Next Article in Journal
Batch-Fabricated α-Si Assisted Nanogap Tunneling Junctions
Next Article in Special Issue
A Novel Polymeric Adsorbent Embedded with Phase Change Materials (PCMs) Microcapsules: Synthesis and Application
Previous Article in Journal
A Facile Approach to Solid-State White Emissive Carbon Dots and Their Application in UV-Excitable and Single-Component-Based White LEDs
Previous Article in Special Issue
The Preparation and Catalytic Properties of Nanoporous Pt/CeO2 Composites with Nanorod Framework Structures
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

A Porous Carbon with Excellent Gas Storage Properties from Waste Polystyrene

1
Dipartimento di Scienze e Innovazione Tecnologica (DISIT), Università del Piemonte Orientale, via T. Michel 11, I-15121 Alessandria, Italy
2
School of Engineering, Universtity of Edinburgh, Sanderson Building, R. Stevenson Road, Edinburgh EH11 3AZ, UK
*
Author to whom correspondence should be addressed.
Nanomaterials 2019, 9(5), 726; https://doi.org/10.3390/nano9050726
Submission received: 6 March 2019 / Revised: 30 April 2019 / Accepted: 30 April 2019 / Published: 10 May 2019

Abstract

:
In this paper, we describe the synthesis and gas adsorption properties of a porous carbonaceous material, obtained from commercial expanded polystyrene. The first step consists of the Friedel-Craft reaction of the dissolved polystyrene chains with a bridging agent to form a highly-crosslinked polymer, with permanent porosity of 0.7 cm3/g; then, this polymer is treated with potassium hydroxide at a high temperature to produce a carbon material with a porous volume larger than 1.4 cm3/g and a distribution of ultramicro-, micro-, and mesopores. After characterization of the porous carbon and determination of the bulk density, the methane uptake was measured using a volumetric apparatus to pressures up to 30 bar. The equilibrium adsorption isotherm obtained is among the highest ever reported for this kind of material. The interest of this product lies both in its excellent performance and in the virtually costless starting material.

Graphical Abstract

1. Introduction

The numerous applications of methane as an energy vector would benefit greatly from adsorbed natural gas (ANG) technologies [1,2,3], which are expected to compensate for the relatively low energy density of gaseous methane reducing the costs related to compressed or liquified natural gas (CNG or LNG, respectively) approaches. With suitable adsorbers, the gas storage pressure in tanks could be lowered up to 20% of the value necessary in CNG [4], or alternatively, the stored quantity could be largely increased at the same pressure. These expectations have been quantified by the U.S. Department of Energy (DOE) with the storage target of 180 cm3(STP)/cm3 at 35 bar (where STP stands for standard temperature and pressure, 273 K and 1 bar), raised successively to 263 cm3(STP)/cm3, though it is a value thought to be too ambitious by some researchers [5].
Among the various classes of materials proposed for ANG applications [6,7,8,9,10,11,12,13,14,15], activated porous carbons seem the most promising for several reasons [3,4,16,17,18,19,20,21]: versatility, which allows for tuning of the porosity by tailoring the starting materials and the reaction conditions; high mechanical and chemical stability; and finally, the possibility to design cheap and scalable productions.
Here, we describe the preparation and characterization of a porous carbon with a very high methane uptake capacity, obtained through an easy and scalable reaction from expanded polystyrene (a virtually costless material which can be recycled from the packaging industry). The very good performances of this adsorber are related to the favorable pore distribution in the regions of micropores (7–20 Å) and small mesopores (20–50 Å) coupled with high bulk density, leading to an unusually large uptake on a volume basis.
The material was prepared in two steps: first, a hyper-crosslinked polymer (HCP) was obtained with the Friedel-Crafts reaction from expanded polystyrene (PS): this material is referred to as HCP-PS in the following. HCP have been widely studied [22,23,24,25,26,27,28] for their simplicity of synthesis [29,30,31] and excellent mechanical and textural properties. Cooper et al. studied the crosslinking reaction of various polystyrenes synthesized in situ with different molecular weights; Fu et al. [32] reported the same reaction on expanded PS, using 1,2-dichloroethane as the crosslinking agent [33]. Very recently, waste polystyrene foam was used to prepare cross-linked polymers through a Friedel-Crafts reaction with acetone and aluminum chloride in the presence of silica nanoparticles, followed by calcination to obtain a porous carbon [34]; another porous carbon was prepared from PS by pyrolysis and chemical activation with KOH [35]. Then, HCP-PS was chemically and thermally activated, producing a highly porous carbonaceous material, named KPS-1. Analogous procedures were recently employed to prepare porous carbons from HCP [36,37,38,39,40]. We have also followed this approach in the past starting from tetraphenylmethane, testing different reaction conditions to optimize the textural properties of the products [31,41,42].

