Palak Mehra1, Amit Paul1. 1. Department of Chemistry, Indian Institute of Science Education and Research (IISER) Bhopal, Bhopal Bypass Road, Bhauri, Bhopal, MP 462066, India.
Abstract
Carbon-based materials are well established as low-cost, easily synthesizable, and low regeneration energy adsorbents against harmful greenhouse gases such as CO2. However, the development of such materials with exceptional CO2 uptake capacity needs well-described research, wherein various factors influencing CO2 adsorption need to be investigated. Therefore, five cost-effective carbon-based materials that have similar textural properties, functional groups, and porous characteristics were selected. Among these materials, biordered ultramicroporous graphitic carbon had shown an excellent CO2 capture capacity of 7.81 mmol/g at 273 K /1 bar with an excellent CO2 vs N2 selectivity of 15 owing to its ultramicroporous nature and unique biordered graphitic morphology. On the other hand, reduced graphene revealed a remarkable CO2 vs N2 selectivity of 57 with a CO2 uptake of 2.36 mmol/g at 273 K/1 bar. In order to understand the high CO2 capture capacity, important properties derived from adsorption/desorption, Raman spectroscopy, and X-ray photoelectron spectroscopy were correlated with CO2 adsorption. This study revealed that an increase in ultramicropore volume and sp2 carbon (graphitic) content of nanomaterials could enhance CO2 capture significantly. FTIR studies revealed the importance of oxygen functionalities in improving CO2 vs N2 selectivity in reduced graphene due to higher quadruple-dipole interactions between CO2 and oxygen functionalization of the material. Apart from high CO2 adsorption capacity, biordered ultramicroporous graphitic carbon also offered low regeneration energy and excellent pressure swing regeneration ability for five consecutive cycles.
Carbon-based materials are well established as low-cost, easily synthesizable, and low regeneration energy adsorbents against harmful greenhouse gases such as CO2. However, the development of such materials with exceptional CO2 uptake capacity needs well-described research, wherein various factors influencing CO2 adsorption need to be investigated. Therefore, five cost-effective carbon-based materials that have similar textural properties, functional groups, and porous characteristics were selected. Among these materials, biordered ultramicroporous graphitic carbon had shown an excellent CO2 capture capacity of 7.81 mmol/g at 273 K /1 bar with an excellent CO2 vs N2 selectivity of 15 owing to its ultramicroporous nature and unique biordered graphitic morphology. On the other hand, reduced graphene revealed a remarkable CO2 vs N2 selectivity of 57 with a CO2 uptake of 2.36 mmol/g at 273 K/1 bar. In order to understand the high CO2 capture capacity, important properties derived from adsorption/desorption, Raman spectroscopy, and X-ray photoelectron spectroscopy were correlated with CO2 adsorption. This study revealed that an increase in ultramicropore volume and sp2 carbon (graphitic) content of nanomaterials could enhance CO2 capture significantly. FTIR studies revealed the importance of oxygen functionalities in improving CO2 vs N2 selectivity in reduced graphene due to higher quadruple-dipole interactions between CO2 and oxygen functionalization of the material. Apart from high CO2 adsorption capacity, biordered ultramicroporous graphitic carbon also offered low regeneration energy and excellent pressure swing regeneration ability for five consecutive cycles.
