Nghiên cứu khoa học công nghệ<br />
<br />
SYNTHESIS OF CARBON AEROGEL MATERIAL<br />
IN ATMOSPHERE CONDITION<br />
Le Anh Kien1*, Le Khac Duyen1,2, Pham Quoc Nghiep1, Le Thi Kim Phung2<br />
Abstract: Porous carbon aerogels were prepared from resorcinol–formaldehyde<br />
monomers using sodium carbonate catalyst by ambient pressure drying technique.<br />
Aerogels were characterized by using SEM, XRD, TGA and nitrogen adsorption<br />
methods. The experimental results indicated that carbon aerogels obtained by using<br />
ambient pressure drying showed BET surface area, density, average pore size, total<br />
pore volumes in the range of 459.7–522.1 m2/g, 0.167–0.629 g/cm3, 19.45 Å, and<br />
0.259 cm3/g, respectively. The activation process with CO2 was influence to<br />
properties of carbon aerogels and it can improve the surface area reach about 779<br />
m2/g. Thus, depending on the applications, carbon aerogels can be synthesized at<br />
different conditions.<br />
Keywords: Aerogel; Carbon aerogel; Ambient pressure drying; Resorcinol–formaldehyde; Microstructure.<br />
<br />
1. INTRODUCTION<br />
Aerogels are highly porous materials with low density and large specific surface area,<br />
derived via sol–gel technique. The first aerogels were made from waterglass–derived silica<br />
gels, employing solvent exchange and using supercritical conditions to remove the pore<br />
liquid [1]. The aerogels can be obtained as monoliths, granulates, films, or powders. Most<br />
notably aerogels are known for their extreme low densities (0.0011–0.8 g/cm3), high<br />
porosity (80–99%), and large surface area (400–1000 m2/g) [2–4]. Due to these special<br />
properties, aerogels have attracted much attention for they have large potential to be<br />
applied in many fields.<br />
First carbon aerogel was obtained by resorcinol–formaldehyde organic aerogel<br />
synthesis, and pyrolysis in the inert atmosphere by Pekala [2] at the end of 1980s. The<br />
properties of carbon aerogels were depended on the amount of reactant, catalyst, and water<br />
used in the sol–gel polycondensation [5–7] and drying methods [8–10]. Because of their<br />
chemical and textural characteristics, they were expected to be materials for thermal and<br />
sonic insulation, chromatography packing in the research of Wu et al. [8], or the electrodes<br />
for electrochemical double layer capacitors by Pekala et al. and Kim et al. [11, 12],<br />
adsorbents in study of Meena et al. [13] and catalyst supports by research of Moreno–<br />
Castilla et al.[14]. In the research of Shariff et al., the effect of different catalysts, such as<br />
acetic acid, sodium carbonate and sodium hydroxide on the sol–gel process were tested.<br />
The results showed that the carbon aerogel that synthesized with acetic acid catalyst gave a<br />
very high surface area (619.2 m2/g), high pore–volume and microporous area comparing to<br />
the other samples in the same conditions [5]. All the different catalysts resulted in different<br />
surface morphology of the aerogels. The study of Liviu Cosmin et al. [15] with varieties<br />
of synthesis parameters such as R/C ratio and RF content indicated that when using ratio<br />
of R/C ≤ 100, mesoporous carbon aerogels with high BET surface area from 800 to 1100<br />
m2/g were obtained, whereas for ratio of R/C > 100, the carbon aerogels were mostly<br />
macroporous. Drying methods were also affected on properties of carbon aerogels. The<br />
researches of Wu et al. carried out the drying techniques to convert the liquid gel to a solid<br />