2. Materials and Methods

As mentioned above [31,32] and illustrated in Figure 1, the hyper-crosslinked polymer HCP-PS was obtained using the Friedel-Crafts reaction from expanded polystyrene (PS), using ferric chloride as a catalyst and formaldehyde dimethyl acetal (FDA) as a bridging agent. 20 g of polystyrene from packaging (PS) and 93.1 g of FeCl3 (0.57 mol) were suspended in 0.54 L of dichloroethane (DCE). The mixture was stirred mechanically at room temperature to obtain a homogeneous solution; then, 54 mL (0.61 mol) of formaldehyde dimethylacetal (FDA) were added dropwise. The mixture was stirred at room temperature for 30 min and then heated at 80 °C for 18 h. After cooling to room temperature, the thick gel was diluted with ethanol and washed several times with EtOH and water until a neutral pH was reached. Finally, the solid was dried in the oven at 110 °C overnight (the material obtained is named HCP-PS).
To obtain the porous carbon, 2 g of HCP-PS were homogeneously grinded with 6 g of KOH (0.107 mol) under inert conditions. Then, the mixture was placed in a crucible of alumina and thermally treated under a N2 flow with a ramp of 2 °C/min up to 800 °C, and subsequently held under isothermal conditions for 1 h. After the chemical activation, [23] all the resulting carbons were washed with deionized water (250 mL), with 2M HCl (200 mL) and washed again with deionized water to remove potassium salts and to neutralize the solution, and then dried at 110 °C for 18 h (the final material was named KPS-1).
The materials were characterized by Fourier Transform Infrared (FTIR) spectra, recorded with a Brucker Equinox 55 spectrometer (Billerica, USA), equipped with a Deuterated triglycine sulfate detector (DTGS) pyroelectric detector with 4 cm−1 resolution, and Raman spectra, recorded as prepared powders using a Jobin Yvon HR800 Lab-Ram μ -spectrometer (Kyoto, Japan), equipped with an Olympus BX41 microscope, a He-Ne 20 mW laser working at 632.8 nm, and a charge-coupled device (CCD).
The pore structures of HCP-PS and KPS-1 were investigated by adsorbing N2 at 77 K and CO2 at 273 K and analyzing the adsorption isotherms using the Quenched Solid Density Functional Theory (QSDFT) method (using carbon slit/cylindrical pore parameters) [43,44].
Solid-state Nuclear Magnetic Spectra (NMR) spectra were acquired on a Bruker Avance III 500 spectrometer (Billerica, USA), and a wide bore 11.7 Tesla magnet with operational frequencies for 1H and 13C of 500.13 and 125.77 MHz, respectively. A 2.5 mm double resonance probe with Magic Angle Spinning (MAS) was employed in all experiments. The magnitude of radio frequency field was 131 kHz for 1H MAS NMR and relaxation delays, d1, between accumulations was 3 s. For the 13C cross-polarization (CP) magic angle spinning (MAS) experiments, the proton radio frequency (RF) of 100 and 42 kHz were used for initial excitation and decoupling, respectively.
During the CP period, the 1H RF field was ramped using 100 increments, whereas the 13C RF field was maintained at a constant level. During the acquisition, the protons were decoupled from the carbons by using a Spinal64 decoupling scheme. A moderate ramped RF field of 54 kHz was used for spin-locking, while the carbon RF field was matched to obtain an optimal signal and CP contact times of 0.5 ms were used. The 13C NMR spectra were also acquired using DP (direct polarization) MAS-based experiments under high-power proton-decoupling conditions.
To avoid baseline distortions and to remove 13C background signals associated with the probe in direct polarization magic angle spinning (DPMAS) experiments, a special pulse program (aringdec) was used from the Bruker topspin library. The magnitude of the radio frequency field was 80 kHz for 13C MAS NMR, and the 1H decoupling field was 66 kHz, as well as the relaxation delays, d1, between accumulations was 30 s. All chemical shifts were reported using the δ scale and externally referenced to tetramethylsilane at 0 ppm.

3. Results and Discussion

3.1. Vibrational Characterization

The FTIR spectrum of HCP-PS is reported in Figure 2. In the high-frequency region, both the PS precursor (curve a) and the HCP (curve b) are characterized by bands at 3100–3000 cm−1, attributed to aromatic C–H groups stretching modes. After polymerization, the group of bands in the region 3000–2800 cm−1 due to the stretching of aliphatic C–H became more intense due to methylene linkers between the aromatic rings. The low-frequency region shown in the PS spectrum the structural bands were due to –CH2 and aromatic –CH2 bending bands. The spectrum of HCP shows new bands in the region 1800–1700 cm−1 and 950–650 cm−1 due to the higher number of positions substituted on the aromatic rings after the polymerization. Also, the bands at 1450 cm−1 due to the –CH2 bending mode of the methylene linker, along with the band 1262 cm−1 due to –CH2 wagging modes of the chloro-methylene groups confirm the successful cross-linking reaction.
Raman spectroscopy was used to evaluate the carbonization degree after the KOH-activated thermal process described above; the spectrum of KPS-1 is shown in Figure 3. The KPS-1 Raman spectrum shows two main vibrational modes at 1329 and 1593 cm−1. The 1593 cm−1 mode (G peak) corresponds to the Raman-allowed E 2 g mode in the ideal graphite, and the 1329 cm−1 mode (D peak) corresponds to the disorder-induced band, which is associated to the large density of phonon states [45]. In particular, the strong D-band peak demonstrates that the microporous carbon has a low degree of graphitization ( I D / I G = 1.16) and contains a significant amount of disordered sections and defects [46].

