Hyoung-Ju Yoon,
Jae Young Lee,
Jae-Suk Lee and
Tae-Ho Yoon*
School of Materials Science and Engineering, Gwangju Institute of Science and Technology (GIST), 123 Cheomdan-gwagiro (Oryong-dong), Buk-gu, Gwangju 61005, Republic of Korea. E-mail: thyoon@gist.ac.kr
First published on 26th March 2019
Monolithic carbon xerogel (MCX) with co-continuous hierarchical porosity was prepared via a one-step, template- and catalyst-free hydrothermal polycondensation reaction with resorcinol (R), formaldehyde (F) and distilled water (W), followed by pyrolysis and CO2 activation. The reaction was carried out in a pressurized Teflon mold at 100 °C for 6 h, while F/R (2.2, 2.4, 2.6, and 2.8) and R/W ratios (40 and 45) were varied to obtain a co-continuous pore structure with interconnected particles. Next, the gels were dried at 60 °C for 36 h and then at 100 °C for 12 h to produce xerogels, which were then subjected to pyrolysis at 900 °C for 2 h and CO2 activation at 1000 °C for 2, 4 or 6 h. A co-continuous pore structure with interconnected particles was observed in gels with F/R = 2.4 and 2.6 at R/W = 40 and with F/R = 2.2 at R/W = 45, but the gel with F/R = 2.4 at R/W = 40 was the only one that showed no crack generation upon 6 h CO2 activation. Thus, this gel was subjected to a N2 sorption study, which resulted in a specific surface area (SSA) of 1418, 2489 and 3418 m2 g−1 at 2, 4 and 6 h activation, respectively. This was attributed to the introduction of micro-pores via activation, which also generated meso- and macro-pores to form hierarchical porosity.
Unfortunately, the monolithic PCM was not available until Pekala introduced the base-catalyzed polycondensation reaction of resorcinol (R) and formaldehyde (F).16 It was one-step, template-free reaction in a glass ampule at 85 °C for 7 days. But solvent exchange and supercritical drying were employed to retain the pore structure after drying, and the monolithic carbon aerogel (MCA) was produced instead of monolithic carbon xerogel (MCX). Furthermore, the pores were formed by aggregated carbon particles, instead of interconnected particles, which is related to the rate of gelation and phase separation for spinodal decomposition.17 Pekala's study also showed low specific surface area (SSA) (500–700 m2 g−1) despite carrying out supercritical drying.
In 2008, however, Baumann and co-workers18 prepared MCAs with a high SSA of 3125 m2 g−1 by using a similar approach to Pekala's, but CO2 activation was employed, which is known to introduce micro-pores that lead to high SSA. In fact, there are a number of other studies reporting monolithic MCAs with high SSA values via CO2 activation.19–22 In Baumann's study, the obtained pore structure with aggregated carbon particles was converted to a co-continuous pore structure with interconnected particles via CO2 activation. Additionally, the CO2 activation also introduced meso- and macro-pores, leading to the formation of hierarchical porosity that is highly desirable for high performance. However, one critical drawback of this study is the aforementioned supercritical drying.
The MCX was prepared without supercritical drying by Tsuchiya19 through a similar approach used by Baumann18 but it required a multi-step process. As expected from 6 h of CO2 activation, a high SSA of 2965 m2 g−1 was reported, but the pore structure was formed by aggregated carbon particles and was similar to the one observed by Baumann.18 On the other hand, the MCX having a co-continuous pore structure with interconnected carbon particles was reported by Huang and co-workers.23 As noted, such unique pore structure can be attributed to (1) hydrothermal reaction at 100 °C, which is higher than 85 °C used by Pekala,16 or 80 °C used by Baumann,18 thus, leading to a higher degree of condensation reaction, and (2) phenol resin, which is much less soluble in water than in formaldehyde, thus, changing the degree of spinodal decomposition. In addition, the phenol resin may form much more rigid chemical bonds with formaldehyde than with resorcinol, producing a tenacious pore structure to afford xerogels without employing supercritical drying. Unfortunately, a low SSA of ∼620 m2 g−1 was reported despite the use of soft templates in the absence of CO2 activation. Similar pore structures were also reported by Liang and Dai,24 and Werner,25 but they also have some drawbacks to be resolved.
Among the aforementioned studies, the one by Bauman18 appears to be the most attractive since it involves a simple one-step, template-free reaction. Also, the resorcinol used has a much better solubility in water than in phenol, making an aqueous solution process possible, and is much less expensive than phloroglucinol, making it a very attractive resin for MCAs.26 Moreover, CO2 activation was successfully employed, which introduced not only micro-pores for a greatly increased SSA, but also meso- and macro-pores for hierarchical porosity. However, there are two major drawbacks to be resolved: aggregated carbon particles obtained rather than interconnected ones, and the aerogel produced rather than the xerogel.
