# Fabrication and Characterization of Carbon-Based Nanofluids through the Water Vortex Trap Method

Authors: Ching-Min Cheng; Shang-Pang Yu; Tun-Ping Teng
Journal: Journal of Nanomaterials
 (2018)

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## Abstract

This study designed an efficient one-step method for synthesizing carbon-based nanofluids (CBNFs). The method employs the vortex trap method (VTM) and an oxygen-acetylene flame, serving as a carbon source, in a manufacturing system of the VTM (MSVTM). The flow rate ratio of O2 and C2H2 was adjusted to form suitable combustion conditions for the reduced flame. Four flow rate ratios of O2 and C2H2 were used: 1.5 : 2.5 (V1), 1.0 : 2.5 (V2), 0.5 : 2.5 (V3), and 0 : 2.5 (V4). The morphology, structure, particle size, stability, and basic physicochemical characteristics of the obtained carbon-based nanomaterials (CBNMs) and CBNFs were investigated using transmission electron microscopy, field-emission scanning electron microscopy, X-ray diffraction, Raman spectrometry, ultraviolet–visible–near-infrared spectrophotometry, and a particle size-zeta potential analyzer. The static positioning method was utilized to evaluate the stability of the CBNFs with added EP dispersants. The evaluation results revealed the morphologies, compositions, and concentrations of the CBNFs obtained using various process parameters, and the relation between processing time and production rate was determined. Among the CBNMs synthesized, those obtained using the V4-0 flow rate ratio had the highest stability when no EP dispersant was added. Moreover, the maximum enhancement ratios of the viscosity and thermal conductivity were also obtained for V4-0: 4.65% and 1.29%, respectively. Different types and concentrations of dispersants should be considered in future research to enhance the stability of CBNFs for further application.


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## Body

## 1. Introduction

Nanofluids (NFs) are solid-liquid mixtures containing nanoscale materials such as nanoparticles (NPs), nanofibers, nanotubes, nanowires, nanorods, nanosheets, and droplets. The base fluids are commonly used fluids such as ethylene glycol (EG), mineral oil, or a mixture of various liquids (e.g., EG and water or water and propylene glycol) [1, 2]. The primary advantage of NFs is that they have superior thermophysical properties to conventionally used fluids. These superior thermophysical properties result in higher efficiency of their heat exchange [3, 4]. Moreover, the addition of nanoscale particles to NFs can result in considerably lower pressure drops, blocks, wear, and energy consumption in heat exchange system pipelines, thereby improving the availability of NFs. Therefore, NFs have numerous potential applications in engineering, especially in the fields of electromechanics, air conditioning, automobiles, manufacturing, machining, solar energy, building structures, and biomedicine [5–10].The NF synthesis methods can be divided into two categories—one-step and two-step methods. In the one-step method, NPs are directly synthesized in base fluids; thus, the synthesized NFs have high stability. However, the geometric appearance and size of the NPs and the concentration of the NFs are limited. In the two-step method, NPs are synthesized in advance and then distributed in the base fluid to form an NF. The concentration and particle size distribution of the NFs produced in the two-step method can be easily controlled; however, these NFs have low stability. Therefore, it is crucial to improve the long-term stability of NFs by adding dispersants and conducting pH control, mechanical stirring, and dispersion [5, 11].The one-step methods for producing NFs, such as sputtering arc discharge, laser ablation, water-assisted synthesis, and flame synthesis, are the most common. Ishida et al. [12] prepared thiolate-protected fluorescent silver NPs by conducting sputtering deposition onto a liquid matrix. Nguyen et al. [13, 14] synthesized Ag–Au alloy NPs in a liquid by utilizing a novel approach known as double target sputtering. This method allows the manipulation of NP composition, size, and optical properties by controlling the sputter parameters for each metal target. Farajimotlagh et al. [15] synthesized η-Al2O3 NPs by conducting direct-current arc discharge in ethanol and methanol, which are environmentally friendly liquid carrier media. The size of the synthesized NPs was between 37 and 50 nm. Hayashi et al. [16] prepared hydrophilic carbon NPs (CNPs) from amino acids by conducting pulsed arc discharge over an aqueous solution surface under pressurized argon at 4 MPa. This method produced CNPs that were highly dispersible in water because the amino acids provided hydrophilic groups. Zhang et al. [17] efficiently prepared silver NPs by using large-area arc discharge in a liquid. The minimum size of the synthesized silver NPs was 33 nm. Amans et al. [18] reviewed the nanocarbon material preparation methods that employed a pulse laser in a liquid. Palazzo et al. [19] prepared “naked” gold NPs (AuNPs) in the absence of capping agents by performing pulsed laser ablation in a liquid; these AuNPs were stabilized by negative charges. Krstulović et al. [20] prepared colloidal Al-doped ZnO NPs by using Nd:YAG pulsed laser ablation of a ZnO:Al2O3 target with two laser wavelengths (1064 and 532 nm) in a water medium. The size of the synthesized Al-doped ZnO NPs was between 20 and 30 nm. Sathya et al. [21] presented a simple, one-step approach named microwave-assisted synthesis for the preparation of water-dispersible magnetic nanoclusters (MNCs) of superparamagnetic iron oxide; this method involved reducing Fe2(SO4)3 in sodium acetate, polyethylene glycol, and EG within a microwave reactor. The average size of the MNCs increased from 27 to 52 nm as the reaction time was increased from 10 to 600 s. Golestan et al. [22, 23] studied nanocatalysts that were synthesized through a hydrothermal procedure in a fixed-bed reactor. Teng et al. [24] fabricated nanocarbon-based NFs using the oxygen-acetylene flame synthesis method. By adjusting the oxygen-acetylene ratio, the size of the synthesized CNPs was varied between 20 and 30 nm. In the present study, the oxygen-acetylene flame synthesis method was employed to produce CNPs, and hybrid NFs were collected using vortex trap equipment. This method is a fast, efficient, simple, and energy-conserving approach to the synthesis of carbon NFs.In recent years, numerous studies of materials such as nanocarbons, carbon nanotubes, and graphene have been conducted and have discovered that these materials have high thermal conductivity [25–28], excellent heat transfer performance [29, 30], and physical properties that are unique for such materials [21–34]. Therefore, carbon-based nanomaterials are one of the most popular research areas. This study employed the vortex trap method (VTM) with an oxygen (O2)–acetylene (C2H2) flame as the carbon source to develop a manufacturing system of the VTM (MSVTM) for fabricating carbon-based NFs (CBNFs) through the one-step synthesis method. The MSVTM has features such as a simplistic system design, low-cost production, convenient and safe manufacturing procedures, and no requirement of additional chemicals. Moreover, the CBNFs produced using the one-step synthesis method generally have high suspension performance because of the optimal surface wettability of the suspended nanoparticles. The MSVTM was used at various flow rate ratios of O2 and C2H2 to produce varying combustion conditions of the reduced flame. The morphology, structure, particle size, suspension performance, and basic physicochemical characteristics of the carbon-based nanomaterials (CBNMs) and CBNFs were investigated by utilizing appropriate techniques such as transmission electron microscopy (TEM), field-emission scanning electron microscopy (FE-SEM), X-ray diffraction (XRD), Raman spectrometry, ultraviolet–visible–near-infrared spectrophotometry (UV–Vis–NIR), and a particle size-zeta potential analyzer. Moreover, the feasibility of manufacturing CBNFs by using the MSVTM was evaluated.