3.2. Pore-Size Analysis

To evaluate the textural properties of the synthesized materials, we measured the adsorption isotherms of nitrogen at 77 K and carbon dioxide at 293 K, both in HCP-PS and in KPS-1. With N2, HCP-PS shows a type IV isotherm (with specific surface area, SSABET, of 739 m2/g) with a pronounced hysteresis loop between 0.9 and about 0.4 P/P0, evidencing the presence of mesopores in the material. On the other hand, the derivated carbon KPS-1 shows a pseudo-Langmuir isotherm of type I (SSABET = 2637 m2/g) and a small hysteresis loop of type H4 that can be associated to the presence of narrow slit pores, as commonly found for nitrogen sorption isotherms on activated carbons. The porosity of both the materials was described in greater detail by applying QSDFT analysis to the adsorption isotherms.
The N2 adsorption isotherms for the two materials are shown in Figure 4, and the corresponding pore size distributions (PSD) and cumulative pore volumes (CPV) are compared in Figure 5.
In KPS-1, a rich family of micropores appears below 10 Å. To investigate this region in greater detail, this material was further analyzed by adsorbing CO2 at 273 K: the QSDFT analysis was applied to the CO2 isotherm, providing the PSD and CPV for ultramicropores, reported in Figure 6. The smallest pores have been described in much greater detail by CO2 adsorption at the higher temperature, as is well-known: the ultramicropores around 4–7 Å width are clearly characterized by this experiment. Notably, both gases find a family of micropores at 9 Å, though their relative abundance is different in the N2 and CO2 curves; however, the two gases provide very similar values for the total microporous volume (CPV).
HCP-PS presents a porous volume of 0.74 cm3/g, of which 0.11 cm3/g is due to micropores (below 20 Å width): the analogous systems prepared by the Friedel-Crafts reaction from tetraphenylmethane, in different conditions, showed porous volumes in the range 0.64–0.83 cm3/g, with microporous contributions from 0.16 to 0.21 cm3/g [31]. Other HCP obtained from benzene, thiophene, and pyrrole were found to have porous volumes of 1.52 (0.40), 0.33 (0.22), and 0.25 (0.14) cm3/g, respectively (in parentheses are the microporous volumes) [16].
After the chemical and thermal activation, the porosity increased significantly, exceeding 1.40 cm3/g (note that pores above 200 Å width, approximately, become less and less important in gas adsorption processes), and the pore distribution changes deeply too. The same effect was reported after the carbonization of the HCP polymers mentioned above, where their porous volume increased to 1.58 (for benzene monomer), 1.51 (thiophene), and 3.14 (pyrrole) cm3/g [16].
The micropores in HCP-PS appear in a quite narrow distribution around 15 Å, while the mesopore family is widely spread above 30 Å width. In KPS-1, on the other hand, micropores split in two narrow peaks around 9 and 13 Å, and ultramicropores appear also, between 5 and 6 Å, as clearly shown by CO2 PSD in Figure 6. Overall, the KPS-1 microporous volume reaches 0.7 cm3/g; a large family of mesopores appears between 20 and 40 Å, adding 0.4 cm3/g to the porous volume, while a broad distribution of mesopores exist with a larger size, contributing approximately 0.32 cm3/g to the total volume. The porous volumes of the materials are resumed in Table 1, and compared to the volumes recently reported for other porous carbons obtained from PS.

3.3. Solid State NMR

The nature of hyper-crosslinking in HCP-PS was also investigated using solid-state 13C and 1H NMR spectroscopy. The HCP-PS 13C CPMAS NMR spectrum, recorded using 0.5 ms cross polarization contact time and 20 kHz MAS rate, is shown in Figure 7.
Aromatic 13C peaks in the range of 120–150 ppm were assigned as following: 128 ppm for the aromatic C–H and 138 ppm for the methylene- and/or methine-substituted aromatic carbons [31,47]; there are no 13C resonances above 145 ppm, confirming the absence of free polystyrene units in HCP-PS [48].
In the aliphatic region, the 13C resonances at 42 and 36 ppm were assigned to the methylene units of the polystyrene blocks and to the CH2 (benzylic carbon) linker. Polystyrene methine carbons appeared as a very broad resonance centered at 50 ppm, and this assignment was further supported by the intensity increase in the long contact-time CPMAS experiment (data not shown). Additional resonance at 72 ppm, is assigned to CH2OH groups, substituted on the aromatic rings [31]. On the other hand, CH2Cl carbons formed in the benzene chloromethylation during Friedel-Crafts reaction were expected at 43 ppm, and their presence cannot be ruled out. Moreover, a strong broad peak was also observed at 15 ppm and assigned to a CH3 group due to the methylation and/or ethylation of aromatic rings [49]; the unusual broad peak observed at around 190 ppm is tentatively assigned to carbonyl carbons.
Likewise, the 13C NMR spectrum was recorded on carbonized material, KPS-1. In this case, we employed the 13C DPMAS NMR technique, since the low proton content and the influence of paramagnetic interactions in KPS-1 are problematic for recording a 13C NMR spectrum using the CPMAS technique [50].
Indeed, a combination of several technical challenges, such as the highly electrically conductive nature of carbonized material, the magnetic susceptibility effects observed in graphitic material, the very low isotopic abundance of 13C, very long carbon recycle delay, and the low sample volume (less than 10 mg in a 2.5 mm rotor) made the acquisition of a good 13C spectrum quite problematic [50].
Nevertheless, the 13C spectrum of KPS-1, obtained at a MAS rate of 30 kHz and shown in Figure 8, revealed a very broad resonance in the aromatic region and three narrow resonances in the aliphatic region. A typical resonance of a carbonized material appears at 129 ppm with a down-field shoulder at 150 ppm. The broad peak centered at 129 ppm is assigned to the presence of sp2 hybridized carbons sites as in graphitic material [51,52,53,54]. Furthermore, the broad shoulder centered at 150 ppm was due to the advancement of polycyclization of the benzene rings during carbonization. The narrow resonances at 7, 19, and 27 ppm were either due to the methyl and ethyl carbons generated upon the methylene disproportionation during carbonization, and/or the entrapped aliphatic carbon fragments in the hierarchical pores of the material.
To further test the above hypothesis, we employed the 1H MAS NMR technique, which proved particularly useful for studying molecular adsorption inside porous carbon materials. As shown in Figure 8, the HCP-PS polymeric material presents peaks due to both aliphatic and aromatic protons. Upon carbonization of the hyper-crosslinked polymeric material, intensity due to aromatic and aliphatic protons decreases dramatically, and intense multiple resonances appear at around −3 ppm (Figure 8 and the inset).
Such a strong up-field 1H shift (relative to TMS at 0 ppm) is highly unusual for aliphatic protons; however, proton species close to porous carbon surfaces can experience a reduced local magnetic field owing to the circulation of nearby delocalized π -electrons, leading to large chemically-shielded proton environments. The protonic species can be either structural or adsorbed in nature, and their chemical shifts can be influenced by the carbon ring currents, as has been reported for plane and curved graphene sheets, nanotubes, and fullerene-like elements [55,56,57]. As discussed above, these protonic species are probably associated with the aliphatic carbons fragments that appeared in the 13C NMR spectrum. However, a further NMR characterization is necessary for the detailing of chemical compositions of KPS-1, which is beyond the scope of this paper.
Then, 13C and 1H NMR spectroscopy unambiguously confirmed the hyper-crosslinking of the polystyrene units during the formation of HCP-PS. Moreover, carbon linkages such as benzylic units, derived from FDA between aromatic rings were identified. Finally, polycyclization of the benzene rings and the aliphatization of aromatic rings during carbonization were also determined.