gel, in the atmosphere condition drying [8], whilst the freeze drying [9] were chosen in the<br />
study of Yamamoto et al., supercritical drying were performed by Liu et al. and Tamon et<br />
al. [10, 16]. The results of these researches gave that the porous structure and surface area<br />
of the carbon aerogel depended on the initial conditions of synthesis, drying, and<br />
<br />
<br />
<br />
Tạp chí Nghiên cứu KH&CN quân sự, Số 42, 04 - 2016 155<br />
Hóa học & Kỹ thuật môi trường<br />
<br />
carbonizing techniques. This also mentioned in the researches of Pekala et al., Czakkel et<br />
al., and Gallegos–Suarez et al. [2, 17, 18].<br />
In this paper, carbon aerogels were synthesized via a sol–gel process by the aqueous<br />
polycondensation of resorcinol with formaldehyde, using sodium carbonate as a base<br />
catalyst under ambient drying technique. The preparing conditions such as the catalyst<br />
concentration, the ratio of reactant to solvents were investigated in this study, the structure<br />
and properties of the obtained products were characterized by scanning electron<br />
microscope (SEM), X–Ray diffraction (XRD), thermo gravimetric analysis (TGA) and<br />
nitrogen absorption measurements. The effects of activation process with CO2 was also<br />
tested on the product carbon aerogels.<br />
2. EXPERIMENTAL<br />
2.1. Preparation of carbon aerogel<br />
The resorcinol–formaldehyde wet gels were prepared using resorcinol (99.5% purity),<br />
formaldehyde (37% solution), Na2CO3 (99.8% purity), and deionized water. Appropriate<br />
amounts of resorcinol (R), formaldehyde (F), Na2CO3 (C) and water were mixed at room<br />
temperature with magnetic stirrer for in an hour. The mixture was transferred into plastic<br />
moulds (8 cm–length x 2 cm internal diameter) and cured: 1 day at room temperature, 1<br />
day at 50oC, and 3 days at 80oC for gelation. The resorcinol–formaldehyde gels were then<br />
immersed in acetone for three days in order to completely exchange the water in the sol–<br />
gel structure. Subsequently, the samples were directly dried in air at room temperature for<br />
2 days at first, and then further dried in an oven at 50oC for 2 days and 80oC for 1 day in<br />
ambient pressure. Finally, pyrolysis of the RF aerogel was performed at 800oC for 3 hours<br />
under N2 atmosphere (400 cm3min–1), resulting in carbon aerogels (CA). The pyrolysis<br />
product yield was calculated by dividing the weight of the carbon aerogels to the weight of<br />
as–prepared aerogel. Carbon aerogels was further activated at 800oC for 2 hours under a<br />
flow of CO2 to increase its properties. In this study, the ratio of R and F was kept at 1/2,<br />
the RF content was changed from 10% to 40%, the ratio of resorcinol and catalyst (R/C<br />
ratio) was changed from 500 to 3000.<br />
2.2. Characterization methods<br />
Surface area and pore-size distribution of carbon aerogels samples were characterized<br />
by analysis of nitrogen absorption–desorption isotherms measured by ASAP 2020<br />
analyzer (Micrometrics Instruments Corp.). The samples were degassed under vacuum<br />
(10–5 torr) to 110oC (for organic aerogels) and 200oC (for carbon aerogels) for at least 10<br />
hours to remove all adsorbed species. Brunauer–Emmett–Teller (BET) method was used<br />
for total surface area measurements, and t–plot method was used for estimating mesopore<br />
surface area. Pore–size distribution was obtained by the Barret–Joyner–Halenda (BJH)<br />
method from desorption branch of the isotherms. Total pore–volume was calculated from<br />
the adsorbed volume of nitrogen at P/P0=0.99 (saturation pressure).<br />
