products, the TEM measurements were conducted (Figure 7). As depicted from the TEM images, the carbon black prepared from argon plasma shows the homogeneous distribution of the primary particle size but aggregates more severely than those prepared from nitrogen and hydrogen plasma. The nonuniformity in the size of carbon black from nitrogen plasma is evident from the observation shown in Figure 7(b). This nonuniformity is possibly caused by the adsorption of energy to break a N≡N bond, which brings a relatively intense temperature gradient in the plasma environment. In the high-temperature area, the carbon black particles grow in a sufficiently fast rate, while the growth rate is limited in the low-temperature area.

3.2. Structures of Carbon Black

The critical structures of carbon black were characterized by XRD and Raman spectroscopic analysis to determine the effect of plasma gas on the structure of carbon black. As shown in Figure 8, the peak corresponding to the (002) lattice plane around 26° appears in all of the three patterns. For the carbon black prepared by hydrogen plasma, the (002) lattice plane is located at 25.9° with a -spacing of 0.352 nm. The plane exhibits left skewing compared with the ideal graphite, which shows a sharp and intense peak at 26.5° with a -spacing of 0.334 nm. This left skewing and the enlargement of interlamellar spacing indicate the existence of amorphous carbon and distortion of lattice fringes [28]. The (002) peak of carbon black obtained from nitrogen plasma is located at 26.1° with a -spacing of 0.349 nm. The carbon black obtained from argon plasma shows a wide (002) peak with a low intensity at 25.5° and -spacing of 0.356 nm. Based on this information, the crystalline structure of carbon black from nitrogen plasma is the best among the three samples. The Raman spectroscopic analysis was carried out to verify this result.

The Raman spectroscopy can effectively characterize the structure of carbon nanomaterials. Generally, the two pattern peaks of carbon black in the Raman spectra are as follows: the band around 1330 cm-1 is assigned to the disorder and defects in carbon black and the band around 1580 cm-1 is due to the well-ordered lattice plane [43, 44]. The intensity ratio between the band and the band () is a significant index used to estimate the quality of carbon black. As shown in Figure 9, the ratio of carbon black prepared from argon plasma exhibits the highest value of 1.33. This finding is probably because in the argon plasma, a large amount of amorphous carbon was deposited onto the surface of carbon black, leading to larger defects and bigger particle size. The ratio of carbon black from hydrogen plasma is lower; it is because of active hydrogen radicals etching the amorphous carbon during the growth process. The ratio of carbon black prepared from nitrogen plasma is 0.99, which is the lowest among the three kinds of carbon black and indicates the best quality. This result is consistent with the XRD results.

3.3. Thermal Stability of Carbon Black

The thermogravimetric analysis (TGA) was conducted to investigate the thermal stability of carbon black prepared by different processes. This analysis can estimate the surface cleanliness of carbon black to indirectly assess the quality and secondary structure. As shown in Figure 10, the carbon black prepared by argon plasma degraded faster than other samples due to the volatilization of amorphous carbon with 73.5% residual at 1000°C. The carbon black prepared by nitrogen plasma is more stable than that prepared by argon plasma due to less amorphous carbon with 84.2% residual at 1000°C. However, the carbon black from nitrogen plasma shows a higher amount of surface functional groups than that from hydrogen plasma which is theoretically recognized to have a totally clean surface with little amorphous carbon black. Hence, the carbon black from hydrogen plasma is more stable and maintains 88.9% residual at 1000°C. As shown in the TGA curves, all three kinds of samples exhibit obvious weight loss before 200°C. The highest weight loss was found in carbon black from argon plasma. This phenomenon could be explained by TEM observation of its structure. It is well known that carbon black exhibits hygroscopicity, developed secondary structure, and high water absorbing capacity. In Figure 7(a), the carbon black prepared from argon plasma possesses a more organized secondary structure owing to more chains. Therefore, a higher amount of water vapor was adsorbed by the carbon black from argon plasma when stored in air, leading to a dramatic weight loss during the thermogravimetric process. As shown in Figure 7(c), carbon black prepared by hydrogen plasma is less branched with lower water absorbing capacity and thus exhibits the highest thermal stability before 200°C.