3.4. Methane Adsorption

Before testing the methane adsorption in KPS-1, the synthesized fine powder needed to be compressed in tablets, allowing for the measure of the packing density (sometimes referred to as bulk density) used to estimate the volume-based gas uptake. After the compression, the KPS-1 packing density was 0.50 g/cm3, and the PSD and CPV were measured again on the compressed sample, without significant changes with respect to the as-synthesized powder up to pores of 200 Å width, showing that packing does not affect the micro- and mesopore network, while removing the interparticle voids and possibly part of the macropores.
The uptake of methane on mass and volume bases, measured for compressed KPS-1 at 298 K with the procedure described in ref. [58], is shown in Figure 9, compared to the data reported in Ref. [18] for one of the best-performing porous carbons (LMA738), often used as a benchmark for methane adsorption. Note that both volume- and mass-based uptakes are of interest for large-scale applications, depending on whether the final weight or volume of the container is the limiting factor.
The results are very satisfying—at intermediate pressure (about 30 bar), both measures of uptake are markedly superior to the results of the best carbon-based materials described so far. The good mass-based uptake can be ascribed to the high microporosity (effective at low pressure), coupled to a large fraction of “small” mesopores (20–40 Å wide) but also to a long tail of wider mesopores, so that the adsorption is very high throughout the whole pressure range. Furthermore, the packing density is large enough to also maintain the good performance in the volume-based scale.
The adsorption performance of KPS-1 is compared to the results obtained at the same temperature for the best carbon-based materials in Table 2.
Another measure of the gas uptake has recently been suggested—namely, the storage capacity [18], designed to more accurately predict the performance of a given adsorber in real operative conditions. The storage capacity ( n s t g ), expressing the density of gas stored in an actual tank completely filled by the adsorber, is defined by the following equation:
n s t g = n e x c + ρ g a s 1 ρ p a c k ρ H e
Combining the excess uptake on a volume basis ( n e x c ) with the free gas density ( ρ g a s ), the quantity in parenthesis estimates the fraction of “dead volume” in the container from the adsorbent skeleton density ( ρ H e ) and its packing density ( ρ p a c k ). KPS-1 skeleton density was measured by helium pycnometry as 2.32 g/cm3, which is a rather high value, confirming that the material is strongly amorphous, as suggested by Raman spectra.
The storage density provided by KPS-1 is reported in Figure 10; also in this case, KPS-1 performance is extremely good, as the storage capacity reaches 168 cm3(STP)/cm3 at 30 bar, larger than the best result published so far for a porous carbon (148 cm3(STP)/cm3 for LMA738 in Ref. [18]).

4. Conclusions

In this paper, we have described a new porous carbon material (KPS-1) able to adsorb a very large quantity of gaseous methane in a wide range of pressures. The material was obtained first by a Friedel-Crafts reaction on expanded polystyrene to get a highly hyper-crosslinked polymer (HCP-PS), and then with an activated carbonization of this polymer. Both HCP-PS and KPS-1 were carefully characterized by FTIR and Raman spectroscopy, which showed the degree of polymerization first and of carbonization after the activation process, as well as by SS-NMR, providing details on the nature of the chemical moieties formed in the process. Then, the porosity of both the polymer and the activated carbon were estimated with QSDFT analysis of nitrogen and CO2 adsorption isotherms.
Thanks to the optimal combination of micro- and mesoporosity and packing density, KPS-1 presented mass-based and volume-based methane uptakes, as well as storage capacities which were among the highest presented so far for this kind of material. KPS-1 was also synthesized starting from a commercial expanded polystyrene peanut through a cheap and easily scalable procedure, suggesting the possibility of a large-scale production from recycled materials. The KPS-1 adsorption capacity towards other gases, primarily CO2, as well as the test of various sources of expanded PS with different molecular weights of the starting material, will be described in future studies.

Author Contributions

G.G. and M.E. proposed the idea; G.G., M.E. and L.T. synthesized the materials; G.G. and M.E. characterized the samples; E.M. and S.B. measured the methane adsorption; M.C. and L.M. supervised the work and provided funding; G.G and M.C. wrote the paper. All the authors have discussed and critically reviewed the manuscript, and agreed with all the content.

Funding

This work was funded by SOL Group and by the Italian Ministry of Education, University and Research (PRIN-2010A2FSS9).