Environmental deterioration and climate
change brought considerable
attention from researchers toward the emission of greenhouse gases.[1,2] The massive consumption of fossil fuels leading to carbon dioxide
(CO2) emission is the main cause of these problems.[3] Thus, developing CO2 capture and storage
methodologies demands the undivided attention of researchers.[4] Currently, the amine-scrubbing methodology is
used for industrial CO2 capture.[5] However, this approach has several drawbacks, such as high regeneration
costs, solvent loss, toxicity, amine degradation, and a tendency to
corrode the equipment.[6−8] In comparison, solid porous adsorbents are attractive
as they offer easy handling, simple processing, and low regeneration
costs.[9] In this category, porous materials
having high surface areas, such as zeolites, metal–organic
frameworks (MOFs), silica, nanocarbons, etc., are widely explored
as CO2 adsorbents.[10] Among these,
carbon nanomaterials with narrow pores are of tremendous importance
as they offer a high surface area, large pore volume, ease of surface
modification, excellent thermal and mechanical stability, and minimal
adsorbent regeneration energy.[11,12] Moreover, the synthesis
methodologies are also low-cost, and hence bulk synthesis of these
materials is a viable option.Activated carbons (ACs) and graphene-based
CO2 adsorbents
are independently well explored to achieve high CO2 adsorption
capacity due to their microporous nature and laminar morphology with
functionalized surfaces, respectively.[13] Recently, a simple yet innovative approach has emerged wherein graphene-based
precursors (GO or rGO) and activated carbon materials are combined
to obtain new materials that can enhance the CO2 adsorption
capacity. For example, poly(p-phenylenediamine) (PpPDA)
as a carbon source and GO as a graphene source were used to prepare
an N-doped porous carbon that provided a CO2 uptake of
4.65 mmol/g at 298 K and 5 bar pressure.[14] In another study, Yuan and co-workers reported nitrogen-doped porous
carbon employing melamine-resorcinol-formaldehyde resin and graphene
oxide. This material had shown a CO2 adsorption capacity
of 5.21 mmol/g at 298 K at 5 bar pressure.[15] In other attempts, graphene-like morphology/graphene-based nanomaterials
were also synthesized and explored for CO2 adsorption.[16−20] For example, graphene-like multiscale microporous carbon nanosheets
were synthesized by Shi et al., which provided a CO2 adsorption
capacity of 6.32 mmol/g at 273 K/1 bar.[21] A novel three-dimensional B,N co-doped graphene-like carbon nanosheet
material was developed, which showed 3.57 mmol/g CO2 adsorption
capacity (at 273 K and 1 bar).[22] These
materials have shown great potential for CO2 adsorption
application, which suggests that a detailed study to understand the
impact of various structural features of these nanomaterials on CO2 uptake is of great importance. In this context, Merchán
and co-workers prepared hybrid hydrogels from graphene oxide and activated
carbon fibers and focused on correlating various textural properties
with CO2 uptake.[23] However,
these materials had distinct domains of activated carbon fiber and
GO, which resulted in difficulties correlating adsorption characteristics
with graphene-like structures. The novel idea of investigating the
relation between the properties of materials and CO2 adsorption
can help researchers to synthesize new materials that can achieve
extraordinary CO2 adsorption capacity and selectivity.
Therefore, we opted for low-cost, easily synthesizable carbon materials
to establish new insights in correlating the properties with CO2 uptake capacity.We recently reported a biordered ultramicroporous
graphitic carbon
(BUGC), which has a high surface area, ultramicropore/micropore volume,
and unique graphitization ordering.[24] Considering
all the above examples, we envisioned that the BUGC’s properties
should be beneficial for CO2 uptake and can provide useful
insights into the morphological effects on the adsorption properties
of carbon nanomaterials. With this objective, we selected five nanomaterials,
namely, non-porous carbon (NC), reduced graphene (RG), IMC (immense
microporous carbon), BUGC (biordered ultramicroporous graphitic carbon),
and MMC (microporous mesoporous carbon).[24−26] These materials
have distinct porous and functional group characteristics yet similar
textures, which allowed us to understand the correlations of their
properties with CO2 capture capacity. In the following
few sections, we discuss the syntheses, characterizations, and correlation
plots for these materials with CO2 uptake.
Experimental Section
Materials and Chemicals
Graphite (150 micron, cat#496588),
non-porous carbon (untreated, granular, 4–8 mesh, cat#C2764)
(NC), and commercial micro-mesoporous carbon (100 mesh, CMMC) were
bought from Sigma-Aldrich. Potassium permanganate (KMnO4), sulfuric acid (H2SO4), formic acid (HCOOH),
potassium hydroxide (KOH), acetone, and hydrogen peroxide (H2O2, 50%) were also purchased from Sigma-Aldrich. Acetone
and concentrated hydrochloric acid were supplied by Spectrochem and
Pallav Chemicals, respectively. Milli-Q water (>18 MΩ) was
used
for all synthesis and solution preparation.
Synthesis of Reduced Graphene (RG)
RG was synthesized
by following a protocol previously reported by our group.[25] Briefly, modified Hummer’s method was
used wherein 2 g of graphite (150 μm) was dispersed in 46 mL
of conc. H2SO4 in a 250 mL round-bottom flask.