## 2. Preparation of CBNFs

The one-step synthesis method known as the VTM was employed to prepare CBNFs. The layout of the MSVTM for synthesizing CBNFs is displayed in Figure1. An O2–C2H2 flame was utilized as the carbon source. The MSVTM comprised curved baffles, baffles with a labyrinth structure, a jagged baffle, a smoke cover, a collection tank, an exhaust fan, a digital mass flow controller (MFC), an electromagnetic stirrer, and an O2–C2H2 torch. As shown in Figure 1, filtered tap water was placed in the collection tank. Subsequently, the electromagnetic stirrer (HMS-102, FARGO, Taiwan) was turned on at approximately 500 rpm to create a disturbance in the water and to increase the cooling and collection efficiency on the water surface for suspended particles in air at stage 1. Finally, the exhaust fan was switched on to produce air flow (approximately 0.2 m3/s), which generated negative pressure in the MSVTM and sucked air from the front of the jagged baffle. Due to the asymmetric shape of the jagged baffle’s holes and the change in the internal structure and configuration of the jagged baffle, a strong disturbance was caused in the intake air of the MSVTM. Moreover, the strong disturbance in the intake air produced a vortex that splashed the water to cool and collect the suspended particles in the air. An MFC was used to control the flow rate and O2–C2H2 ratio, while a flame was produced using the O2–C2H2 torch. The O2–C2H2 flame was used as a carbon source and was lit under a smoke cover over the water surface. The smoke generated by the O2–C2H2 flame was sucked into the MSVTM. Therefore, the smoke was cooled and condensed by the disturbed water (stage 1) and splashing water (stages 2 and 3) to form a CBNM. When the mixture of CBNM and water had flowed into the collection tank, CBNFs were produced. This CBNF manufacturing technology has considerable potential.Figure 1
Schematic of the MSVTM for preparing CBNFs.The manufacturing process parameters of the MSVTM for yielding CBNFs are detailed as follows. The amount of water in the collection tank was 2 L for each process; the C2H2 flow rate was fixed at 2.5 L/min at a pressure of 1.5 kg/cm2; and the O2 flow rate was controlled in the range 0–1.5 L/min at a pressure of 3.0 kg/cm2. The flow ratio and pressure settings of C2H2 and O2 were based on the settings used in previous studies [24]. The O2–C2H2 fuel was employed in four flow ratio configurations—V1 (1.5 : 2.5), V2 (1.0 : 2.5), V3 (0.5 : 2.5), and V4 (0 : 2.5). The flame was a reduction flame because the O2 proportion was lower than the C2H2 proportion. An increase in the proportion of oxygen in the O2–C2H2 flame was expected to result in more complete combustion, less smog, and less CBNM. In this study, each flow ratio configuration was employed for 3, 6, 9, and 12 min; thus, a total of 16 CBNF samples were obtained. In the combustion process, some water vaporized; thus, water was frequently replenished to maintain the water level in the tank. When the CBNFs were removed from the collection tank, 1 L of water was slowly poured into the collection tank to drain the carbon attached to the collection tank. The volume of CBNFs yielded per process parameter and time configuration was approximately 3 L.To improve the suspension and dispersion performance of the CBNMs in water, the collected CBNFs were stirred using a stirrer/hot plate (PC420D, Corning, USA) operated at 450 rpm for 2 h, after which they were homogenized at 5000 rpm for 20 min using a homogenizer (YOM300D, Yotec, Taiwan). Subsequently, the CBNFs were bathed in an ultrasonic bath (5510R-DTH, Branson, USA) for 30 min and then subjected to an intermittent oscillation process (35% amplitude, on/off duty cycle was 30/10 s) by using an ultrasonic liquid processor (Q700, Qsonica, USA) for 10 min. By using these dispersing devices consecutively and three times for short periods, temperature increases in the dispersing devices and the CBNFs were effectively prevented, thus achieving excellent dispersion. This technique was employed on the basis of the authors’ research experience. Figure2(a) displays photographs of the CBNFs fabricated using various process configurations. In contrast to the V1 CBNFs, which were almost transparent, the other CBNFs were dark. Figure 2(b) displays all the samples that were statically placed for 48 h to evaluate their suspension status; the V2 CBNFs exhibited obvious sedimentation. After dispersed CBNFs were produced, they were subjected to a series of examinations for determining their characteristics.Figure 2
Photographs of CBNFs obtained using various process parameter configurations.
(a)
Initial state (b)
After 48 hours