3.4. The Formation of Cyanide

The equilibrium components of 1 mol propane after pyrolysis under different kinds of plasma are shown in Figures 11, 12, and 13. The simulation was carried out using FactSage software [45]. Generally, the components show similar varying trends under all circumstances. It is noticeable that propane is first decomposed into methane and ethane and then further polymerized to form polycyclic aromatic hydrocarbon, which becomes the primary nuclei of carbon black [28]. The propane could be totally pyrolyzed before 800°C in the argon (Figure 14) and nitrogen (Figure 15) plasma and at 1200°C in the hydrogen (Figure 11) plasma. This phenomenon could be attributed to the fact that high hydrogen concentration would hinder the decomposition of propane into methyl and hydrogen radicals. Although previous works reported that HCN cannot be generated using nitrogen as plasma gas [46], the thermodynamic equilibrium simulation showed that HCN is one of the major components in the equilibrium system while using nitrogen as the carrier gas. The concentration of HCN increases significantly along with the increasing of temperature.

To verify the simulation results, experiments were carried out by changing the electric current (1, 2, 3, and 4 A) and propane flow percentage (10%, 20%, 30%, and 40%; total flow 120 L/h) to demonstrate whether cyanide was generated. The HCN concentration was then measured in the tail gases. Figure 12 shows the concentration of HCN under the experimental conditions. In contrast to previous reports, HCN was formed using nitrogen as plasma gas. In general, the concentration of HCN increases with the increasing of current or propane flow percentage. Based on the data when propane flow percentages are at 10% and 20%, the concentration of HCN increases linearly as the current increases from 0.62 and 1.15 mg/L to 2.31 and 3.01 mg/L, respectively. The reason is probably that the ionization degree of carrier gas increases as the current increases, and the amount of active plasma species increases. Hence, the reaction system could obtain more heat, and the temperature of the system increased for the ease of propane pyrolysis. Therefore, many carbon and hydrogen radicals react with nitrogen radicals to generate HCN in the system. And the increase of temperature was conducive to the combination of the three species. When the propane flow percentage increases to 30% and the current in the range of 1 A to 3 A, the concentration of HCN also increases linearly (from 1.85 mg/L to 3.58 mg/L). However, when the current is further increased to 4 A, the concentration of HCN becomes 3.61 mg/L, which is almost the same as the results when the current is 3 A. When the propane flow percentage is 30% and the current increases to some certain extent, the amount of carbon and hydrogen free radicals in the system is more than that of nitrogen. Further increasing of the current could not enhance the reaction extent to produce more HCN. When the propane flow percentage increases to 40%, the situation becomes more obvious. When the current is 2 A, the reaction is nearly saturated, and the concentration of HCN reaches a plateau; when the currents are 3 A and 4 A and the propane flow percentage is 30%, the concentration of HCN is low. The reason might be that when the propane flow percentage increases to 40%, the amounts of carbon and hydrogen free radicals are high and the amount of nitrogen is low. Therefore, nitrogen combined less with carbon and hydrogen resulting in a decrease in concentration.

The experiments were also carried out to investigate the influence of the distance between electrodes (1, 2, 3, 4, and 5 mm) on the formation of HCN. Figure 13 illustrates the concentration of HCN absorbed in the sodium hydroxide from the tail gas at different distances between electrodes. The HCN concentration in the solution varies with distances between electrodes. When the distance is 1 mm, the HCN concentration is as low as 1.19 mg/L. The concentration increases with the increasing distance between electrodes. When the distance is increased to 3 mm, the concentration reaches a peak value of 4.06 mg/L and started to decrease when the distance further increases. The HCN concentration decreases to 2.17 mg/L at a distance of 5 mm. This is due to, at a 1 mm distance, the plasma volume being small and the electrodes too close to achieve the competition of reaction when mixed gases passed by, which leads to the low concentration of the byproduct HCN. The plasma volume increases with the increasing electrode distance, and the gas has sufficient time to react, resulting in increasing HCN concentration. However, after elongating the distance to more than 3 mm, the current decreases and the plasma temperature is low. The energy of plasma is not enough to promote the pyrolysis of propane, and therefore, the concentration of HCN decreases again.

According to these experimental results, the amount of cyanide after the pyrolysis of 1 mol propane in nitrogen was calculated. For the sample prepared at an electrode distance of 3 mm, a discharge current of 4 A, and a propane percentage of 30%, the amount of cyanide is , which is lower than that from the thermodynamic equilibrium computation obtained between 1500°C and 2500°C, the usual temperature range of AC arc discharge. This finding is due to the difficulty in reaching the thermodynamic equilibrium under experimental conditions and the insufficient reaction time for the formation of cyanide. Thus, carbon black was prepared at the electrode distance of 3 mm, discharge current of 4 A, and propane percentage of 30% under nitrogen plasma. The FT-IR and XPS measurements were further performed for more spectroscopic studies.