Acknowledgments

Katia Sparnacci (Università del Piemonte Orientale) is warmly thanked for the measure of PS molecular weight.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Byamba-Ochir, N.; Shim, W.; Balathanigaimani, M.; Moon, H. High Density Mongolian Anthracite Based Porous Carbon Monoliths for Methane Storage By Adsorption. Appl. Energy 2017, 190, 257–265. [Google Scholar] [CrossRef]
  2. Rash, T.; Gillespie, A.; Holbrook, B.; Hiltzik, L.; Romanos, J.; Soo, Y.; Sweany, S.; Pfeifer, P. Microporous Carbon Monolith Synthesis and Production for Methane Storage. Fuel 2017, 200, 371–379. [Google Scholar] [CrossRef]
  3. Kizzie, A.; Dailly, A.; Perry, L.; Lail, M.; Lu, W.; Nelson, T.; Cai, M.; Zhou, H.C. Enhanced Methane Sorption in Densified Forms of a Porous Polymer Network. Mater. Sci. Appl. 2014, 5, 387–394. [Google Scholar] [CrossRef]
  4. Casco, M.; Martínez-Escandell, M.; Kaneko, K.; Silvestre-Albero, J.; Rodríguez-Reinoso, F. Very High Methane Uptake on Activated Carbons Prepared from Mesophase Pitch: A Compromise Between Microporosity and Bulk Density. Carbon 2015, 93, 11–21. [Google Scholar] [CrossRef]
  5. Simon, C.; Kim, J.; Gomez-Gualdron, D.; Camp, J.; Chung, Y.; Martin, R.; Mercado, R.; Deem, M.; Gunter, D.; Haranczyk, M.; et al. The Materials Genome in Action: Identifying the Performance Limits for Methane Storage. Energy Environ. Sci. 2015, 8, 1190–1199. [Google Scholar] [CrossRef]
  6. Makal, T.; Li, J.R.; Lu, W.; Zhou, H.C. Methane Storage in Advanced Porous Materials. Chem. Soc. Rev. 2012, 41, 7761–7779. [Google Scholar] [CrossRef] [PubMed]
  7. He, Y.; Zhou, W.; Yildirim, T.; Chen, B. A Series of Metal-organic Frameworks with High Methane Uptake and An Empirical Equation for Predicting Methane Storage Capacity. Energy Environ. Sci. 2013, 6, 2735–2744. [Google Scholar] [CrossRef]
  8. Konstas, K.; Osl, T.; Yang, Y.; Batten, M.; Burke, N.; Hill, A.; Hill, M. Methane Storage in Metal Organic Frameworks. J. Mater. Chem. 2012, 22, 16698–16708. [Google Scholar] [CrossRef]
  9. Furukawa, H.; Yaghi, O. Storage of Hydrogen, Methane, and Carbon Dioxide in Highly Porous Covalent Organic Frameworks for Clean Energy Applications. J. Am. Chem. Soc. 2009, 131, 8875–8883. [Google Scholar] [CrossRef]
  10. Feng, X.; Ding, X.; Jiang, D. Covalent Organic Frameworks. Chem. Soc. Rev. 2012, 41, 6010–6022. [Google Scholar] [CrossRef] [PubMed]
  11. Xiang, Z.; Cao, D. Porous Covalent-organic Materials: Synthesis, Clean Energy Application and Design. J. Mater. Chem. A 2013, 1, 2691–2718. [Google Scholar] [CrossRef]
  12. Yuan, D.; Lu, W.; Zhao, D.; Zhou, H.C. Highly Stable Porous Polymer Networks with Exceptionally High Gas-uptake Capacities. Adv. Mater. 2011, 23, 3723–3725. [Google Scholar] [CrossRef]
  13. Ben, T.; Pei, C.; Zhang, D.; Xu, J.; Deng, F.; Jing, X.; Qiu, S. Gas Storage in Porous Aromatic Frameworks (PAFs). Energy Environ. Sci. 2011, 4, 3991–3999. [Google Scholar] [CrossRef]
  14. Wood, C.; Tan, B.; Trewin, A.; Su, F.; Rosseinsky, M.; Bradshaw, D.; Sun, Y.; Zhou, L.; Cooper, A. Microporous Organic Polymers for Methane Storage. Adv. Mater. 2008, 20, 1916–1921. [Google Scholar] [CrossRef]
  15. Cooper, A. Conjugated Microporous Polymers. Adv. Mater. 2009, 21, 1291–1295. [Google Scholar] [CrossRef]
  16. Lee, S.J.; Bae, Y.S. Review of Molecular Simulations of Methane Storage in Metal-organic Frameworks. J. Nanosci. Nanotech. 2016, 16, 4284–4290. [Google Scholar] [CrossRef]
  17. Marco-Lozar, J.; Kunowsky, M.; Carruthers, J.; Linares-Solano, A. Gas Storage Scale-up at Room Temperature on High Density Carbon Materials. Carbon 2014, 76, 123–132. [Google Scholar] [CrossRef]
  18. Casco, M.; Martínez-Escandell, M.; Gadea-Ramos, E.; Kaneko, K.; Silvestre-Albero, J.; Rodríguez-Reinoso, F. High-pressure Methane Storage in Porous Materials: Are Carbon Materials in the Pole Position? Chem. Mater. 2015, 27, 959–964. [Google Scholar] [CrossRef]
  19. Alonso, A.; Moral-Vico, J.; Abo Markeb, A.; Busquets-Fité, M.; Komilis, D.; Puntes, V.; Sánchez, A.; Font, X. Critical Review of Existing Nanomaterial Adsorbents to Capture Carbon Dioxide and Methane. Sci. Total Environ. 2017, 595, 51–62. [Google Scholar] [CrossRef]
  20. Marco-Lozar, J.; Kunowsky, M.; Suárez-García, F.; Carruthers, J.; Linares-Solano, A. Activated Carbon Monoliths for Gas Storage At Room Temperature. Energy Environ. Sci. 2012, 5, 9833–9842. [Google Scholar] [CrossRef]
  21. Marco-Lozar, J.; Juan-Juan, J.; Suárez-García, F.; Cazorla-Amorós, D.; Linares-Solano, A. MOF-5 and Activated Carbons as Adsorbents for Gas Storage. Int. J. Hydrogen Energy 2012, 37, 2370–2381. [Google Scholar] [CrossRef]
  22. Xu, S.; Luo, Y.; Tan, B. Recent Development of Hypercrosslinked Microporous Organic Polymers. Macromol. Rapid Commun. 2013, 34, 471–484. [Google Scholar] [CrossRef]
  23. Li, B.; Gong, R.; Wang, W.; Huang, X.; Zhang, W.; Li, H.; Hu, C.; Tan, B. A New Strategy to Microporous Polymers: Knitting Rigid Aromatic Building Blocks By External Cross-linker. Macromolecules 2011, 44, 2410–2414. [Google Scholar] [CrossRef]
  24. Ding, L.; Gao, H.; Xie, F.; Li, W.; Bai, H.; Li, L. Porosity-Enhanced Polymers from Hyper-Cross-Linked Polymer Precursors. Macromolecules 2017, 50, 956–962. [Google Scholar] [CrossRef]
  25. Davankov, V.A.; Tsyurupa, M.P. Comprehensive Analytical Chemistry. In Hypercrosslinked Polymeric Networks and Adsorbing Materials; Elsevier: Amsterdam, The Netherlands, 2011; Volume 56. [Google Scholar]
  26. Slater, A.; Cooper, A. Function-led Design of New Porous Materials. Science 2015, 348, aaa8075. [Google Scholar] [CrossRef] [PubMed]
  27. Tan, L.; Tan, B. Hypercrosslinked Porous Polymer Materials: Design , Synthesis, and Applications. Chem. Soc. Rev. 2017, 46, 3322–3356. [Google Scholar] [CrossRef] [PubMed]