This dispersion was kept in an ice bath (0 °C), and 6 g of KMnO4 was added carefully. This addition was performed gradually
by covering a time span of 20 min in order to keep the temperature
of the dispersion below 20 °C. This mixture was stirred for 3
h at 35 °C using a reflux condenser. Thereafter, 92 mL of water
was added cautiously over a period of 30 min. Next, in 280 mL of water,
all of these contents were poured, and 10 mL of 30% H2O2 was added to destroy excess KMnO4 (the color changed
from dark brown to yellow). Finally, this material was filtered and
washed with water in a sintered glass filter until the sulfate was
completely destroyed (checked with barium chloride addition), and
it was named graphite oxide (GO). Then, GO was further washed with
20% formic acid solution to intercalate formic acid into the interlamellar
regions of GO. Formic acid-intercalated GO was collected and dried
at 60 °C. To obtain RG, 0.5 g of dried GO was exfoliated at 160
°C in a preheated oven.
Synthesis of IMC and BUGC
Both materials were prepared
by a chemical activation method using KOH as a porogen, which was
reported earlier by our group.[24,26] For IMC, an optimized
ratio of NC and KOH (1:5) was taken in an alumina boat. This mixture
was kept in a temperature-controlled cylindrical tube furnace and
ramped to a temperature of 750 °C with a ramp rate of 5 °C/min
under a constant flow of N2. The sample was carbonized
at 750 °C for 1 h, and then it was allowed to cool down under
N2 flow naturally. Thereafter, the obtained sample was
washed with 5 M HCl to remove the mineral content. This procedure
was followed by washing with distilled water to eliminate chloride
ions. The carbon material procured by this procedure was named immense
microporous carbon (IMC) since the material is mostly microporous
in nature (vide infra).[26] For BUGC, a similar procedure was utilized, except that the carbon
precursor was NC and RG in a ratio of 8:2, a procedure reported previously
by our group.[24] The prepared materials
were dried at 100 °C for 24 h in a hot air oven.
Synthesis of MMC
MMC was also synthesized by the procedure
described above. Herein, instead of NC, CMMC was used as a precursor.[26]
Characterizations
Scanning electron microscopy (SEM)
morphological analysis was performed in a Carl ZEISS (Ultraplus) FE-SEM
instrument at 20 kV. For SEM imaging, dried carbon materials were
spread on carbon tape and coated with gold for 120 s. Transmission
electron microscopy (TEM) experiments were conducted using a TEM FEI
TALOS 200S under an accelerating voltage of 200 kV. For TEM sample
preparation, sample dispersion was prepared in 2-propanol (0.5 mg
in 15 mL), which was drop-casted on a carbon-coated copper grid. Before
imaging, these samples were dried overnight at ambient temperature.
A Lab RAM HR 800 (Horiba) instrument with an excitation wavelength
of 532 nm laser was used to record Raman spectra. Fourier transform
infrared (FTIR) spectroscopy experiments were carried out using a
Perkin-Elmer Model UATR Spectrum Two Instrument in the range of 500
to 4000 cm–1. Degassed samples were directly used
to capture the FTIR spectra. CO2 gas flowed at a rate of
100 mL/min for 12 h to capture the FTIR spectra of CO2-rich
samples. During the FTIR characterization, samples were exposed to
air for <15 s. X-ray photoelectron spectroscopy (XPS) was performed
using a PHI 5000 Versa Prob II, FEI Inc., with a scan time of 1 h
per element for a core level scan (energy band of 20 eV, with pass
setting of 23.5 eV, 0.025 eV step, 100 ms time per step, 5 cycles).
N2 and CO2 adsorption/desorption experiments
were carried out using a Quantachrome Autosorb QUA21011 instrument.
Prior to the adsorption experiments, samples were degassed under vacuum
at 80 °C for 20 h.
Results and Discussion
Morphological Analysis
Morphological analyses of all
nanomaterials were performed using SEM and TEM. The SEM image of NC
showed a nonporous morphology (Figure S1a, SI), whereas RG revealed a layered structure (Figure S1b, SI).[25,26] IMC, BUGC, and MMC
had shown porous characteristics (Figure S1c–S1e, SI), while BUGC also had layered graphitic regions (Figure S1d, SI).[24,26] These observations
were further verified by TEM (Figure ). NC showed non-porous characteristics, while RG showed
layered graphitic structures (Figures a,b).[25,26] IMC, BUGC, and MMC displayed
porous characteristics, whereas BUGC had unique layered graphitic
morphology (Figures c,d,h).[24,26] The magnified HRTEM images of BUGC revealed
biordered characteristics wherein short-range graphitic orders were
visible inside the grain boundary (Figure e), and along the grain boundaries, long-range
graphitic order was present (Figure f).[24] HRTEM images further
exhibited narrow micropores in BUGC (Figure g). An in-depth analysis and discussion about
the morphology of BUGC were provided by us previously.[24] We proposed that the catalyzation of disordered
NC with an ordered RG nanostructure might have occurred for the formation
of BUGC, which resulted in the short-range ordered morphological pattern.