In the FT-IR spectrum, as shown in Figure 16, the peak at 3675 cm-1 is ascribed to -OH from water, which was adsorbed by carbon black in the air. The peak at 1384 cm-1 is due to the existence of the C-H bending model. The peak at 1630 cm-1 originates from the stretching vibration of C=C, which is the essential unit of polycyclic aromatic hydrocarbon. In addition to the typical peaks in normal carbon black, two additional pattern peaks are also found in the spectrum. The peaks at 1110 cm-1 and 2360 cm-1 are assigned to the stretching vibration of C-N and C≡N, respectively. The FT-IR results provide a solid evidence for the existence of cyanide.

Figure 17 shows the XPS spectra of carbon black prepared from nitrogen plasma. The spectra reveal the existence of carbon, oxygen, and nitrogen bonds. The peaks around 284.6, 400.0, and 533.2 eV represent C, N, and O, respectively [4749]. The existence of O 1s suggests that the air in the reactor cannot be removed completely. The high resolution spectrum of N 1s was further analyzed to acquire additional information about the chemical bonds on carbon black. Figure 17(b) shows the deconvoluted N 1s spectrum, which is fitted by two best fitted peaks with Gauss function. The peak at 399.6 eV is attributed to the cyano group -C≡N, and the peak at 402.4 eV is assignable to the pyridine group C-N [50]. Although O has been detected, the N-O bond is not found.

3.5. The Existence of Graphene in the Product

During the preparation of carbon black by pyrolysis of propane, it is remarkable to find the existence of graphene in the product, when using argon as plasma gas mixed with a small amount of hydrogen. As shown in Figure 18(a), only carbon black was observed in the range of vision with the absence of hydrogen. When a small amount of hydrogen (hydrogen/propane ratio is 1 : 40) was added, some graphene appeared in the field of view, but the graphene boundary was blurred as shown in Figure 18(b). As the hydrogen flow ratio increases (hydrogen/propane ratio is 1 : 20), the amount of graphene in the field of view increases as shown in Figure 18(c), and the morphology of the graphene has distinct edge.

4. Conclusions

Carbon black was prepared by pyrolysis of propane using different plasma gases. The effects of plasma gases on the morphology and the structure of carbon black were investigated. We found that carbon black prepared by argon plasma exhibits the biggest particle size but the worst quality due to the deposition of abundant amorphous carbon. The carbon black prepared by hydrogen plasma shows the smallest particle size but the highest thermal stability because the surface is the cleanest. The carbon black prepared by nitrogen plasma exhibits the best quality. Unfortunately, HCN was found when using nitrogen as plasma gas by both the thermodynamics computations and the experimental investigations. The concentration of HCN increased with increasing current and amounts of propane but ceased to increase under certain current and propane content. At the same time, the distance between the electrodes also influenced the concentration of HCN. The presence of cyanide was confirmed by FT-IR and XPS analyses. The graphene could be found in the product when using argon as plasma gas with a small amount of hydrogen, and the content of graphene can be controlled by regulating the amount of hydrogen.

Data Availability

The data used to support the findings of this study are included within the article. Any more specific details on the data will be delivered by the corresponding author upon request.


The abstract of the submitted article had been presented at the 10th Annual Conference of China Particle Society and the Cross-Strait Particle Technology Seminar.

Conflicts of Interest

The authors declare that they do not have conflicts of interest.


This research was financially supported by the Foundation of Jiangsu Provincial Engineering Laboratory for Advanced Materials of Salt Chemical Industry (No. 82317070), the National Natural Science Foundation of China (NSFC, No. 21246002), the Minjiang Scholarship of Fujian Province, and the Central-Government Guided Special Funds for Local Economic Development (No. 830170778).