The bulk densities of the samples were estimated by measuring the dimensions and the<br />
mass of each monolithic sample.<br />
Thermo gravimetric analysis was carried out to determine the weight loss in relation to<br />
temperature with a TA Instruments TGA Q500 V20.10 Build 36 thermal analyzer. The<br />
specimen was heated up to 150◦C for 1 h to ensure that the adsorbed water in the specimen<br />
to be removed. Then, the specimen was heated to 900◦C at a rate of 10◦C min−1 in air.<br />
Scanning electron microscopy was performed with a HITACHI S–4800 microscope.<br />
<br />
<br />
<br />
<br />
156 Le Anh Kien,…, “Synthesis of carbon aerogel material in atmosphere condition.”<br />
Nghiên cứu khoa học công nghệ<br />
<br />
X–ray diffractogram was recorded on Bruker D8 Advance diffractometer with Cu–Kα<br />
radiation (λ=1.54060 Å) operated at the voltage and current values of 40 kV and 40 mA<br />
respectively for the 2θ values in the range 5–70° at a scan speed of 1.2°/min.<br />
3. RESULTS AND DISCUSSION<br />
3.1. Evaluation of the synthesis process<br />
In this study, the RF aerogels were synthesized via a sol–gel process by the aqueous<br />
polycondensation of resorcinol with formaldehyde, using sodium carbonate as a base<br />
catalyst [2]. The R and F monomers were polymerized in a plastic container and a<br />
monolithic product was obtained by ambient pressure drying. The RF aerogel samples<br />
with dimension of 140x120x5 of length x width x thickness were prepared as in Figure 1.<br />
<br />
<br />
<br />
<br />
Figure 1. RF aerogel and carbon aerogel samples with R/C = 1000, RF content = 40%.<br />
The varieties of catalyst concentration (R/C ratio) and RF content (RF%) were<br />
investigated to determine the optimal condition for synthesis RF aerogel by ambient<br />
pressure drying. The results showed that, all RF samples with R/C ratio from 1500 to 3000<br />
were not completely gelation, they all were coagulated in the solution and precipitated at<br />
the bottom of container. This might be because of the concentration of catalyst was not<br />
enough to form a cross–linked network. When the R/C ratio was decreased, the sol–gel<br />
process was improved. RF samples with R/C ratio less than 1000 were easily gelation. In<br />
the gelation process, catalyst concentration was much affected. This was because of that:<br />
(1) the formation of monomer from resorcinol and formaldehyde, (2) the condensation of<br />
monomer with each other to form nanometer–sized clusters; and (3) crosslinking of<br />
clusters through their surface groups to form a gel [1]. The size of clusters was regulated<br />
by the catalyst concentration in RF mixture. Figure 2 showed a schematic diagram of the<br />
reaction of resorcinol with formaldehyde under used conditions in this study.<br />
<br />
<br />
<br />
<br />
Figure 2. A schematic diagram of the reaction of resorcinol with formaldehyde.<br />
<br />
<br />
<br />
Tạp chí Nghiên cứu KH&CN quân sự, Số 42, 04 - 2016 157<br />
Hóa học & Kỹ thuật môi trường<br />
<br />
In this results, densities of RF samples ranged of 0.254–0.853 g/cm3, and surface area<br />
were in the range of 176.08–204.08 m2/g. The RF samples with R/C = 1000 and RF<br />
content = 40% show the best properties. The density of those samples were minimum<br />
value of all types because of lowest volume shrinkage taken place (Table 1).<br />
Table 1. Physical properties of RF aerogel at different conditions.<br />
Samples Mass shrinkage (%) Volume shrinkage (%) Density (g/cm3)<br />
RF–40–1000 79.47 18.34 0.254<br />