These short-range ordered graphitic structures reorganize randomly,
create a directionally disordered morphology, and generate micropores/ultramicropores.
Moreover, the K+ ion from KOH intercalates between graphitic
layers and facilitates the exfoliation of multilayered graphitic structure
to form a single-layer graphene-like structure under heat treatment.[24]
Figure 1
TEM micrographs of (a) NC,[26] (b) RG,[25] (c) IMC,[26] (d) BUGC,[24] magnified view of
BUGC showing (e) short-range
graphitic order,[24] (f) long-range graphitic
order,[24] and (g) ultramicropores,[24] and (h) MMC.[26]
TEM micrographs of (a) NC,[26] (b) RG,[25] (c) IMC,[26] (d) BUGC,[24] magnified view of
BUGC showing (e) short-range
graphitic order,[24] (f) long-range graphitic
order,[24] and (g) ultramicropores,[24] and (h) MMC.[26]
Functional Group Analysis
The FTIR spectra provided
in Figure S2 revealed the presence of peaks
corresponding to hydroxyl functionalities (C–O) (3300–3700
and 1030 cm–1), alkene/alkane C–H bond (2980–3000
cm–1), ketonic functionalities (C=O) (1695–1720
cm–1), and alkene (C=C) bond (1540–1566
cm–1).[24,27] XPS was also performed
to determine the surface functional groups of nanomaterials. All materials
consisted of carbon and oxygen (Figure S3, SI), and the respective percentages of carbon and oxygen are tabulated
in Table S1. The highest percentage of
oxygen was present in RG followed by MMC, BUGC, and IMC. Next, the
high-resolution C 1s spectra of these materials were deconvoluted
to analyze carbon functionalization (Figure S4 and Table S2, SI). Except NC, all other materials had five
types of functionalizations situated at 284.6 eV for C=C (sp2 carbon), 285.1 eV for C–C/C–H (sp3 carbon), 286.3 eV for C–O (alcohol functionalities), 287.9
eV for C=O (ketonic functionalities), and 290 eV for O-C=O
(carboxylic functionalities) (Figure S4, SI).[24,28] Interestingly, a high percentage of sp2 carbon was present in BUGC followed by IMC and MMC, in accordance
with the SEM and TEM analysis (vide supra) (Table S2, SI). A relatively low sp2 carbon content in RG does not indicate a low graphitic content;
rather, it was due to a higher percentage of oxygen content in comparison
to other materials (Table S2, SI). Notably,
the alcohol functionality (C–O) content was maximum in BUGC
among all materials, whereas the percentage of ketonic functionality
(C=O) content was maximum for RG (Table S2, SI).
Raman Analysis
The Raman spectra of all materials were
fitted and analyzed (Figure S5, SI). Two
major peaks at 1330 and 1590 cm–1 were observed
due to defects (D-band) and stretching of sp2 carbons (G-band)
in carbon lattice, respectively (Figure S5, SI).[27,29] Moreover, D* (∼1110 cm–1), D″ (1500–1540 cm–1), and D′
(1680–1695 cm–1) bands were also present,
corresponding to the disordered graphitic lattice due to Csp3 carbon centers, amorphous phases, and defects of the basal plane,
respectively (Figure S5, SI).[23] The defect ratio (ID/IG) was also determined for all samples
and summarized in Table S3, SI. Importantly,
the ID/IG ratio
was lowest in BUGC, implying that the sp2 carbon character
was the highest in BUGC, which validates the results obtained from
XPS spectroscopy (vide supra).
Porous Characteristics of Materials
Porous characteristics
of all of the materials were analyzed by obtaining N2 adsorption/desorption
isotherms at 77 K and CO2 isotherms at 273 K. Figure shows the isotherms
for all materials, and the inset provides the CO2 isotherm
at 273 K. The isotherm for NC showed a non-porous characteristic (Figure a), whereas RG presented
type-III and type-IV isotherms according to IUPAC classification,
having an H3 type of hysteresis loop, indicating the mesoporous characteristics
of the material (Figure b).[25] IMC and BUGC exhibited a type-I
isotherm, highlighting the microporous nature of the nanomaterials
(Figures c,d).[24,26] MMC revealed a mixed type-I and type-IV isotherm, showing the microporous
and mesoporous characteristics of the material (Figure e).[29] BET surface
areas (SBET) were analyzed in the range
of 0.05–0.2 P/P0 (relative pressure) and are tabulated in Table . The surface area of NC was only 37 m2/g, whereas RG exhibited a surface area of 732 m2/g (Table ). An increasing
trend of surface areas in micropore-rich carbons (type-I isotherm)
with the highest surface area for MMC (3090 m2/g) followed
by IMC (3030 m2/g) and BUGC (2472 m2/g) was
obtained (Table ).
The porous characteristics of materials were analyzed using the non-local
density functional theory (NLDFT) model. To probe the narrow micropores,
CO2 adsorption isotherms were obtained at 273 K and were
also analyzed by the NLDFT model (Figure insets). The combined total pore volume
and pore size distribution from N2 and CO2 isotherms
are provided in Figure S6a–d and Figure S6e–h, respectively. RG was mesoporous
in nature, having a sharp pore size distribution peak at 3.9 nm (Figure S6e, SI). On the other hand, IMC and BUGC
exhibited completely ultramicroporous/microporous characteristics
having pore size distribution in the ranges of 0.33–1.96 and
0.35–1.47 nm, respectively (Figure S6f,g, SI). MMC consisted of bimodal porous characteristics having microporous
(0.34–1.32 nm) and mesoporous characteristics (2.56–5.25
nm) (Figure S6h, SI).
Figure 2
N2 adsorption/desorption
isotherm at 77 K for (a) NC,
(b) RG,[25] (c) IMC,[26] (d) BUGC,[24] and (e) MMC[26] with a CO2 adsorption/desorption isotherm at
273 K as an inset.
Table 1
Porous Characteristics of the Studied
Materials Obtained from N2 Adsorption/Desorption Isotherms
at 77 K (Superscript a) and CO2 Adsorption/Desorption Isotherms
at 273 K (Superscript b)
CO2 uptake at 273 K (mmol/g)
material
SBET (m2/g)a
total pore volume (cm3/g)a
ultramicropore volume (cm3/g) (0.3–0.7 nm)b
micropore
volume (cm3/g) (0.7–20 nm)a
@1.0 bar
@0.15 bar
CO2 uptake
at 298 K (mmol/g) and 1 bar
NC
37
0.04
0.00
0.03
0.55
0.14
0.39
RG
732
3.56
0.12
0.20
2.36
1.12
1.56
IMC
3030
1.49
0.21
1.04
5.56
1.25
2.89
BUGC
2472
1.07
0.31
0.84
7.81
1.98
4.29
MMC
3090
2.30
0.20
0.77
4.00
1.06
2.82
N2 adsorption/desorption
isotherm at 77 K for (a) NC,
(b) RG,[25] (c) IMC,[26] (d) BUGC,[24] and (e) MMC[26] with a CO2 adsorption/desorption isotherm at
273 K as an inset.
CO2 Capture
CO2 uptake capacity
of the materials was performed at two temperatures, i.e., 273 and
298 K (Figure ). BUGC
exhibited an exceptional CO2 adsorption capacity of 7.81
mmol/g at 273 K and relative pressure of 1 bar (Figure a and Table ). Under similar conditions, 5.56, 4.00, 2.63, and
0.55 mmol/g of CO2 were adsorbed by IMC, MMC, RG, and NC,
respectively (Figure a and Table ). CO2 adsorption measurements at 298 K and 1 bar relative pressure
revealed a decrement in adsorption capacity in all materials (Figure b and Table ). However, the order of uptake
was similar, having the highest CO2 uptake of 4.49 mmol/g
for BUGC followed by IMC (2.90 mmol/g), MMC (2.81 mmol/g), RG (1.56
mmol/g), and NC (0.39 mmol/g). Uptake capacity at room temperature
(298 K) was comparatively lower due to the high kinetic energy of
CO2 molecules at 298 K compared to 273 K. At higher temperatures,
the adsorption energy decreases, which leads to reduced CO2 adsorption.[30] At this point, it is essential
to consider the industrial applicability wherein CO2 uptake
at a lower pressure (0.15 bar, post-combustion flue gas streams from
power plants) needs to be as high as possible (>2 mmol/g at 0.15
bar).[8] A high CO2 uptake of
1.98 mmol/g was
obtained for BUGC at 273 K, which was close to the industrial requirement
(Table ). Interestingly,
although the adsorption capacity of RG was comparatively low at a
high pressure (2.56 mmol/g at 1 bar pressure), it still possessed
a relatively high adsorption capacity of 1.12 mmol/g at a low pressure
of 0.15 bar (Table ).
Figure 3
CO2 adsorption isotherms at (a) 273 and (b) 298 K for
different materials.
CO2 adsorption isotherms at (a) 273 and (b) 298 K for
different materials.Figure presents
the comparison of CO2 and N2 adsorption isotherms
for different materials. To understand the adsorption mechanisms,
all isotherms were fitted using either Langmuir single-site (eq S1, SI) or Langmuir-dual site adsorption models
(eq S2, SI), and fitting parameters are
provided in Table S4.[31] Except for RG (at 273 K), other isotherms were well fitted
with a single-site model describing mostly monolayer adsorption. RG
showed the highest accuracy with the Langmuir dual-site model describing
two types of favorable sites for adsorption. The mechanism described
for RG by the dual-site model presumably reflects the edges/defects
as the first adsorption site and pores as second adsorption site.[32] The decrement in “k”
(Langmuir parameter) value with temperature signifies physical adsorption
behavior between CO2 and materials.[33] Fitted isotherms were used to calculate the selectivity
using ideal adsorbed solution theory (IAST).[34] IAST provides ease of determining the selectivity in a gaseous mixture
from equilibrium adsorption capacity obtained from the adsorption
isotherm of the pure component at a particular pressure and temperature.[34] The flue gas consists of more than 70% of N2 in addition to other gases such as water or oxygen gas and
only ∼5–15% of CO2. Therefore, the obtained
molar loadings from fitted adsorption isotherms (0.15 bar for CO2 and 0.85 bar for N2) of pure component isotherms
were used to calculate CO2 vs N2 selectivity.
IAST CO2 vs N2 selectivity for BUGC, IMC, and
MMC were 15, 11, and 13, respectively (Figure d). Fascinatingly, RG displayed the highest
selectivity of 57 (Figure a,d), which can be attributed to the extent of oxygen functionalities
present and a detailed analysis has been provided in next few sections
(vide infra).
Figure 4
CO2 vs N2 adsorption
isotherms at 273 K for
(a) RG, (b) IMC, (c) BUGC, and (d) MMC. (e) CO2 vs N2 selectivity histogram for all materials.
CO2 vs N2 adsorption
isotherms at 273 K for
(a) RG, (b) IMC, (c) BUGC, and (d) MMC. (e) CO2 vs N2 selectivity histogram for all materials.
Scientific Understanding of CO2 Uptake
In
order to understand the science behind the high CO2 uptake
of BUGC and high selectivity for RG, various materials’ characteristics
are analyzed with respect to CO2 uptake (Figure ). First, the porous characteristics
of the materials are compared with uptake capacity in Figure a and Figure S8. The ultramicropore (<0.7 nm) volume showed an excellent
correlation with CO2 capture having a coefficient of determination
(R2) value of 0.99 (Figure a). Ultramicropores offer a large adsorption
potential due to adjacent pore walls (pore wall–wall interactions).
The overlapping of these adsorption potentials generates van der Waals
forces to attract CO2 molecules.[7,35] Next,
the R2 value of 0.73 was obtained upon
analyzing the CO2 adsorption capacity with micropore volume
(0.7–2.0 nm) (Figure S7a, SI). However,
the BET surface area and total pore volume of the materials had very
poor correlations with the adsorption capacity and showed R2 values of 0.45 and 0.01, respectively (Figure S7b,c, SI). Hence, these results firmly
establish that the narrow micropores/ultramicropores (0.3–0.7
nm) are one of the major driving factors for the high CO2 adsorption capacity of BUGC, which agrees well with the previous
reports.[20,36,37]
Figure 5
Correlation
plots of different materials with CO2 uptake
at 273 K and 1 bar with (a) ultramicropore volume, (b) IG/ID ratio from Raman spectra,
and (c) % C=C from C 1s XPS spectra.
Correlation
plots of different materials with CO2 uptake
at 273 K and 1 bar with (a) ultramicropore volume, (b) IG/ID ratio from Raman spectra,
and (c) % C=C from C 1s XPS spectra.The high adsorption capacity of BUGC compared to
other materials
also indicated the importance of unique graphitic regions. Therefore,
to correlate sp2 character, Raman spectroscopy inferences
were utilized. In this context, the inverse of the defect ratio (IG/ID) calculated
from Raman results correlated precisely with the CO2 uptake
capacity (R2 = 0.99) (Figure b). The IG/ID ratio is directly proportional
to the G-band area, which signifies a higher sp2 carbon
content for a higher IG/ID ratio. Thus, this analysis suggests that the higher
sp2 hybridized carbon content helps to improve CO2 adsorption. To further verify this correlation, the percentage composition
of various C 1s species derived from XPS spectra was also evaluated
with CO2 uptake at 1 bar (Figure c and Figure S8, SI). Fascinatingly, the percentage of sp2 carbon (C=C)
correlated perfectly with the CO2 adsorption capacity (R2 = 0.99) (Figure c). A glimpse of this correlation was provided
by Merchán and co-workers in their recent report, wherein they
suggested that this structural property can improve the micropore
volume and thus CO2 uptake.[23] Carbon in sp2 hybridization states is considered to adsorb
CO2 through π–π interactions since sp2 bonds (C=C) are polarizable.[38] Therefore, it can be concluded that the BUGC’s short- and
long-range graphitic ordering, which is a polarizable π-electron
system, has the potential to interact with CO2 molecules
effectively through dispersion forces. Additionally, this unique ordering
created enormous ultramicropores (vide supra) in
BUGC and thus high CO2 uptake capacity was obtained for
this material. Furthermore, oxygen-containing carbons such as hydroxyl/ester
(C–O) and ketonic (C=O) functional groups had relatively
poor correlations with R2 values of 0.81
and 0.84, respectively (Figure S8b,c, SI).The abovementioned correlations of uptake with respect to the percentage
of hydroxyl/ketonic-type functionalities (C–O/C=O) indicate
that the presence of oxygen functionalities also affects the adsorption
of CO2 molecules. Therefore, in order to confirm the role
of these functional groups with CO2 uptake, FTIR experiments
were carried out for BUGC (high adsorption capacity) and RG (high
selectivity) after purging the materials with CO2. Materials
were degassed and purged with CO2 continuously for 12 h,
and thereafter, ex situ FTIR spectra were recorded
and compared with those before purging (Figure and Figure S9 and Table S5, SI). All the peaks for
different functionalities were present after CO2 purging,
which indicates the unchanged identity of carbon materials and suggested
non-covalent physisorption interactions between CO2 and
materials (BUGC and RG) (Figure a and Figure S9a, SI).[39] However, shifts in peak positions for different
functionalities were observed (Figure b and Figure S9b, SI). These
shifts can be correlated as quadrupole–dipole interactions
wherein CO2 acts as a quadrupole and dipoles are the ionic
or polar sites of the adsorbent.[13] Blue
shifts in the wavenumber suggest the electron-donating nature of the
functional groups of the materials, whereas red shifts highlight the
electron-accepting nature.[39] In the case
of BUGC, the magnified spectra in Figure b suggest a blue shift in the wavenumber
related to hydroxyl-type (C–O) (1030 cm–1) and ketone-type (C=O) (1695 cm–1) functionalities,
suggesting the electron-donating nature of these oxygen-containing
groups in the quadrupole–dipole interactions with CO2 molecules. The peak located at 1564 cm–1 for the
graphitic (C=C) bond was also blue-shifted (Figure b), which highlights the participation
of sp2 hybridized carbon in the CO2 adsorption
mechanism in accordance with Raman and XPS correlations (vide
supra). A COO– band situated at 2328 cm–1 was red-shifted to 2315 cm–1, indicating the electron-accepting
nature of COO– functionalities (Figure b). Another shift of this band to a high
wavenumber (2342 cm–1, blue shift) was also observed,
which corresponds to the electron-donating nature of the functional
group (Figure b),
and this shift symbolizes the interactions with the hydrogen atoms
present at the edges of the carbon matrix. Apparently, a red shift
in peak corresponding to the C–H bond (2988 cm–1) was observed, indicating the electron-accepting nature of this
bond (Figure b). Notably,
similar shifts were observed in the case of RG, which are displayed
in Figure S9a,b. However, the wavenumber
shift was higher for RG compared to BUGC (Table S5, SI), which can be directly correlated to the relatively
higher oxygen content in RG. Since the oxygen functionalities are
electronegative in nature, they act as basic adsorption sites, which
results in the attraction of CO2 molecules toward themselves.[35,40] Thus, it can be anticipated that the interactions between oxygen
functionalities of RG and CO2 molecules could be the major
driving force for the high selectivity in RG. BUGC had a lower selectivity
compared to RG due to a smaller percentage of oxygen (7.70% in BUGC
vs 16.03% in RG, Table S1, SI), which is
presumably a requirement for a higher selectivity. At this point,
it can be concluded that the high CO2 adsorption for BUGC
was due to the ultramicroporous nature, unique sp2 carbon-rich
morphology, and presence of oxygen-containing functional groups. In
IMC and MMC, a low ultramicroporous volume and undefined morphology
lead to comparatively lower CO2 uptakes. Interestingly,
in the case of RG, the absence of ultramicropores limits the uptake
capacity of the material; nevertheless, a greater amount of oxygen
content was responsible for exceptional CO2 vs N2 selectivity.
Figure 6
FTIR spectral analysis of BUGC before and after purging
CO2 for 12 h: (a) full range spectra and (b) magnified
regions
of spectra. Respective spectral shifts are color matched for easy
visibility.
FTIR spectral analysis of BUGC before and after purging
CO2 for 12 h: (a) full range spectra and (b) magnified
regions
of spectra. Respective spectral shifts are color matched for easy
visibility.
Thermodynamics and Recyclability of CO2 Capture
In order to understand the thermodynamics of the adsorption, isosteric
heat of adsorption (QST) was determined
using the Clausius–Clapeyron equation at 273 and 298 K (Figure a).[41]QST reflects the interaction
of adsorbate molecules with the adsorbent material. For all materials, QST values ranged between 18 and 35 kJ/mol, indicating
a predominant physisorption phenomenon (<40 kJ/mol), in accordance
with the above fitted “k” (Langmuir
parameter) values (vide supra). The smallest QST was in the range of 18–23 kJ/mol for
IMC and MMC, which signifies their relatively weaker interactions
with CO2 molecules (Figure a). RG has shown high values of heat of adsorption,
indicating strong interactions with CO2 because of high
concentrations of oxygen functional groups, as stated earlier, which
validates the high selectivity (Figure a). An optimum QST in BUGC
(30 kJ/mol) suggests a lower regeneration cost and low-energy desorption
(Figure a).[42] An ease of regeneration in BUGC was further
verified by pressure swing regeneration experiments, wherein excellent
cyclability after five consecutive cycles of CO2 uptake
was observed (Figure b). At this juncture, it is important to highlight that the BUGC
had shown an excellent performance as a CO2 adsorbent,
and the adsorption capacity was significantly higher than that of
recently reported carbon-based adsorbents (Table ).[1,30,43−51] Most importantly, the studied correlations of materials’
properties with CO2 capture presented in this work will
work as a strong foundation for the scientific community, which will
help to further improve CO2 capture by carbon-based materials.
Figure 7
(a) Heat
of adsorption and (b) pressure swing regeneration experiment
of BUGC for five cycles of CO2 uptake at 273 K and 1 bar.
Table 2
Literature Comparison of the Latest
Carbonaceous Materials Utilized for CO2 Adsorption with
BUGC
(a) Heat
of adsorption and (b) pressure swing regeneration experiment
of BUGC for five cycles of CO2 uptake at 273 K and 1 bar.
Conclusions
In conclusion, five cost-effective carbon
nanomaterials were selected
for CO2 capture. Among them, the BUGC nanomaterial prepared
from simple KOH activation of two carbon resources (mechanically infused
NC and RG) has shown the highest CO2 uptake capacity of
7.81 mmol/g at 273 K and 1 bar pressure. This study revealed that
a high ultramicroporous volume helps to improve CO2 capture
since the adjacent pore walls of ultramicropores develop a high adsorption
potential to interact with CO2 molecules. Next, the higher
sp2 carbon content also promotes CO2 adsorption
as the polarizable π-electron cloud interacts with CO2 molecules through dispersion forces. Thus, BUGC having high ultramicroporous
volume, biordered morphology, and graphitic characteristics had a
very high CO2 adsorption capacity. In addition, BUGC revealed
a high CO2 vs N2 selectivity of 15, low regeneration
energy, and 100% CO2 uptake retention for five consecutive
pressure swing cycles. On the other hand, RG has shown a remarkable
CO2 vs N2 selectivity of 57 due to the high
percentage of different oxygen functionalities present in the nanomaterial,
which act as basic adsorption sites due to their electronegative nature
and attract CO2 molecules toward themselves, employing
a higher quadruple–dipole interaction. Finally, it is important
to highlight that the fundamental science developed herein will create
a strong foundation for the further development of new materials to
improve CO2 uptake in the near future.
Authors: Yating Ye; L Vega Martín; M J Sánchez Montero; D López-Díaz; M M Velázquez; M D Merchán Journal: Ind Eng Chem Res Date: 2022-01-13 Impact factor: 3.720