  1. J. Gonzalez-Aguilar, M. Moreno, and L. Fulcheri, “Carbon nanostructures production by gas-phase plasma processes at atmospheric pressure,” Journal of Physics D: Applied Physics, vol. 40, no. 8, pp. 2361–2374, 2007. View at: Publisher Site | Google Scholar
  2. W. Cho, S.-H. Lee, W.-S. Ju, Y. Baek, and J. K. Lee, “Conversion of natural gas to hydrogen and carbon black by plasma and application of plasma carbon black,” Catalysis Today, vol. 98, no. 4, pp. 633–638, 2004. View at: Publisher Site | Google Scholar
  3. E. Bormashenko, R. Pogreb, A. Musin, R. Balter, G. Whyman, and D. Aurbach, “Interfacial and conductive properties of liquid marbles coated with carbon black,” Powder Technology, vol. 203, no. 3, pp. 529–533, 2010. View at: Publisher Site | Google Scholar
  4. J. Yan, T. Wei, B. Shao et al., “Electrochemical properties of graphene nanosheet/carbon black composites as electrodes for supercapacitors,” Carbon, vol. 48, no. 6, pp. 1731–1737, 2010. View at: Publisher Site | Google Scholar
  5. M. S. Mauter and M. Elimelech, “Environmental applications of carbon-based nanomaterials,” Environmental Science & Technology, vol. 42, no. 16, pp. 5843–5859, 2008. View at: Publisher Site | Google Scholar
  6. F. Wang, R. Y. Hong, W. G. Feng, D. Badami, and K. Zeng, “Electrical and mechanical properties of ABS/EPDM composites filled with carbon black,” Materials Letters, vol. 125, pp. 48–50, 2014. View at: Publisher Site | Google Scholar
  7. N. K. V. Nadimpalli, V. S. Buddhiraju, and V. Runkana, “Modeling and simulation of carbon black synthesis in an aerosol flame reactor,” Advanced Powder Technology, vol. 22, no. 1, pp. 141–149, 2011. View at: Publisher Site | Google Scholar
  8. M. Ono-Ogasawara and T. Myojo, “Characteristics of multi-walled carbon nanotubes and background aerosols by carbon analysis; particle size and oxidation temperature,” Advanced Powder Technology, vol. 24, no. 1, pp. 263–269, 2013. View at: Publisher Site | Google Scholar
  9. D. L. Sun, F. Wang, R. Y. Hong, and C. R. Xie, “Preparation of carbon black via arc discharge plasma enhanced by thermal pyrolysis,” Diamond and Related Materials, vol. 61, pp. 21–31, 2016. View at: Publisher Site | Google Scholar
  10. M. Inada, N. Enomoto, J. Hojo, and K. Hayashi, “Structural analysis and capacitive properties of carbon spheres prepared by hydrothermal carbonization,” Advanced Powder Technology, vol. 28, no. 3, pp. 884–889, 2017. View at: Publisher Site | Google Scholar
  11. Y. B. Fainberg, “Plasma electronics and plasma methods of charged particle acceleration,” Plasma Physics Reports, vol. 20, pp. 549–554, 1994. View at: Google Scholar
  12. L. Bromberg, D. R. Cohn, A. Rabinovich et al., Onboard Plasmatron Hydrogen Production for Improved Vehicles, Massachusetts institute of Technology MIT Plasma Science and Fushion Center, 2006.
  13. T. Kappes, W. Schiene, and T. Hammer, “Energy balance of a dielectric barrier discharge reactor for hydrocarbon steam reforming,” in 8th International Symposium on High Pressure Low Temperature Plasma Chemestry proceedings, p. 49, Hakone, Japan, 2002. View at: Google Scholar
  14. T. Paulmier and L. Fulcheri, “Use of non-thermal plasma for hydrocarbon reforming,” Chemical Engineering Journal, vol. 106, no. 1, pp. 59–71, 2005. View at: Publisher Site | Google Scholar
  15. J. M. Cormier and I. Rusu, “Syngas production via methane steam reforming with oxygen: plasma reactors versus chemical reactors,” Journal of Physics D: Applied Physics, vol. 34, no. 18, pp. 2798–2803, 2001. View at: Publisher Site | Google Scholar
  16. M. Sobacchi, A. Saveliev, A. Fridman, L. A. Kennedy, S. Ahmed, and T. Krause, “Experimental assessment of a combined plasma/catalytic system for hydrogen production via partial oxidation of hydrocarbon fuels,” International Journal of Hydrogen Energy, vol. 27, no. 6, pp. 635–642, 2002. View at: Publisher Site | Google Scholar