RF–40–500 79.40 52.25 0.436<br />
RF–30–500 84.65 67.33 0.475<br />
RF–20–500 95.21 90.04 0.485<br />
RF–10–500 94.73 90.36 0.552<br />
RF aerogels were then pyrolysized to form CA samples. The pyrolysis yields of<br />
aerogels under different conditions were all the same, ranged from 41% to 50%. The<br />
densities of the CA samples were in the range of 0.167 – 0.629 g/cm3, and the surface area<br />
of CA were of 459.76 – 522.13 m2/g. They all were close to the values of monolithic CAs<br />
in the literature [8]. During the pyrolysis process, the organic groups in the structure of RF<br />
aerogel were volatile to form carbon network. The mass loss of the samples due to<br />
pyrolysis was in range of 51–56%, similar to the study of Yamashita et al. [19].<br />
3.2. Morphology and nanostructure of the carbon aerogel<br />
(a)-CA500<br />
<br />
<br />
<br />
<br />
(b)-CA1000 (c)-ACA1000<br />
<br />
<br />
<br />
<br />
Figure 3. SEM photographs of aerogel samples. (a) carbon aerogel R/C=500 (CA500);<br />
(b) carbon aerogel R/C=1000 (CA1000) và (c) activated carbon aerogel R/C=1000<br />
(ACA1000).<br />
Figure 3 showed the morphology of CA samples with different R/C ratio. The<br />
morphologies of CA particles were found to be nearly spherical in shape. All types of<br />
structures were formed by a three–dimensional network of interconnected nano–sized<br />
primary particles more or less fused. It can be seen that the product CA particles at<br />
<br />
<br />
158 Le Anh Kien,…, “Synthesis of carbon aerogel material in atmosphere condition.”<br />
Nghiên ccứu<br />
ứu khoa học công nghệ<br />
<br />
CA1000 were larger than those at CA500. These particles were very difficult to<br />
distinguish in CA500 sample, where a continuous and hhighly<br />
ighly cross–linked<br />
cross linked porous structure<br />
has been formed. The carbon nano–particles<br />
nano particles in obtained aerogels stacked into grape–like<br />
grape like<br />
aggregates and then these aggregates interconnect in different directions into a network.<br />
When the R/C ratio was controlled at 1000 (see Figure 3a), the size of the carbon particles<br />
of the CA1000 sample was in the range of about 40 40–50<br />
50 nm, similar to the nano–structures<br />
nano structures<br />
of monolithic CA reported by Wu et al. [88].. The CA prepared in this work have the nano–nano–<br />
particle structures typical of the samples prepared with the CO2 supercritical drying<br />
technique in the studies of Al–Muhtaseb<br />
Al et al. and Qin et al. [6, 20].<br />
20 . Additionally, the size<br />
of the carbon particles was hardly affected by activation with CO2; Figure 3c indicated that<br />
the particles size was decreased into 20–<br />
20–30<br />
30 nm due to the reaction of CO2 with carbon<br />
network and the abrasion of carbon structure during activation.<br />
The XRD diagram of the synthesized CA samples were shown in Figure 4. It presented<br />
two large peaks at about 2θ = 24ο and 44o, similar to the diffraction peaks of C(002) and<br />
C(101) and it was in agreement with the literature data [7].. The first peak indicated that<br />
CA samples contained a proportion of highly disordered materials in the form of<br />
amorphous carbon. In addition, the samples also con contained<br />
tained some graphite–like<br />
graphite like structures<br />
(crystalline carbon) indicated by the presence of a clear (002) band at ~ 24o and (101)<br />
weak band at ~ 44o. Moreover, the presence of a peak at ~10o showed that there was<br />
impurity in the CA samples after pyrolysis becau because<br />