## 3. Evaluation of the Characteristics of the CBNFs

### 3.1. Morphology, Crystallization, and Structure Analyses

TEM (H-7100, Hitachi, Japan) and FE-SEM (JSM-7610F, JEOL, Japan) were used to identify the morphologies of the obtained CBNMs in the CBNFs. The shapes and sizes of the CBNMs were determined. The crystallization of the CBNMs was analyzed using XRD (D8 Advanced, Bruker, Germany) with Cu Kα radiation. Raman spectroscopy (532.15 nm, NRS 4100, Jasco, Japan) was employed to detect the Raman shift in the D and G peaks of the CBNM spectra. The CBNFs were placed on glass sheets (20 × 20 × 0.6 mm3) and dried by heating to form carbon films in advance of conducting XRD and Raman spectroscopy. Because the concentrations of the V1 CBNFs were extremely low, a vacuum concentrator was used to increase the concentration of the test samples for all the aforementioned measurements.


### 3.2. Production Rate Analysis

The CBNM production rate for each process parameter configuration was measured for determining the concentration of CBNMs in the CBNFs [24]. A moisture analyzer (MX-50, A&D, Japan) was used to remove moisture from a 25 g sample of each CBNF by heating, and the remaining weight was utilized (weighing method) to estimate the CBNM concentration in the CBNF sample. Samples were weighed before and after drying. Because the highest resolution of the moisture analyzer was only 1.0 mg, a high-precision electronic balance (0.01 mg/42 g, GR202, A&D, Japan) was employed to improve the weighing accuracy. The entire weighing procedure was repeated four times, and the average value of test data was calculated to determine the CBNM content weight of a CBNF for each process parameter configuration. Finally, the actual weight concentration in each CBNF was obtained from the CBNM content weight and CBNF sample weight.


### 3.3. Stability Analysis

To appropriately employ the stability test and facilitate the stability comparison (suspension and dispersion performance), samples that were synthesized using various process parameters were adjusted to the same concentration by diluting with water or concentrating with a vacuum concentrator, because the concentrations of all the CBNFs were not equal. Moreover, if a CBNF had poor stability, the accuracy and reliability of the characteristic measurements were affected. Figure2 displays that V2 had poor stability, and obvious sedimentation was observed through static positioning. Hence, the stability of each sample was tested by adding a nonionic dispersant (EP dispersant, polyoxyethylene alkyl ether; EP9050, First Chemical, Taiwan) in various concentrations. The samples with optimal stability were subjected to the following measurements of particle size (dp), zeta potential (ζ), and basic physicochemical characteristics. To determine their stability, the CBNFs were mainly tested using static positioning and UV–Vis–NIR (V670, Jasco, Japan). An elaborate account of the static positioning method is provided as follows. First, a CBNF was placed into a transparent sample bottle, and the sediment difference was visually observed after 120 h. To measure the difference in the absorbance at the initial (ABSi) and static position for each CBNF after 48 h (ABS48h), UV–Vis–NIR combined with static positioning (2.5-mL CBNF sample in a transparent cuvette) was performed. The absorbance difference ratio (RABS) was calculated using (1) and utilized to determine the stability of the CBNF. A lower RABS represents a higher CBNF stability. (1)RABS=ABSi-ABS48hABSi×100%.Moreover, the stability of a CBNF can be evaluated using the suspendeddp distribution, average suspended dp, and ζ. The suspended dp of CBNMs is similar to the dp is observed using electron microscopy, thus indicating the favorable dispersion of the CBNMs in the CBNFs. Moreover, the larger the absolute value of ζ, the higher the stability of an CBNF. The ζ values of the colloidal dispersions were within the ranges 0 to ±10, ±10 to ±30, ±30 to ±40, and ±40 to ±60 mV; these values indicated rapid coagulation or flocculation, incipient instability, moderate stability, and favorable stability, respectively. When the magnitude of the ζ of a NF is greater than 60 mV, the colloidal dispersion has excellent stability [35, 36]. The dynamic light-scattering method was conducted for dp and ζ analysis. A CBNF into which a 6 mm gold-plated electrode cell was placed was simultaneously measured by using a nanoparticle analyzer (SZ-100, HORIBA, Japan) to evaluate the average dp, the dp distribution, and ζ. The dp and ζ values for each CBNF were measured five times, and the average dp and ζ were then calculated.