  17. L. A. Arce-Saldaña, E. Espinoza-Mosso, B. Castro-Rodríguez et al., “Plasma synthesis of carbon powder with embedded Fe3C nanoparticles for magnetic separation of biomolecules,” Advanced Powder Technology, vol. 29, no. 4, pp. 1035–1041, 2018. View at: Publisher Site | Google Scholar
  18. V. D. Rusanov, A. I. Babaritskii, E. N. Gerasimov et al., “Stimulation of the partial oxidation of methane in a microwave discharge,” Doklady Physics, vol. 48, no. 3, pp. 119–122, 2003. View at: Publisher Site | Google Scholar
  19. A. I. Babaritskii, I. E. Baranov, M. B. Bibikov et al., “Partial hydrocarbon oxidation processes induced by atmospheric-pressure microwave-discharge plasma,” High Energy Chemistry, vol. 38, no. 6, pp. 407–411, 2004. View at: Publisher Site | Google Scholar
  20. S. Asai, Y. Sekine, K. Urasaki, E. Kikuchi, M. Matsukata, and S. Kado, “Development of liquid fuel reformer using low energy pulse (LEP) discharge at room temperature,” in Asian Pacific Confederation of Chemical Engineering Congress Program, pp. 255–255, 2004. View at: Publisher Site | Google Scholar
  21. F. Fabry, G. Flamant, and L. Fulcheri, “Carbon black processing by thermal plasma. Analysis of the particle formation mechanism,” Chemical Engineering Science, vol. 56, no. 6, pp. 2123–2132, 2001. View at: Publisher Site | Google Scholar
  22. G. Petitpas, J.-D. Rollier, A. Darmon, J. Gonzalez-Aguilar, R. Metkemeijer, and L. Fulcheria, “A comparative study of non-thermal plasma assisted reforming technologies,” International Journal of Hydrogen Energy, vol. 32, no. 14, pp. 2848–2867, 2007. View at: Publisher Site | Google Scholar
  23. J. R. Rose, “Process of and apparatus for producing carbon and gaseous fuel,” 1920, US Patent US3420632. View at: Google Scholar
  24. N. W. Ryan, “Production of carbon black using plasma-heated nitrogen,” 1969, US Patent US3420632. View at: Google Scholar
  25. M. K. Nikoo and N. A. S. Amin, “Thermodynamic analysis of carbon dioxide reforming of methane in view of solid carbon formation,” Fuel Processing Technology, vol. 92, no. 3, pp. 678–691, 2011. View at: Publisher Site | Google Scholar
  26. R. Hong, Z. Ren, J. Ding, and H. Li, “Experimental investigation and particle dynamic simulation for synthesizing titania nanoparticles using diffusion flame,” Chemical Engineering Journal, vol. 108, no. 3, pp. 203–212, 2005. View at: Publisher Site | Google Scholar
  27. L. Chen, R. Y. Hong, and H. Li, “Thermodynamic investigation of plasma pyrolysis of hydrocarbon,” Computers and Applied Chemistry, vol. 24, no. 6, 2007. View at: Google Scholar
  28. F. Wang, D. L. Sun, R. Y. Hong, and M. R. Kumar, “Preparation of carbon nanoparticles by plasma arc discharge under fluidized dynamic equilibrium,” Journal of Nanoparticle Research, vol. 18, no. 6, 2016. View at: Publisher Site | Google Scholar
  29. D. Bittner, H. Baumann, and J. Klein, “Relation between coal properties and acetylene yield in plasma pyrolysis,” Fuel, vol. 64, no. 10, pp. 1370–1374, 1985. View at: Publisher Site | Google Scholar
  30. J. C. Pereira-Lima, J. V. Busnello, C. Saul et al., “High power setting argon plasma coagulation for the eradication of Barrett’s esophagus,” American Journal of Gastroenterology, vol. 95, no. 7, pp. 1661–1668, 2000. View at: Google Scholar
  31. B. Yan, P. Xu, C. Y. Guo, Y. Jin, and Y. Cheng, “Experimental study on coal pyrolysis to acetylene in thermal plasma reactors,” Chemical Engineering Journal, vol. 207-208, pp. 109–116, 2012. View at: Publisher Site | Google Scholar
  32. X. Y. Liu, R. Y. Hong, W. G. Feng, and D. Badami, “Synthesis of structure controlled carbon nanomaterials by AC arc plasma process,” Powder Technology, vol. 256, pp. 158–165, 2014. View at: Publisher Site | Google Scholar
  33. S. Zhao, R. Hong, Z. Luo, H. Lu, and B. Yan, “Carbon nanostructures production by AC arc discharge plasma process at atmospheric pressure,” Nanomaterials, vol. 2011, Article ID 346206, 6 pages, 2011. View at: Publisher Site | Google Scholar
  34. W. Zhang and Y. Catherine, “Deposition of carbon films by the dissociation of methane in r.f. discharge,” Surface and Coatings Technology, vol. 47, no. 1-3, pp. 69–83, 1991. View at: Publisher Site | Google Scholar