se its intensity was decreased after<br />
activation with CO2. The activation process removed the impurities; surface functional<br />
groups and carbon in the structure of CA by abrasion and reaction of CO2. These<br />
observations suggested that the crystallites in all the CA samples have intermediate<br />
structures between graphite and amorphous state called turbostratic structure or random<br />
layer lattice structure.<br />
<br />
<br />
<br />
<br />
Figure 4. X–Ray<br />
Ray diffraction pattern of carbon aerogel (AC1000) and activated carbon<br />
aerogel (ACA1000).<br />
TGA experiments showed that a first slight weight loss from 50 50–90oC was due to the<br />
desorption of physical moisture from the aerogel structure. Further heating in the<br />
temperature range of 550o–650650oC resulted in about 81% weight lo<br />
loss.<br />
ss. This weight loss can<br />
be attributed to the destruction of CA structure and the combustion in air. This results<br />
showed that CA samples easily absorbed moisture during storage and were destroyed in<br />
the air at the temperature of higher 550oC.<br />
<br />
<br />
Tạp<br />
ạp chí Nghi<br />
Nghiên cứu<br />
ứu KH&CN quân<br />
uân sự,<br />
s Số 422, 04 - 2016 159<br />
Hóa học & Kỹ thuật môi trường<br />
<br />
<br />
<br />
<br />
Figure 5. Thermo gravimetric analysis data for activated carbon aerogel (ACA1000).<br />
3.3. Porous properties of the CA samples<br />
Physical properties, especially the surface characteristics of aerogels were evaluated by<br />
nitrogen gas sorption studies using BET analyzer at 77 K (Figure 6). Results of BET<br />
analysis were given in Table 2. The isotherms of the RF aerogels have been observed to be<br />
of Type IVa following the IUPAC classification, indicating multilayer absorption on the<br />
surface of the RF aerogels. This type of isotherm was characteristic of mesoporous<br />
adsorbents. Pore–diameter of RF aerogel was distributed from 10 to 150 Å (Figure 7), with<br />
mesopore–volume percentage was 42.5% of total pore–volume. BET surface area of RF<br />
aerogels was in range of 176–208 m2/g. The isotherms of carbon aerogel were type Ia,<br />
indicating the microporous adsorbents. Microporous volume was about 98 percent of total<br />
pore–volume of carbon aerogel, with the pore–size was in range of 5–11 Å. The surface<br />
area of carbon aerogels increased dramatically to 459–522 m2/g after pyrolysis, which was<br />
due to the creation of micropores as a result of evaporative loss of organic moieties.<br />
Table 2. Porous properties of RF aerogel, carbon aerogel and activated carbon aerogel.<br />
Activated carbon<br />
Properties RF aerogel Carbon aerogel<br />
aerogel<br />
Density (g/cm3) 0.254–0.853 0.167–0.629 0.150–0.510<br />
SBET (m2/g) 176.08–204.08 459.76–522.13 637.13–779.06<br />
Average pore size (Å) 31.77 19.45 22.24<br />
Median pore width (Å) 20.17 5.66 6.11<br />
Average particle size (Å) 294.00 114.91 77.02<br />
Vtotal (cm3/g) 0.1658 0.2591 0.4408<br />
Vmic(cm3/g) 0.0879 0.2540 0.3173<br />
Vmes(cm3/g) 0.0705 0.0033 0.0547<br />
Vmac(cm3/g) 0.0074 0.0051 0.0688<br />
Vmic (%) 53.01 98.04 71.98<br />
Vmes (%) 42.52 1.27 12.40<br />
Vmac (%) 4.47 1.96 15.62<br />
<br />
<br />
<br />
160 Le Anh Kien,…, “Synthesis of carbon aerogel material in atmosphere condition.”<br />
Nghiên ccứu<br />
ứu khoa học công nghệ<br />
<br />
<br />
<br />
<br />
Figure 6. Adsorption–desorption<br />
Adsorption desorption isotherms of RF aerogel (RF<br />
(RF1000<br />
1000);<br />
); Carbon aerogel<br />
(CA1000)) and Activated carbon aerogel (ACA<br />
(ACA1000<br />
1000).<br />