### 3.4. Basic Physicochemical Characteristic Measurements

The basic physicochemical characteristics measured for the CBNFs were pH, electrical conductivity (E), density (ρ), viscosity (μ), and thermal conductivity (k), which were measured using a pH meter (SensION+ MM374, Hack, USA) with an accuracy of ±0.002 pH and ±0.5%, an electrical conductivity meter (SensION+ MM374), a liquid density meter (DA-130N, KEM, Japan) with an accuracy of ±0.001 g/mL, a viscosity meter (T15-3, Hydramotion, England) with an accuracy of ±1.0%, and a thermal properties analyzer (KD-2 Pro, Decagon Devices, USA) with an accuracy of ±5.0%, respectively. These measurements were made in an isothermal bath (P-20, YSC, Taiwan) to provide individual sample temperature control of 30, 40, or 50°C within ±0.5°C. To increase the experimental accuracy, these experiments were conducted six times, and the four most similar values were used to obtain the average.In a high-purity nitrogen (5 N) atmosphere, the specific heat (cp) of the test samples was measured using a differential scanning calorimeter (DSC, Q20, TA, USA) with a mechanical refrigeration system (RCS40, TA, USA). The temperature and calorimetric accuracies of the DSC were ±0.1°C and ±1.0%, respectively. The cp test method used was the standard reference approach, and the standard reference was pure water [37]. The experimental temperature was between 10 and 80°C, and the heating rate was maintained at 10°C/min. To increase the measurement accuracy, the experiments were conducted thrice for each CBNF, and the average cp value of the CBNF was then calculated.


### 3.5. Data Analysis

The experimental results were transformed into a change ratio (CR) for comparison of water with the CBNFs; the CR can be expressed as(2)CR=DCBNFs-DwDw×100%.


## 3.1. Morphology, Crystallization, and Structure Analyses

TEM (H-7100, Hitachi, Japan) and FE-SEM (JSM-7610F, JEOL, Japan) were used to identify the morphologies of the obtained CBNMs in the CBNFs. The shapes and sizes of the CBNMs were determined. The crystallization of the CBNMs was analyzed using XRD (D8 Advanced, Bruker, Germany) with Cu Kα radiation. Raman spectroscopy (532.15 nm, NRS 4100, Jasco, Japan) was employed to detect the Raman shift in the D and G peaks of the CBNM spectra. The CBNFs were placed on glass sheets (20 × 20 × 0.6 mm3) and dried by heating to form carbon films in advance of conducting XRD and Raman spectroscopy. Because the concentrations of the V1 CBNFs were extremely low, a vacuum concentrator was used to increase the concentration of the test samples for all the aforementioned measurements.


## 3.2. Production Rate Analysis

The CBNM production rate for each process parameter configuration was measured for determining the concentration of CBNMs in the CBNFs [24]. A moisture analyzer (MX-50, A&D, Japan) was used to remove moisture from a 25 g sample of each CBNF by heating, and the remaining weight was utilized (weighing method) to estimate the CBNM concentration in the CBNF sample. Samples were weighed before and after drying. Because the highest resolution of the moisture analyzer was only 1.0 mg, a high-precision electronic balance (0.01 mg/42 g, GR202, A&D, Japan) was employed to improve the weighing accuracy. The entire weighing procedure was repeated four times, and the average value of test data was calculated to determine the CBNM content weight of a CBNF for each process parameter configuration. Finally, the actual weight concentration in each CBNF was obtained from the CBNM content weight and CBNF sample weight.


## 3.3. Stability Analysis

To appropriately employ the stability test and facilitate the stability comparison (suspension and dispersion performance), samples that were synthesized using various process parameters were adjusted to the same concentration by diluting with water or concentrating with a vacuum concentrator, because the concentrations of all the CBNFs were not equal. Moreover, if a CBNF had poor stability, the accuracy and reliability of the characteristic measurements were affected. Figure2 displays that V2 had poor stability, and obvious sedimentation was observed through static positioning. Hence, the stability of each sample was tested by adding a nonionic dispersant (EP dispersant, polyoxyethylene alkyl ether; EP9050, First Chemical, Taiwan) in various concentrations. The samples with optimal stability were subjected to the following measurements of particle size (dp), zeta potential (ζ), and basic physicochemical characteristics. To determine their stability, the CBNFs were mainly tested using static positioning and UV–Vis–NIR (V670, Jasco, Japan). An elaborate account of the static positioning method is provided as follows. First, a CBNF was placed into a transparent sample bottle, and the sediment difference was visually observed after 120 h. To measure the difference in the absorbance at the initial (ABSi) and static position for each CBNF after 48 h (ABS48h), UV–Vis–NIR combined with static positioning (2.5-mL CBNF sample in a transparent cuvette) was performed. The absorbance difference ratio (RABS) was calculated using (1) and utilized to determine the stability of the CBNF. A lower RABS represents a higher CBNF stability. (1)RABS=ABSi-ABS48hABSi×100%.Moreover, the stability of a CBNF can be evaluated using the suspendeddp distribution, average suspended dp, and ζ. The suspended dp of CBNMs is similar to the dp is observed using electron microscopy, thus indicating the favorable dispersion of the CBNMs in the CBNFs. Moreover, the larger the absolute value of ζ, the higher the stability of an CBNF. The ζ values of the colloidal dispersions were within the ranges 0 to ±10, ±10 to ±30, ±30 to ±40, and ±40 to ±60 mV; these values indicated rapid coagulation or flocculation, incipient instability, moderate stability, and favorable stability, respectively. When the magnitude of the ζ of a NF is greater than 60 mV, the colloidal dispersion has excellent stability [35, 36]. The dynamic light-scattering method was conducted for dp and ζ analysis. A CBNF into which a 6 mm gold-plated electrode cell was placed was simultaneously measured by using a nanoparticle analyzer (SZ-100, HORIBA, Japan) to evaluate the average dp, the dp distribution, and ζ. The dp and ζ values for each CBNF were measured five times, and the average dp and ζ were then calculated.