  35. C. R. Houska and B. E. Warren, “X-ray study of the graphitization of carbon black,” Journal of Applied Physics, vol. 25, no. 12, pp. 1503–1509, 1954. View at: Publisher Site | Google Scholar
  36. B. R. Locke, M. Sato, P. Sunka, M. R. Hoffmann, and J. S. Chang, “Electrohydraulic discharge and nonthermal plasma for water treatment,” Industrial and Engineering Chemistry Research, vol. 45, no. 3, pp. 882–905, 2006. View at: Publisher Site | Google Scholar
  37. R. Saito, G. Dresselhaus, and M. S. Dresselhaus, “Physical Properties of Carbon Nanotubes,” in World Scientific Publishing Company, 1998. View at: Google Scholar
  38. K.-J. Cho, J.-T. Ryu, Y.-G. Baek et al., “Fabrication and characteristics of amorphous carbon films grown in pure methane plasma by using radio frequency plasma enhanced chemical vapor deposition,” Journal of Applied Physics, vol. 42, Part 1, pp. 1744–1748, 2003. View at: Publisher Site | Google Scholar
  39. M. Kumar and Y. Ando, “Single-wall and multi-wall carbon nanotubes from camphor—a botanical hydrocarbon,” Diamond and Related Materials, vol. 12, no. 10-11, pp. 1845–1850, 2003. View at: Publisher Site | Google Scholar
  40. A. R. Bunsell, “Fibre reinforcements for composite materials and electron microscopy,” Microscopy Microanalysis Microstructures, vol. 2, no. 1, pp. 1–13, 1991. View at: Publisher Site | Google Scholar
  41. Y. Lin, T. W. Smith, and P. Alexandridis, “Adsorption of a rake-type siloxane surfactant onto carbon black nanoparticles dispersed in aqueous media,” Langmuir, vol. 18, no. 16, pp. 6147–6158, 2002. View at: Publisher Site | Google Scholar
  42. L. Xie, L. Jiao, and H. Dai, “Selective etching of graphene edges by hydrogen plasma,” Journal of the American Chemical Society, vol. 132, no. 42, pp. 14751–14753, 2010. View at: Publisher Site | Google Scholar
  43. K. Nakamura, M. Fujitsuka, and M. Kitajima, “Disorder-induced line broadening in first-order Raman scattering from graphite,” Physical Review B, vol. 41, no. 17, pp. 12260–12263, 1990. View at: Publisher Site | Google Scholar
  44. W. Li, H. Zhang, C. Wang et al., “Raman characterization of aligned carbon nanotubes produced by thermal decomposition of hydrocarbon vapor,” Applied Physics Letters, vol. 70, no. 20, pp. 2684–2686, 1997. View at: Publisher Site | Google Scholar
  45. X. B. Ai, H. Bai, L. H. Zhao, D. Q. Cang, and Q. Tang, “Thermodynamic analysis and formula optimization of steel slag-based ceramic materials by FACTsage software,” International Journal of Minerals, Metallurgy, and Materials, vol. 20, no. 4, pp. 379–385, 2013. View at: Publisher Site | Google Scholar
  46. L. Fulcheri, N. Probst, G. Flamant, F. Fabry, E. Grivei, and X. Bourrat, “Plasma processing: a step towards the production of new grades of carbon black,” Carbon, vol. 40, no. 2, pp. 169–176, 2002. View at: Publisher Site | Google Scholar
  47. H. Estrade-Szwarckopf, “XPS photoemission in carbonaceous materials: a “defect” peak beside the graphitic asymmetric peak,” Carbon, vol. 42, no. 8-9, pp. 1713–1721, 2004. View at: Publisher Site | Google Scholar
  48. S. Biniak, G. Szymański, J. Siedlewski, and A. Światkowski, “The characterization of activated carbons with oxygen and nitrogen surface groups,” Carbon, vol. 35, no. 12, pp. 1799–1810, 1997. View at: Publisher Site | Google Scholar
  49. X. C. LeQuan, W. P. Kang, J. L. Davidson, M. Guo, and B. K. Choi, “Micro-Raman, SEM, XPS, and electron field emission characterizations of nitrogen-induced shallow defects on nanodiamond films fabricated with different growth parameters,” Diamond and Related Materials, vol. 18, no. 2-3, pp. 191–195, 2009. View at: Publisher Site | Google Scholar
  50. R. J. J. Jansen and H. van Bekkum, “XPS of nitrogen-containing functional groups on activated carbon,” Carbon, vol. 33, no. 8, pp. 1021–1027, 1995. View at: Publisher Site | Google Scholar

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