  28. Yang, Y.; Tan, B.; Wood, C. Solution-processable Hypercrosslinked Polymers By Low Cost Strategies: A Promising Platform for Gas Storage and Separation. J. Mater. Chem. A 2016, 4, 15072–15080. [Google Scholar] [CrossRef]
  29. Dawson, R.; Stöckel, E.; Holst, J.; Adams, D.; Cooper, A. Microporous Organic Polymers for Carbon Dioxide Capture. Energy Environ. Sci. 2011, 4, 4239–4245. [Google Scholar] [CrossRef]
  30. Jing, X.; Zou, D.; Cui, P.; Ren, H.; Zhu, G. Facile Synthesis of Cost-effective Porous Aromatic Materials with Enhanced Carbon Dioxide Uptake. J. Mater. Chem. A 2013, 1, 13926–13931. [Google Scholar] [CrossRef]
  31. Errahali, M.; Gatti, G.; Tei, L.; Paul, G.; Rolla, G.A.; Canti, L.; Fraccarollo, A.; Cossi, M.; Comotti, A.; Sozzani, P.; et al. Microporous Hyper-Cross-Linked Aromatic Polymers Designed for Methane and Carbon Dioxide Adsorption. J. Phys. Chem. C 2014, 118, 28699–28710. [Google Scholar] [CrossRef]
  32. Ratvijitvech, T.; Barrow, M.; Cooper, A.; Adams, D. The Effect of Molecular Weight on the Porosity of Hypercrosslinked Polystyrene. Polym. Chem. 2015, 6, 7280–7285. [Google Scholar] [CrossRef]
  33. Fu, Z.; Jia, J.; Li, J.; Liu, C. Transforming Waste Expanded Polystyrene Foam Into Hyper-crosslinked Polymers for Carbon Dioxide Capture and Separation. Chem. Eng. J. 2017, 323, 557–564. [Google Scholar] [CrossRef]
  34. Zhang, Y.; Shen, Z.; Yu, Y.; Liu, L.; Wang, G.; Chen, A. Porous Carbon Derived from Waste Polystyrene Foam for Supercapacitor. J. Mater. Sci. 2018, 53, 12115–12122. [Google Scholar] [CrossRef]
  35. De Paula, F.; de Castro, M.; Ortega, P.; Blanco, C.; Lavall, R.; Santamaría, R. High Value Activated Carbons from Waste Polystyrene Foams. Micropor. Mesopor. Mater. 2018, 267, 181–184. [Google Scholar] [CrossRef]
  36. Zhang, Y.; Qiang, Z.; Vogt, B.D. Relationship between Crosslinking and Ordering Kinetics for the Fabrication of Soft Templated (FDU-16) Mesoporous Carbon Thin Films. RSC Adv. 2014, 4, 44858–44867. [Google Scholar] [CrossRef]
  37. Deng, G.; Zhang, Y.; Ye, C.; Qiang, Z.; Stein, G.E.; Cavicchi, K.A.; Vogt, B.D. Bicontinuous Mesoporous Carbon Thin Films Via An Order–order Transition. Chem. Commun. 2014, 50, 12684–12687. [Google Scholar] [CrossRef]
  38. Zhang, C.; Kong, R.; Wang, X.; Xu, Y.; Wang, F.; Ren, W.; Wang, Y.; Su, F.; Jiang, J.X. Porous Carbons Derived from Hypercrosslinked Porous Polymers for Gas Adsorption and Energy Storage. Carbon 2017, 114, 608–618. [Google Scholar] [CrossRef]
  39. Modak, A.; Bhaumik, A. Porous Carbon Derived Via KOH Activation of a Hypercrosslinked Porous Organic Polymer for Efficient CO2, CH4, H2 Adsorptions and High CO2/N2 Selectivity. J. Solid State Chem. 2015, 232, 157–162. [Google Scholar] [CrossRef]
  40. Vinodh, R.; Abidov, A.; Peng, M.; Babu, C.; Palanichamy, M.; Cha, W.; Jang, H.T. Synthesis and Characterization of Semiconducting Porous Carbon for Energy Applications and CO2 Adsorption. J. Ind. Eng. Chem. 2015, 32, 273–281. [Google Scholar] [CrossRef]
  41. Canti, L.; Fraccarollo, A.; Gatti, G.; Errahali, M.; Marchese, L.; Cossi, M. An Atomistic Model of a Disordered Nanoporous Solid: Interplay Between Monte Carlo Simulations and Gas Adsorption Experiments. AIP Adv. 2017, 7, 045013. [Google Scholar] [CrossRef]
  42. Gatti, G.; Olivas Olivera, D.; Sacchetto, V.; Cossi, M.; Braschi, I.; Marchese, L.; Bisio, C. Experimental Determination of the Molar Absorption Coefficient of N-Hexane Adsorbed on High-Silica Zeolites. ChemPhysChem 2017, 18, 2374–2380. [Google Scholar] [CrossRef]
  43. Landers, J.; Gor, G.; Neimark, A. Density Functional Theory Methods for Characterization of Porous Materials. Colloids Surf. A 2013, 437, 3–32. [Google Scholar] [CrossRef]
  44. Thommes, M.; Cychosz, K.A. Physical Adsorption Characterization of Nanoporous Materials: Progress and Challenges. Adsorption 2014, 20, 233–250. [Google Scholar] [CrossRef]
  45. Zhao, J.; Yang, L.; Li, F.; Yu, R.; Jin, C. Structural Evolution in the Graphitization Process of Activated Carbon by High-pressure Sintering. Carbon 2009, 47, 744–751. [Google Scholar] [CrossRef]
  46. Cançado, L.; Takai, K.; Enoki, T.; Endo, M.; Kim, Y.; Mizusaki, H.; Speziali, N.; Jorio, A.; Pimenta, M. Measuring the Degree of Stacking Order in Graphite by Raman Spectroscopy. Carbon 2008, 46, 272–275. [Google Scholar] [CrossRef]
  47. Joseph, R.; Ford, W.T.; Zhang, S.; Tsyurupa, M.P.; Pastukhov, A.V.; Davankov, V.A. Solid-state 13C-NMR Analysis of Hypercrosslinked Polystyrene. J. Polym. Sci. A Polym. Chem. 1997, 35, 695–701. [Google Scholar] [CrossRef]
  48. Conte, P.; Carotenuto, G.; Piccolo, A.; Perlo, P.; Nicolais, L. NMR-investigation of the Mechanism of Silver Mercaptide Thermolysis in Amorphous Polystyrene. J. Mater. Chem. 2007, 17, 201–205. [Google Scholar] [CrossRef]
  49. Woodward, R.T.; Stevens, L.A.; Dawson, R.; Vijayaraghavan, M.; Hasell, T.; Silverwood, I.P.; Ewing, A.V.; Ratvijitvech, T.; Exley, J.D.; Chong, S.Y.; et al. Swellable, Water- and Acid-Tolerant Polymer Sponges for Chemoselective Carbon Dioxide Capture. J. Am. Chem. Soc. 2014, 136, 9028–9035. [Google Scholar] [CrossRef]
  50. Wang, Z.; Opembe, N.; Kobayashi, T.; Nelson, N.C.; Slowing, I.; Pruski, M. Quantitative Atomic-scale Structure Characterization of Ordered Mesoporous Carbon Materials By Solid State NMR. Carbon 2018, 131, 102–110. [Google Scholar] [CrossRef]
  51. Vieira, M.A.; Gonçalves, G.R.; Cipriano, D.F.; Schettino, M.A.; Filho, E.A.S.; Cunha, A.G.; Emmerich, F.G.; Freitas, J.C. Synthesis of Graphite Oxide from Milled Graphite Studied by Solid-state 13C Nuclear Magnetic Resonance. Carbon 2016, 98, 496–503. [Google Scholar] [CrossRef]