## 3.4. Basic Physicochemical Characteristic Measurements

The basic physicochemical characteristics measured for the CBNFs were pH, electrical conductivity (E), density (ρ), viscosity (μ), and thermal conductivity (k), which were measured using a pH meter (SensION+ MM374, Hack, USA) with an accuracy of ±0.002 pH and ±0.5%, an electrical conductivity meter (SensION+ MM374), a liquid density meter (DA-130N, KEM, Japan) with an accuracy of ±0.001 g/mL, a viscosity meter (T15-3, Hydramotion, England) with an accuracy of ±1.0%, and a thermal properties analyzer (KD-2 Pro, Decagon Devices, USA) with an accuracy of ±5.0%, respectively. These measurements were made in an isothermal bath (P-20, YSC, Taiwan) to provide individual sample temperature control of 30, 40, or 50°C within ±0.5°C. To increase the experimental accuracy, these experiments were conducted six times, and the four most similar values were used to obtain the average.In a high-purity nitrogen (5 N) atmosphere, the specific heat (cp) of the test samples was measured using a differential scanning calorimeter (DSC, Q20, TA, USA) with a mechanical refrigeration system (RCS40, TA, USA). The temperature and calorimetric accuracies of the DSC were ±0.1°C and ±1.0%, respectively. The cp test method used was the standard reference approach, and the standard reference was pure water [37]. The experimental temperature was between 10 and 80°C, and the heating rate was maintained at 10°C/min. To increase the measurement accuracy, the experiments were conducted thrice for each CBNF, and the average cp value of the CBNF was then calculated.


## 3.5. Data Analysis

The experimental results were transformed into a change ratio (CR) for comparison of water with the CBNFs; the CR can be expressed as(2)CR=DCBNFs-DwDw×100%.


## 4. Results and Discussion

Figures3 and 4 display TEM and FE-SEM images of the CBNMs obtained using the four process flow ratio configurations (V1–V4) and processing times of 3 and 12 min. Spherical CBNMs (dp: approximately 20–50 nm) were synthesized mostly when the V2–V4 configurations were used, whereas flaky CBNMs were mostly obtained using V1. Flaky CBNMs were thus obtained when the proportion of O2 was increased. Conversely, a high proportion of C2H2 contributed to the formation of CBNMs with more spherical particles. Moreover, the processing time of the MSVTM was not discovered to affect the particle size and morphology of the CBNMs. The FE-SEM and TEM images of CBNMs indicate that processing time did not affect dp for parameter configurations V2–V4, but differences were observed when V1 was employed. Although FE-SEM and TEM images can partially display dp and morphology, a nanoparticle analyzer was required to confirm the dp distribution and average dp of the suspended CBNMs in CBNFs. Moreover, XRD and Raman spectroscopy were necessary to identify the material in the follow-up tests.Figure 3
TEM images of CBNMs obtained using various process parameters for processing time durations of (a) 3 and (b) 12 min.
(a) (b)Figure 4
FE-SEM images of CBNMs obtained using various process parameters for processing time durations of (a) 3 and (b) 12 min.
(a) (b)Figure5 displays XRD patterns of the CBNMs that were synthesized by employing V1–V4. The CBNMs could barely be distinguished. However, dissimilarities existed within the composition and crystalline state of the samples. By using XRD, we observed that the (001) diffraction peak was located at a 2θ value of 11° and that graphene oxide (GO) was the primary constituent of most of the CBNMs. The peaks at 2θ between 21° and 27° suggest that this range overlaps the (002) diffraction peak of graphite, which has a 2θ of 26.5°. A broad diffraction peak at 2θ between 23° and 24° is observed in Figure 5. In some materials, most of the functional groups had been removed, which provides clear evidence that some amount of reduced GO (RGO) was present in these CBNMs [38–40]. The CBNMs were generated by using an O2–C2H2 reduction flame, and reduction gases such as carbon monoxide were present in the combustion products of the reduction flame. Moreover, a very small amount of free oxygen was present to produce different degrees of reduction reactions. The reduction reaction caused the functional groups in the internal layers of GO to gradually disappear, and thus, GO was gradually reduced to RGO [38–40]. Furthermore, the crystallization of the CBNMs for various process parameters was inferior due to the broad range of the (002) diffraction peak. Hence, in this study, amorphous carbon (AC) was included, and different proportions of GO, RGO, and AC were required to synthesize CBNMs by using different process parameter configurations.Figure 5
XRD patterns of CBNMs obtained using various process parameter configurations.The Raman spectra displayed in Figure6 were used to determine the structure of the CBNMs synthesized using V1–V4. The test samples had three test points, and one of the three test points was chosen for Figure 6. Table 1 presents the average data obtained from the Raman spectra for the three test points. In the Raman spectra, the D and G peaks, located at approximately 1324–1346 cm−1 and 1490–1691 cm−1, respectively, are the predominant features [7, 41–44]. In general, the spectrum of pristine graphite has a prominent G peak at 1584.5 cm−1 that corresponds to first-order scattering of the E2g mode in the Brillouin zone. This indicates that the structure of graphite is regular [7, 42–45]. In the Raman spectrum of GO, the G peak is broadened and the D peak is prominent, thus indicating that the C=C bonds in the graphite layers are destroyed by oxidation and that several carbon atoms change from sp2- to sp3-hybridized carbon. The intensity ID/IG represents the ratio of sp3- and sp2-hybridized carbon atoms. In RGO, ID/IG is directly proportional to the number of sp3-hybridized atoms but inversely proportional to the number of sp2-hybridized atoms. Theoretically, ID/IG declines as GO is reduced to RGO. Moreover, a smaller ID/IG indicates more complete reduction of GO to RGO [41, 46]. However, when GO is incompletely reduced, ID is greater than IG. In addition, some studies have demonstrated that the reduction of GO to RGO by utilizing the chemical reduction method caused an increase in ID/IG [47–50]. This mainly occurs because reduction increases the number of small aromatic domains in GO, leading to an increase in the ID/IG ratio [47]. As shown in Figure 6 and Table 1, regardless of the processing time (3 or 12 min) and parameter configuration (V1–V4), the ID/IG ratio first increased and then decreased (the highest ID/IG ratio was obtained for V2).Table 1
Averaged Raman spectroscopy data for the CBNFs obtained using various process parameter configurations.
Item 3 min 12 min V1 V2 V3 V4 V1 V2 V3 V4 I D cm−1 1346.65 1336.04 1339.41 1349.34 1344.86 1337.61 1340.95 1342.19 Int. 230.48 184.43 118.52 51.25 194.21 205.81 297.88 71.23 I G cm−1 1592.65 1590.37 1589.41 1595.34 1589.86 1592.28 1587.61 1600.86 Int. 308.35 143.41 140.69 83.85 261.63 163.47 288.46 121.64 I 2 D cm−1 2639.65 2649.70 2634.74 2636.67 2651.86 2651.61 2638.95 2633.53 Int. 10.54 25.63 10.23 10.06 7.17 21.01 21.73 13.45 I D / I G 0.75 1.29 0.84 0.61 0.74 1.26 1.03 0.59 I 2 D / I G 0.03 0.18 0.07 0.12 0.03 0.13 0.08 0.11 Note. Data are the average of three measurement points for each sample.Figure 6
Raman spectra of CBNMs obtained using various process parameter configurations.This phenomenon may be attributed to the decreasing O2 ratio in the reduction flame. Reducing gases were increasingly generated due to the accumulation of combustion products. Thus, the GO reduction effect became stronger, and the proportion of RGO increased simultaneously. However, a reduction in the O2 ratio of the reduction flame weakens the GO reduction effect by causing a decrease in the flame temperature. Moreover, the I2D of GO and RGO is mostly negligible or zero. However, in this study, CBNMs should also consist of AC in terms of a clear and broad range of I2D observing in the CBNMs produced by some of the process parameters. Moreover, the CBNMs contained different ratios of GO, RGO, and AC, which is inferred by simultaneously considering the Raman spectra and XRD patterns. In addition, for a specific ratio of O2 and C2H2, the processing time only affected the production rate of CBNMs (CBNF concentration).Figure7 displays the concentrations of the CBNMs in the CBNFs, as measured using the weighing method for V2–V4. Despite utilization of the vacuum concentration method, the weighing equipment in the authors’ laboratory could not accurately detect the concentration of V1 CBNFs because this concentration was extremely low. Therefore, in the subsequent related experiments, the V1 CBNF samples were excluded. The V2, V3, and V4 configurations produced CBNM concentrations in the CBNFs of 0.0414, 0.0553, and 0.0239 wt.%, respectively, at a processing time of 12 min. The results revealed that, in addition to V4, the production rate (concentration in the CBNF) of CBNMs and the O2 flow rate were inversely proportional. Moreover, the production rate of all samples was directly proportional to the processing time. In the preparation procedure, the V4 configuration resulted in the most black smoke (V4 with the minimum addition of O2) and the highest CBNM production rate, despite the production rate being lower than that when V2 and V3 were used. The V4 configuration resulted in the generation of considerable smoke and the rapid formation of numerous carbon particles that aggregated on the water surface. While the liquid was being stirred with a magnetic stirrer (stage 1), it was challenging to dissolve these floating carbon particles on the water surface, which hindered the collection efficiency. Subsequently, the carbon particles were collected efficiently by the water vortex in stage 2. However, in stages 2 and 3, obtaining suitable collection efficiency for the V4 configuration was challenging because the carbon particles generated could not be appropriately collected in stage 1. The material analysis results indicated that processing time had no influence on the material obtained. In subsequent experiments, the V2–V4 samples obtained using a processing time of 12 min were adjusted to the same concentration (0.024 wt.%) for testing and comparison.Figure 7
Concentrations of CBNFs obtained using various process parameter configurations.Figure8 displays a photograph of the experimental results obtained after 120 h of static positioning for the V2–V4 samples at various dispersant concentrations. The CBNM concentrations for V2–V4 were 0.024 wt.%, and the numbers 0–5 in each process parameter in the figure represent EP dispersant concentrations of 0, 0.05, 0.1, 0.2, 0.4, and 0.8 wt.%, respectively. As shown in Figure 8, V2-0 had the worst stability, followed by V3-0. For the sample V4-0, the difference between before and after the static positioning cannot be identified by visual inspection. Hence, a spectrometer was required to investigate the stability differences of all samples. Figure 9 plots the absorbance RAbs (at a wavelength of 600 nm) of the CBNFs synthesized using the V2–V4 configurations with various concentrations of EP dispersant. The samples were statically positioned for 48 h to calculate their stability using (1). A high RAbs value represents more severe sedimentation. The samples with the highest stability for the V2, V3, and V4 configurations were V2-5, V3-5, and V4-0, respectively; however, the stability enhancement had to be investigated further. Further research on the addition of different types and concentrations of dispersants should be considered. The results of XRD and Raman spectroscopy confirmed that the CBNMs prepared using V2–V4 were very similar but that EP dispersant addition had different effects on the materials’ stability. This was primarily due to the particle size in the CBNMs, the pH of the CBNFs, and the interfacial effect between a CBNM and its base fluid. The estimation of suspended particle size distribution, zeta potential, and basic physicochemical characteristics requires a long time; thus, the poor stability of the samples that was observed during the measurements caused a large measurement deviation. Therefore, follow-up experiments were only performed on the samples with the highest stability for each of the V2–V4 configurations (V2-5, V3-5, and V4-0).Figure 8
Photographs of the experimental results obtained using the static positioning method.
(a)
Initial state (b)
After 120 hoursFigure 9
Absorbance ratios obtained using the static positioning method applied to the CBNFs obtained using various process parameter configurations.Figure10 depicts the dp distribution of V2-5, V3-5, and V4-0 and reveals that their average dp was 771.1 (274.4 and 1278.1 nm), 680.2, and 293.9 nm, respectively. The results are consistent with those of the stability experiment. The minimum dp was obtained for a V4 sample, and this sample was highly stable even when no dispersant was added. The dp distribution for the V2 sample was a bimodal distribution, which is associated with the existence of a flaky material and causes a wide dp distribution. Figure 10 displays only one of five test results that were obtained for the dp distribution; the average dp of the five test results for each sample is listed in Table 2.Table 2
Basic physicochemical characteristics of the CBNFs.
Item Experimental data CR (%) T (°C) Water V2-5 V3-5 V4-0 V2-5 V3-5 V4-0 Mean particle size (dp, nm) 25 — 749.56 692.05 269.90 — Zeta potential (ζ, mV) 25 −12.86 −13.98 −29.80  Density(ρ, kg/m3) 30 996.27 996.07 996.43 996.17 −0.02 0.02 −0.01 40 991.87 992.97 993.00 992.70 0.11 0.11 0.08 50 987.33 987.70 988.70 987.60 0.04 0.14 0.03  pH 30 8.00 7.29 7.06 7.17 −8.83 −11.75 −10.42 40 7.62 7.37 7.01 7.25 −3.32 −8.05 −4.90 50 7.56 7.38 7.26 7.33 −2.38 −3.97 −3.04  Electrical conductivity(E, μS/cm) 30 110.70 257.00 280.50 190.50 132.16 153.39 72.09 40 113.70 261.67 285.17 193.32 130.14 150.81 70.02 50 120.80 266.50 286.67 193.92 120.61 137.31 60.53  Viscosity(μ, mPa s) 30 0.80 0.83 0.82 0.80 4.17 2.50 0.00 40 0.72 0.78 0.75 0.75 9.30 4.65 4.65 50 0.65 0.70 0.73 0.65 7.69 12.82 0.70  Specific heat(cp, kJ/kg °C) 30 4.183 4.082 4.165 4.197 −2.40 −0.42 0.34 40 4.182 4.083 4.172 4.196 −2.36 −0.24 0.33 50 4.182 4.091 4.175 4.191 −2.17 −0.17 0.22  Thermal conductivity(k, W/m K) 30 0.618 0.615 0.623 0.622 −0.44 0.87 0.73 40 0.629 0.643 0.633 0.638 2.21 0.56 1.29 50 0.644 0.658 0.654 0.652 2.26 1.63 1.29Figure 10
Particle size distributions of the CBNFs obtained using various process parameter configurations.Table2 lists the average dp, ζ, ρ, pH, E, μ, cp, and k of the CBNFs synthesized using the various processing parameters and optimal EP dispersant concentration configurations. The values of dp and ζ were individually measured five times, and then the average was calculated. The lowest dp was that of V4-0, followed by V3-5 and V2-5. Although the differences in the samples with the same configuration parameter existed, the types of dp distribution were similar. The higher the absolute value of ζ, the better the stability of a CBNF. The highest ζ was that for V4-0, followed by V3-5 and V2-5. In general, the ζ of an NF is within the range of ±10 to ±30 mV, which indicates that the NF has incipient instability [35, 36]. In this experiment, CBNFs were obtained by using various process parameters. The ζ of the CBNFs and the optimal EP dispersant concentrations of the MSVTM were within the range −12.86 to −29.80 mV. The stability results indicated that the stability of these materials should be further improved. Further research will provide more details on what types and concentrations of dispersants can be added. Such addition can improve the stability when CBNFs are used in heat exchange systems, which require long-term stability.The density test results for the CBNFs revealed thatρ and temperature were inversely proportional. Hence, there was no significant difference between the ρ of a CBNF and that of water (within the instrumental error) due to the low concentration of CBNM in a CBNF. The highest CRs ofρ for V2-5, V3-5, and V4-0 were, respectively, 0.11%, 0.14%, and 0.08% compared with water for the entire range of sample temperature.The pH test results indicated that the pH of the CBNFs was lower than that of water because CO2 dissolved in the water to form carbonic acid during the combustion process, which slightly lowered the pH of the CBNFs. The highest CRs of the pH for V2-5, V3-5, and V4-0 were −8.83%, −11.75%, and −10.42%, respectively, compared with water for the entire range of sample temperature.Increasing the concentration of solid particles in an NF generally increases theE of that NF. Moreover, the addition of ionic dispersants (e.g., SDBS or SDS) can cause E to increase several times. The rapid movement of ions and suspended particles in NFs also increases the E of NFs at a high temperature. In this study, the EP dispersant employed was a nonionic dispersant and thus minimally affected E. The EP dispersant was less effective than an ionic dispersant with regard to the effect of dispersant addition on E. The highest CRs of E for V2-5, V3-5, and V4-0 were 132.16%, 153.39%, and 72.09%, respectively, compared with water for the entire range of sample temperature. The experimental results revealed that the EP dispersant had a considerable effect on the E of the CBNFs. However, the effect was weaker than that of an ionic dispersant.CBNFs have a higherμ than their base fluids (single-phase fluid) because CBNFs are solid-liquid mixtures (two-phase fluids). In general, the pressure drop and transport energy consumption in the pipeline increase as theμ of the working fluid is increased. However, most NFs are non-Newtonian fluids with shear thinning behavior, which causesμ to decrease at high flow rates or limits its increase. Consequently, rheological experiments were required to understand the relationships betweenμ, pressure drop, and flow rate. The highest CRs of μ for V2-5, V3-5, and V4-0 were 9.30%, 12.82%, and 4.65%, respectively, compared with water for the entire range of sample temperature.On the basis of the concept of a solid-liquid mixture, adding a material with acp lower than that of water forms a suspension that has a cp lower than that of water. The experimental results revealed that the cp of V2-5 to V3-5 were lower than that of water; however, the cp of V4-0 was slightly higher than that of water. This may be attributed to the EP dispersant, the solid-liquid interface, and experimental deviation. The highest CRs of cp for V2-5, V3-5, and V4-0 were −2.40%, −0.42%, and 0.34%, respectively, compared with water for the entire range of sample temperature.Most studies indicate that thek of an NF is higher than that of the NF’s base fluid. The k of the CBNFs in this study was slightly higher than that of water under most sample temperatures and process parameters. Nonetheless, the difference between the k of the CBNFs was small. This was primarily due to the low concentration of CBNMs and the only weak effect that the CBNFs had on the enhancement of k under instrumental deviation. The highest CRs of k for V2-5, V3-5, and V4-0 were 2.26%, 1.63%, and 1.29%, respectively, compared with water for the entire range of the sample temperature.


## 5. Conclusions

In this study, an MSVTM was used to fabricate CBNFs by using a one-step synthesis process. The CBNFs were synthesized using O2–C2H2 combustion flames with different flow rate ratios of O2–C2H2 (V1–V4). The characteristics of the CBNFs and suspended CBNMs were examined using suitable instruments and test methods. The findings of this study are summarized as follows:(i)
The CBNMs in the CBNFs were mainly spherical. Flaky CBNMs were also observed. Thedp of the spherical CBNMs was approximately 20–50 nm. For V1–V4, the CBNMs consisted of GO, RGO, and AC.(ii)
The CBNM production rate was affected by the processing time. Moreover, the processing time did not influence the morphology and material of CBNM. For a processing time of 12 min, the V2, V3, and V4 configurations resulted in CBNM concentrations of 0.0414, 0.0553, and 0.0239 wt.%, respectively.(iii)
The CBNFs prepared using the V4 configuration had optimal stability without the requirement of adding an EP dispersant. Theζ of the CBNFs indicated that the materials had incipient instability (ζ<30 mV) even with the addition of the EP dispersant. Hence, further research is required on the addition of different types and concentrations of dispersants to enhance the feasibility of practical application of CBNFs.(iv)
The highest enhancement ratios ofμ for V2-5, V3-5, and V4-0 were 9.30%, 12.82%, and 4.65%, respectively, higher than that of water for the entire range of sample temperatures. In addition, addition of EP dispersant considerably increased the μ of the CBNFs.(v)
The highest enhancement ratios ofk for V2-5, V3-5, and V4-0 were 2.26%, 1.63%, and 1.29%, respectively, higher than that of water for the entire range of sample temperatures.



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*Source: 3264621-2018-05-15.xml*