After activation with CO2, the characteristics of carbon aerogel were improved. The<br />
highest measured BET surface area of activated carbon aerogel reached 779 m2/g. The<br />
mesopore volumes and macropore volume of the samples were increased, indicated by the<br />
adsorption<br />
sorption isotherm type IIb. The pore–<br />
pore–sizes<br />
sizes were in the range from 8 to 200 Å, with<br />
average pore<br />
pore–diameter<br />
diameter was 22.2 Å, similar to the study of Gallegos<br />
Gallegos–Suárezet<br />
Suárezet et al. [18]..<br />
On the other hand, the size of aerogels particles was decreased by act activation<br />
ivation with CO2<br />
(Table 2); this suggested that the effect of activation on structure of carbon aerogel was<br />
creation more pore and surface area.<br />
<br />
<br />
<br />
<br />
Figure 7. Pore–size<br />
size distributions of RF aerogel (RF1000);<br />
(RF1000); carbon aerogel (CA1000) and<br />
nd<br />
activated carbon aerogel (ACA1000).<br />
(ACA1000)<br />
4. CONCLUSION<br />
The carbon aerogels were synthesized from resorcinol<br />
resorcinol–formaldehyde<br />
formaldehyde monomers using<br />
base catalyst via sol–gel<br />
sol gel process under ambient pressure drying technique. The R/C ratio<br />
and RF content of organic matrix were greatly influence to the shrinkage of gel–network<br />
gel network<br />
of the obtained materials. Characteristics of obtained aerogels were evaluated and<br />
compared with period studies. The results<br />
esults showed that carbon aerogels have intermediate<br />
structures between graphite and amorphous state and were destroyed in the air at the<br />
temperature of higher 550oC. C Surface area, density, average pore<br />
pore–size<br />
size and total pore–<br />
pore–<br />
volume of carbon aerogels 459.7 522.1 m2/g, 0.167–0.629<br />
aerogel were in the range of 459.7–522.1 0.629 g/cm3,<br />
<br />
<br />
Tạp<br />
ạp chí Nghi<br />
Nghiên cứu<br />
ứu KH&CN quân<br />
uân sự,<br />
s Số 422, 04 - 2016 161<br />
Hóa học & Kỹ thuật môi trường<br />
<br />
19.45Å, and 0.259 cm3/g, respectively. The activation process affected on the properties of<br />
carbon aerogels. The highest surface area of activated carbon aerogel reached 779 m2/g.<br />
REFERENCES<br />
[1]. M. A. Aegerter et al., “Aerogels handbook,” Springer Science & Business Media<br />
(2011).<br />
[2]. R. Pekala, "Organic aerogels from the polycondensation of resorcinol with<br />
formaldehyde," J. of Materials Science, Vol. 24 (1989), pp. 3221–3227.<br />
[3]. S. He et al., "Synthesis and characterization of silica aerogels dried under ambient<br />
pressure bed on water glass," J. of Non–Crystalline Solids, Vol. 410 (2015), pp. 58–<br />
64.<br />
[4]. P. Aravind et al, "Ambient pressure drying: a successful approach for the<br />
preparation of silica and silica based mixed oxide aerogels," J. of sol–gel science<br />
and technology, Vol. 54 (2010), pp. 105–117.<br />
[5]. A. M. Shariff et al., "Some studies on the synthesis and characterization of carbon<br />
aerogel," Transactions of the Indian Ceramic Society, Vol. 69 (2010), pp. 83–88.<br />
[6]. S. A. Al‐Muhtaseb and J. A. Ritter, "Preparation and properties of resorcinol–<br />
formaldehyde organic and carbon gels," Advanced Materials, Vol. 15 (2003), pp.<br />
101–114.<br />
[7]. K. S. Rejitha et al., "Role of catalyst on the formation of resorcinol–furfural based<br />
carbon aerogels and its physical properties," 2013.<br />
[8]. D. Wu et al., "Preparation of low–density carbon aerogels by ambient pressure<br />
drying," Carbon, Vol. 42 (2004), pp. 2033–2039.<br />