Thus, in our previous study,27 Baumann's method was modified by employing a hydrothermal reaction at 100 °C, and by varying the ratios of resorcinol to water (R/W) and resorcinol to catalyst (R/C). As expected, this approach resulted in MCXs with a co-continuous pore structure via interconnected carbon particles, and with high enough rigidity to make supercritical drying unnecessary. In addition, subsequent CO2 activation provided a SSA of 1418, 2489 and 3311 m2 g−1 with 2, 4 and 6 h, respectively, along with hierarchical porosity.27 Nevertheless, there remained one critical concern; poor reproducibility due to the strong dependence of the pore structure on the catalyst concentration, which was also reported by others.28–32 This led to studies on a catalyst-free reaction,33,34 but a co-continuous pore structure has yet to be obtained.
In this study, therefore, a catalyst-free reaction was attempted with resorcinol and formaldehyde, which were combined in one-step, template-free hydrothermal reaction at 100 °C. The ratios of F/R (2.2, 2.4, 2.6 and 2.8) and R/W (40 and 45) were varied to obtain a co-continuous pore structure having interconnected carbon particles without employing supercritical drying. The xerogels were then subjected to pyrolysis and CO2 activation to provide high SSA with hierarchical porosity, and the gels were characterized by FE-SEM and N2 adsorption–desorption measurements before and after activation.
A tube furnace (MSTF-1100, Myungsung Eng., Korea) was used for the pyrolysis of RF xerogels (diameter of ∼34 mm and thickness of ∼15 mm). It was heated from room temperature (RT) to 900 °C at 5 °C min−1 under a N2 flow of 200 sccm, and then held for 2 h at 900 °C, followed by natural cooling to RT under N2 flow. The carbon gels were cut in half and subjected to activation in the tube furnace at 1000 °C under a CO2 flow of 200 sccm for 2, 4 or 6 h. First, dimensional changes in the gels were estimated by size measurements, while crack generation was monitored by visual inspection since it is an important factor for the monolithic PCM. Next, the burn off ratio (BOR) was calculated based on the weight before and after activation.19 The MCXs were then analyzed by Field-Emission Scanning Electron Microscopy (FE-SEM, Jeol, JSM-7500F) at 10 keV with carbon coating, and their pore characteristics were studied with an adsorption instrument (ASAP-2010, Micromeritics, USA) using N2 at 77 K. The specific surface area (SSA) and pore size distribution were calculated by Brunauer–Emmett–Teller (BET) and Barrett–Joyner–Halenda (BJH) methods, respectively. The total pore volume was calculated from the total single point adsorption of pores with a radius less than 300 nm at P/Po = 0.99, and the micro-pore volume was obtained by the t-plot theory.
In the N2 sorption analysis, the MCX from R/W = 40 exhibited a Type I isotherm (F/R = 2.2, 2.4, and 2.6), with the exception of F/R = 2.8 which showed a mixed isotherm of Type II and Type IV (Fig. 2a). The latter can be explained by the existence of micro-, meso- and macro-pores, which formed hierarchical porosity.9 This was also supported by the pore size distribution, as shown in Fig. 2b. The micro-pores are believed to be formed by pyrolysis, while the meso- and macro-pores are created by the aggregation of particles (Fig. 1d). The MCXs from F/R = 2.4 and 2.6 showed a Type I isotherm and the presence of only micro-pores from pyrolysis, since there was no aggregation of particles to form meso- and macro-pores (Fig. 1b and c). However, the MCX from F/R = 2.2 at R/W = 40 showed a Type I isotherm despite the presence of aggregated carbon particles (Fig. 1a). This is contrary to what was expected, since aggregated particles would show meso and macro-pores between the particles, as observed from the gel with F/R = 2.8. The discrepancy can be explained by the large particles which form only large pores upon aggregation, which are too large to be detected by the adsorption instrument (ASAP-2010, Micromeritics) that has a detection limit of 300 nm.
Fig. 2 N2 isotherms of carbon xerogels from R/W = 45 (a) and R/W = 40 (c) and activated carbon xerogels from R/W = 40 (e) along with their pore size distribution (b, d and f). |
The MCXs from R/W = 45 also exhibited a similar trend, with one showing a Type I isotherm (F/R = 2.2) and three showing a mixed isotherm of Type II and Type IV (F/R = 2.4, 2.6 and 2.8) (Fig. 2c), as expected from the FE-SEM analysis. In addition, the N2 adsorption in the meso- and macro-pore range increased gradually with higher F/R ratios (2.4, 2.6 and 2.8). This is because the number of meso- and macro-pores increased with higher F/R ratios, which can be attributed to the increased number of small particles as the F/R ratio increased. This was supported by the pore size distribution (Fig. 2d), while the smaller size of particles with higher F/R ratios, which leads to higher aggregation, is evidenced by FE-SEM micrographs (Fig. 1).