  52. Parvez, K.; Wu, Z.S.; Li, R.; Liu, X.; Graf, R.; Feng, X.; Müllen, K. Exfoliation of Graphite into Graphene in Aqueous Solutions of Inorganic Salts. J. Am. Chem. Soc. 2014, 136, 6083–6091. [Google Scholar] [CrossRef]
  53. Cai, W.; Piner, R.D.; Stadermann, F.J.; Park, S.; Shaibat, M.A.; Ishii, Y.; Yang, D.; Velamakanni, A.; An, S.J.; Stoller, M.; et al. Synthesis and Solid-State NMR Structural Characterization of 13C-Labeled Graphite Oxide. Science 2008, 321, 1815–1817. [Google Scholar] [CrossRef]
  54. Gao, W.; Alemany, L.; Ci, L.; Ajayan, P. New Insights Into the Structure and Reduction of Graphite Oxide. Nat. Chem. 2009, 1, 403–408. [Google Scholar] [CrossRef]
  55. Huang, P.; Schwegler, E.; Galli, G. Water Confined in Carbon Nanotubes: Magnetic Response and Proton Chemical Shieldings. J. Phys. Chem. C 2009, 113, 8696–8700. [Google Scholar] [CrossRef]
  56. Kibalchenko, M.; Payne, M.C.; Yates, J.R. Magnetic Response of Single-Walled Carbon Nanotubes Induced by an External Magnetic Field. ACS Nano 2011, 5, 537–545. [Google Scholar] [CrossRef]
  57. Forse, A.C.; Griffin, J.M.; Presser, V.; Gogotsi, Y.; Grey, C.P. Ring Current Effects: Factors Affecting the NMR Chemical Shift of Molecules Adsorbed on Porous Carbons. J. Phys. Chem. C 2014, 118, 7508–7514. [Google Scholar] [CrossRef]
  58. Nguyen, H.; Espinal, L.; van Zee, R.; Thommes, M.; Toman, B.; Hudson, M.; Mangano, E.; Brandani, S.; Broom, D.; Benham, M.; et al. A Reference High-pressure CO2 Adsorption Isotherm for Ammonium ZSM-5 Zeolite: Results of An Interlaboratory Study. Adsorption 2018, 24, 531–539. [Google Scholar] [CrossRef]
  59. Li, Y.; Ben, T.; Zhang, B.; Fu, Y.; Qiu, S. Ultrahigh Gas Storage Both At Low and High Pressures in KOH-activated Carbonized Porous Aromatic Frameworks. Sci. Rep. 2013, 3. [Google Scholar] [CrossRef]
  60. Hilton, R.; Bick, P.; Tekeei, A.; Leimkuehler, E.; Pfeifer, P.; Suppes, G. Mass Balance and Performance Analysis of Potassium Hydroxide Activated Carbon. Ind. Eng. Chem. Res. 2012, 51, 9129–9135. [Google Scholar] [CrossRef]
Figure 1. Formation of hyper-crosslinked polymeric material from polystyrene with the Friedel-Crafts reaction using formaldehyde dimethyl acetal (FDA) as a linker.
Figure 1. Formation of hyper-crosslinked polymeric material from polystyrene with the Friedel-Crafts reaction using formaldehyde dimethyl acetal (FDA) as a linker.
Nanomaterials 09 00726 g001
Figure 2. Vibrational spectra in the region 3300–500 cm−1 of (a) the hyper-crosslinked polymer polymer and (b) polystyrene precursor.
Figure 2. Vibrational spectra in the region 3300–500 cm−1 of (a) the hyper-crosslinked polymer polymer and (b) polystyrene precursor.
Nanomaterials 09 00726 g002
Figure 3. Raman spectrum of the carbon sample in the region 3000–500 cm−1.
Figure 3. Raman spectrum of the carbon sample in the region 3000–500 cm−1.
Nanomaterials 09 00726 g003
Figure 4. Adsorption (filled circles) and desorption (empty circles) isotherms of N2 at 77 K in the hyper-crosslinked polymer (a) and in the carbonized material (b).
Figure 4. Adsorption (filled circles) and desorption (empty circles) isotherms of N2 at 77 K in the hyper-crosslinked polymer (a) and in the carbonized material (b).
Nanomaterials 09 00726 g004
Figure 5. Pore size distribution (PSD) and cumulative pore volume (CPV, insert) for HCP-PS (black dotted line) and KPS-1 (red solid line) from N2 adsorption at 77 K.
Figure 5. Pore size distribution (PSD) and cumulative pore volume (CPV, insert) for HCP-PS (black dotted line) and KPS-1 (red solid line) from N2 adsorption at 77 K.
Nanomaterials 09 00726 g005
Figure 6. PSD and CPV for KPS-1 from CO2 adsorption at 273 K.
Figure 6. PSD and CPV for KPS-1 from CO2 adsorption at 273 K.
Nanomaterials 09 00726 g006
Figure 7. 13C NMR spectra: (a) HCP-PS recorded using the CPMAS technique with a CP contact time of 0.5 ms; (b) KPS-1 recorded using the DPMAS technique with a MAS rate of 30 kHz.
Figure 7. 13C NMR spectra: (a) HCP-PS recorded using the CPMAS technique with a CP contact time of 0.5 ms; (b) KPS-1 recorded using the DPMAS technique with a MAS rate of 30 kHz.
Nanomaterials 09 00726 g007
Figure 8. 1H MAS NMR spectra of HCP-PS (a) and KPS-1 (b) recorded using a MAS rate of 15 kHz. Inset: zoomed KPS-1 spectrum.
Figure 8. 1H MAS NMR spectra of HCP-PS (a) and KPS-1 (b) recorded using a MAS rate of 15 kHz. Inset: zoomed KPS-1 spectrum.
Nanomaterials 09 00726 g008
Figure 9. Excess adsorption isotherms at 298 K for CH4 on a (a) mass basis and a (b) volume basis in KPS-1 (solid circles) and LMA738 (open triangles) [18].
Figure 9. Excess adsorption isotherms at 298 K for CH4 on a (a) mass basis and a (b) volume basis in KPS-1 (solid circles) and LMA738 (open triangles) [18].
Nanomaterials 09 00726 g009
Figure 10. Storage density at 298 K for CH4 in KPS-1 (solid circles) and LMA738 (open triangles) [18].
Figure 10. Storage density at 298 K for CH4 in KPS-1 (solid circles) and LMA738 (open triangles) [18].
Nanomaterials 09 00726 g010
Table 1. Porous volume (cm3/g) of the produced materials.
Table 1. Porous volume (cm3/g) of the produced materials.
MaterialTotalMicroporousMesoporous
HCP-PS0.740.110.63
KPS-11.420.700.72
PC from ref. [34]0.70.7
AC800 from ref. [35]1.200.930.27
Table 2. Excess uptake of CH4 at 298 K in KPS-1 and in some of the best-performing materials.
Table 2. Excess uptake of CH4 at 298 K in KPS-1 and in some of the best-performing materials.
MaterialPressure (Bar)Mass-Based Uptake (g/g)Volume-Based Uptake (cm3(STP)/cm3)Bulk Density (g/cm3)Ref.
KPS-1300.2091460.50this work
LMA738350.1911420.53[18]
PY100_700350.1781500.60[4]
DO100_700350.1821600.62[4]
K-PAF-1-750350.207n. a.n. a.[59]
KOH-corncob350.25n. a.n. a.[60]
Activ. monolith300.1361540.80[17,20]