[9]. T. Yamamoto et al., "Control of mesoporosity of carbon gels prepared by sol–gel<br />
polycondensation and freeze drying," J. of non–crystalline solids, Vol. 288 (2001),<br />
pp. 46–55.<br />
[10]. N. Liu et al., "Carbon aerogel spheres prepared via alcohol supercritical drying,"<br />
Carbon, Vol. 44 (2006), pp. 2430–2436.<br />
[11]. R. Pekala et al., "Carbon aerogels for electrochemical applications," J. of non–<br />
crystalline solids, Vol. 225 (1998), pp. 74–80.<br />
[12]. S. Kim et al., "Preparation of carbon aerogel electrodes for supercapacitor and their<br />
electrochemical characteristics," J. of materials science, Vol. 40 (2005), pp. 725–<br />
731.<br />
[13]. A. K. Meena et al., "Removal of heavy metal ions from aqueous solutions using<br />
carbon aerogel as an adsorbent," J. of Hazardous Materials, Vol. 122 (2005), pp.<br />
161–170.<br />
[14]. C. Moreno–Castilla and F. Maldonado–Hódar, "Carbon aerogels for catalysis<br />
applications: An overview," Carbon, Vol. 43 (2005), pp. 455–465.<br />
[15]. L. C. Coteţ et al., "Synthesis of meso–and macroporous carbon aerogels," Revue<br />
Roumaine de Chimie, Vol. 52 (2007), pp. 1077–1081.<br />
[16]. H. Tamon et al., "Control of mesoporous structure of organic and carbon aerogels,"<br />
Carbon, Vol. 36 (1998), pp. 1257–1262.<br />
[17]. O. Czakkel et al., "Influence of drying on the morphology of resorcinol–<br />
formaldehyde–based carbon gels," Microporous and Mesoporous Materials, Vol. 86<br />
(2005), pp. 124–133.<br />
[18]. E. Gallegos–Suárez et al., "On the micro–and mesoporosity of carbon aerogels and<br />
xerogels. The role of the drying conditions during the synthesis processes," Chemical<br />
Engineering J., Vol. 181 (2012), pp. 851–855.<br />
<br />
<br />
<br />
<br />
162 Le Anh Kien,…, “Synthesis of carbon aerogel material in atmosphere condition.”<br />
Nghiên cứu khoa học công nghệ<br />
<br />
[19]. J. Yamashita et al., "Organic and carbon aerogels derived from poly (vinyl<br />
chloride)," Carbon, Vol. 41 (2003), pp. 285–294.<br />
[20]. G. Qin and S. Guo, "Preparation of RF organic aerogels and carbon aerogels by<br />
alcoholic sol–gel process," Carbon, Vol. 39 (2001), pp. 1935–1937.<br />
TÓM TẮT<br />
TỔNG HỢP VẬT LIỆU CARBON AEROGEL TRONG ĐIỀU KIỆN KHÍ QUYỂN<br />
Vật liệu xốp carbon aerogels được tổng hợp từ các monomer resorcinol-<br />
formaldehyde với xúc tác natri carbonate trong điều kiện sấy khí quyển. Các tính<br />
chất đặc trưng của aerogels được xác định bằng các phương pháp SEM, XRD, TGA<br />
và hấp phụ nitrogen. Kết quả nghiên cứu cho thấy carbon aerogel thu được có các<br />
tính chất diện tích bề mặt, khối lượng riêng, kích thước lỗ xốp trung bình, tổng thể<br />
tích lỗ xốp lần lượt là 459.7–522.1 m2/g, 0.167–0.629 g/cm3, 19.45 Å, and 0.259<br />
cm3/g. Hoạt hóa vật liệu carbon aerogel bằng khí CO2 sẽ ảnh hưởng đến các tính<br />
chất của vật liệu, sau quá trình hoạt hóa diện tích bề mặt riêng carbon aerogel tăng<br />
đến 779 m2/g. Vì thế, tùy thuộc vào các lĩnh vực ứng dụng, carbon aerogel có thể<br />
được tổng hợp trong các điều kiện khác nhau để đạt tính chất mong muốn.<br />
Từ khóa: Aerogel; Carbon aerogel; Sấy khí quyển; Resorcinol–formaldehyde; Cấu trúc micro.<br />
<br />
Nhận bài ngày 22 tháng 02 năm 2016<br />
Hoàn thiện ngày 08 tháng 4 năm 2016<br />
Chấp nhận đăng ngày 20 tháng 4 năm 2016<br />
1<br />
Địa chỉ: Viện Nhiệt đới môi trường, Viện KHCN quân sự;<br />
2<br />
Khoa Kỹ thuật Hóa học – Trường Đại học Bách Khoa TP.HCM;<br />
*<br />
Email: leanhkien@vnn.vn<br />
<br />
<br />
<br />
<br />
Tạp chí Nghiên cứu KH&CN quân sự, Số 42, 04 - 2016 163<br />