It is interesting to note that the SSA decreased slightly with higher F/R ratios; 645, 641, 623 and 618 m2 g−1 with F/R = 2.2, 2.4, 2.6 and 2.8 at R/W = 40, respectively (Table 1). A similar trend was also observed with R/W = 45, as shown in Table S1.† This decrease may be related to the smaller particle size and higher degree of aggregation with the higher F/R ratio (FE-SEM in Fig. 1). As noted, these SSAs are similar to those reported earlier20,24,35 and appear to be the maximum values when activation or template is not utilized. On the other hand, the peak observed at 3–4 nm in all MCXs was attributed to the tensile strength effect caused by the ink-bottle or cylinder-type pores.36
Sa (m2 g−1) | Vtotalb (cm3 g−1) | Vmicroc (cm3 g−1) | dBOR (%) | |
---|---|---|---|---|
a Specific surface area.b Total pore volume.c Micro pore volume.d Burn off ratio from weight loss. | ||||
40-2.2 | 645 ± 12 | 0.252 | 0.242 (96.0%) | |
40-2.4 | 641 ± 14 | 0.254 | 0.243 (95.7%) | |
40-2.6 | 623 ± 12 | 0.271 | 0.232 (85.6%) | |
40-2.8 | 618 ± 11 | 0.401 | 0.206 (51.4%) | |
40-2.4-2 h | 1481 ± 22 | 0.58 | 0.564 (97.2%) | 35 |
40-2.4-4 h | 2489 ± 25 | 1.067 | 1.025 (96.1%) | 60 |
40-2.4-6 h | 3418 ± 48 | 1.774 | 1.554 (87.6%) | 79 |
As for crack generation, different behaviors were observed in the MCXs, as mentioned previously.27 The MCX from R/W = 45 showed crack generation with 6 h activation, regardless of the F/R ratio (Table S3†). However, some MCXs from R/W = 40 exhibited no crack generation (F/R = 2.2 and 2.4) while others showed crack generation (F/R = 2.6 and 2.8) with 6 h activation (Table S2†). It is interesting to note that the MCX with interconnected particles showed no cracks, while those with highly aggregated particles exhibited cracks. Since those showing cracks are samples with high R/W and F/R ratios, it is believed that aggregated particles generate large residual stress upon weight loss or shrinkage, leading to the formation of cracks upon activation, in contrast to the small stress generated by interconnected particles.
When the MCXs showing crack generation after 6 h activation are excluded, only the two MCXs from F/R = 2.2 and 2.4 at R/W = 40 remain. Of these, only the latter MCX showed co-continuous pore structure with interconnected particles. Thus, this sample was selected for the N2 sorption study, which resulted in a Type I isotherm after activation. This is similar to the result obtained before activation, but the adsorbed volume of N2 increased dramatically with activation time (Fig. 2e). This is due to the increased micro- and meso-pores upon activation, which was confirmed by pore size distribution (Fig. 2f), as well as micro-pore volume measurements (Table 1). As expected,18,22,37 the activation resulted in high SSA values of 1481, 2489 and 3418 m2 g−1 for 2, 4 and 6 h, respectively, which are much higher than 641 m2 g−1 obtained from the MCX before activation.
According to the FE-SEM analysis, the pore structure of MCXs after activation is similar to each other, irrespective of the activation time (Fig. 3), and also similar to the structure before activation, as reported previously.27,37 This indicates that there was no shrinkage upon activation, which appears to be inconsistent with the results of large BOR and size reduction upon activation. It is believed that the size reduction arises from the removal of the outer layer of MCX by CO2 oxidation, which is also partially responsible for the large BOR.27 Of course, the large BOR is also believed to be caused by micro- and meso-pore formation in the skeleton upon activation, which in turn increases the SSA dramatically, but this cannot be demonstrated by FE-SEM.
Fig. 3 FE-SEM micrographs of RF xerogels after activation for F/R = 2.4 at R/W = 40 for 0 h (a), 2 h (b), 4 h (c), and 6 h (d). |
Footnote |
† Electronic supplementary information (ESI) available: Photo of monolithic RF (left) and carbon (right) xerogel. Characteristics of monolithic carbon xerogels at R/W = 45. Burn off ratio (%) of monolithic carbon xerogels from F/R of 2.2, 2.4, 2.6 and 2.8 at R/W = 40 upon activation. Burn off ratio (%) of monolithic carbon xerogels from F/R of 2.2, 2.4, 2.6 and 2.8 at R/W = 45 upon activation. See DOI: 10.1039/c9ra00904c |
This journal is © The Royal Society of Chemistry 2019 |