Share and Cite

MDPI and ACS Style

Gatti, G.; Errahali, M.; Tei, L.; Mangano, E.; Brandani, S.; Cossi, M.; Marchese, L. A Porous Carbon with Excellent Gas Storage Properties from Waste Polystyrene. Nanomaterials 2019, 9, 726. https://doi.org/10.3390/nano9050726

AMA Style

Gatti G, Errahali M, Tei L, Mangano E, Brandani S, Cossi M, Marchese L. A Porous Carbon with Excellent Gas Storage Properties from Waste Polystyrene. Nanomaterials. 2019; 9(5):726. https://doi.org/10.3390/nano9050726

Chicago/Turabian Style

Gatti, Giorgio, Mina Errahali, Lorenzo Tei, Enzo Mangano, Stefano Brandani, Maurizio Cossi, and Leonardo Marchese. 2019. "A Porous Carbon with Excellent Gas Storage Properties from Waste Polystyrene" Nanomaterials 9, no. 5: 726. https://doi.org/10.3390/nano9050726

APA Style

Gatti, G., Errahali, M., Tei, L., Mangano, E., Brandani, S., Cossi, M., & Marchese, L. (2019). A Porous Carbon with Excellent Gas Storage Properties from Waste Polystyrene. Nanomaterials, 9(5), 726. https://doi.org/10.3390/nano9050726

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop