Kristoffer W Bø Hunvik1, Patrick Loch2, Dirk Wallacher3, Alexsandro Kirch4, Leide P Cavalcanti5, Martin Rieß2, Matthias Daab2, Vegard Josvanger1, Sven Grätz6, Fabiano Yokaichiya3, Kenneth Dahl Knudsen1,5, Caetano Rodrigues Miranda4, Josef Breu2, Jon Otto Fossum1. 1. Department of Physics, Norwegian University of Science and Technology, Høgskoleringen 5, 7491 Trondheim, Norway. 2. Bavarian Polymer Institute and Department of Chemistry, University of Bayreuth, Universitätsstraße 30, D-95447 Bayreuth, Germany. 3. Helmholtz-Zentrum Berlin für Materialien und Energie, Hahn-Meitner-Platz 1, 14109 Berlin, Germany. 4. Departamento de Física dos Materiais e Mecânica, Instituto de Física, Universidade de São Paulo, 05508-090 São Paulo, SP, Brazil. 5. Institute for Energy Technology (IFE), P.O. Box 40, N-2027 Kjeller, Norway. 6. Inorganic Chemistry I, Ruhr-Universität Bochum, Universitätsstraße 150, 44780 Bochum, Germany.
Abstract
Due to the compact two-dimensional interlayer pore space and the high density of interlayer molecular adsorption sites, clay minerals are competitive adsorption materials for carbon dioxide capture. We demonstrate that with a decreasing interlayer surface charge in a clay mineral, the adsorption capacity for CO2 increases, while the pressure threshold for adsorption and swelling in response to CO2 decreases. Synthetic nickel-exchanged fluorohectorite was investigated with three different layer charges varying from 0.3 to 0.7 per formula unit of Si4O10F2. We associate the mechanism for the higher CO2 adsorption with more accessible space and adsorption sites for CO2 within the interlayers. The low onset pressure for the lower-charge clay is attributed to weaker cohesion due to the attractive electrostatic forces between the layers. The excess adsorption capacity of the clay is measured to be 8.6, 6.5, and 4.5 wt % for the lowest, intermediate, and highest layer charges, respectively. Upon release of CO2, the highest-layer charge clay retains significantly more CO2. This pressure hysteresis is related to the same cohesion mechanism, where CO2 is first released from the edges of the particles thereby closing exit paths and trapping the molecules in the center of the clay particles.
Due to the compact two-dimensional interlayer pore space and the high density of interlayer molecular adsorption sites, clay minerals are competitive adsorption materials for carbon dioxide capture. We demonstrate that with a decreasing interlayer surface charge in a clay mineral, the adsorption capacity for CO2 increases, while the pressure threshold for adsorption and swelling in response to CO2 decreases. Synthetic nickel-exchanged fluorohectorite was investigated with three different layer charges varying from 0.3 to 0.7 per formula unit of Si4O10F2. We associate the mechanism for the higher CO2 adsorption with more accessible space and adsorption sites for CO2 within the interlayers. The low onset pressure for the lower-charge clay is attributed to weaker cohesion due to the attractive electrostatic forces between the layers. The excess adsorption capacity of the clay is measured to be 8.6, 6.5, and 4.5 wt % for the lowest, intermediate, and highest layer charges, respectively. Upon release of CO2, the highest-layer charge clay retains significantly more CO2. This pressure hysteresis is related to the same cohesion mechanism, where CO2 is first released from the edges of the particles thereby closing exit paths and trapping the molecules in the center of the clay particles.
To mitigate greenhouse
gas emissions, new technologies are required.
As they are cheap, abundant, good CO2 adsorbers,[1−−15] and present in cap-rock formations for carbon storage sites,[16] smectite clay minerals are particularly important
in this context. Understanding how carbon dioxide can selectively
adsorb in the interlayers of clay minerals and tuning those mechanisms
could both pave the way for new adsorbent materials and improve our
understanding of the long-term stability of anthropogenic storage
sites.Smectite clay minerals are phyllosilicates consisting
of 2:1 nanolayers
built from two tetrahedral sheets sandwiching an octahedral sheet.
Isomorphic substitutions in the tetrahedral or octahedral sheet cause
a permanent charge of the 2:1 layer that is compensated by cations
in the interlayer space. In dried smectite clay minerals, the two-dimensional
interlayers are separated by ∼1 nm, providing ∼1000
km2 of accessible surface area per cubic meter of clay
material. Within the interlayers there is a high density of molecular
adsorption sites.[17] The mechanism for molecular
adsorption depends on the interlayer species at each adsorption site
and their affinity for specific molecules. This means that the volumetric
capacity for molecular adsorption in smectite clay minerals can be
very high. In particular, this renders smectite clay minerals very
competitive for CO2 capture, which was recently shown experimentally.[15]Depending on their layer charge, these
silicates can be divided
into smectites, with a layer charge of 0.2–0.6 per formula
unit (pfu) of Si4010F2, and vermiculites,
with a layer charge in the range of 0.6–0.9 pfu.[17] The influence of the layer charge on the hydration
properties of clay minerals has attracted considerable interest.[18−25] Simulations on montmorillonite suggested that a higher layer charge
facilitates the entry of water molecules into the clay interlayers
and decreases CO2 adsorption, while a higher CO2/(CO2 + H2O) mole fraction is acquired when
the charge is low.[26] However, a systematic
experimental study of how the layer charge influences CO2 adsorption in clay minerals has thus far not been conducted. Layer
charge has been shown to have an effect on the adsorption of CH4 in hectorite,[27] where a lower
layer charge enhances CH4 adsorption.In this work,
we investigate the role of the layer charge in CO2 uptake
and swelling in a synthetic clay mineral, fluorohectorite
intercalated with nickel (Ni-Hec). Synthetic Hec shows a homogeneous
charge density and, consequently, a uniform intracrystalline reactivity.[28] It can be synthesized as large defect free particles,[29] providing an excellent template for studying
interactions with CO2 without the interference of defects
or impurities. Ni-Hec has recently been shown to form a corrensite-like
structure, with an ordered interstratifaction of chlorite-like layers
with a composition of [Ni(OH)0.83(H2O)1.17]0.371.17+, and hydrated smectite-like layers
with Ni2+ cations.[30] For this
clay mineral, the hydration follows an atypical, partly continuous
swelling behavior, which is related to the chlorite-like phase in
the interlayer.[30,31] The chlorite-like phase has also
been demonstrated to be responsible for CO2 adsorption,
where the molecules form a reversible bond with the intercalated nickel
hydroxide.[14] The CO2 could be
grafted as a bicarbonate to the condensed nickel hydroxide species.[14] To investigate the layer charge dependency in
a systematic manner, we have conducted X-ray and neutron diffraction
and gravimetric adsorption measurements on dry Ni-Hec prepared with
three different layer charges, 0.3, 0.5, and 0.7 pfu. The samples
were dried to at least 120 °C to ensure the removal of interlayer
water and water coordinated to uncondensed interlayer cations, while
preserving the clay layers and the nickel hydroxide in the chlorite-like
layers.[30] The experimental measurements
are supported by first-principles calculations performed within the
density functional theory (DFT) approach.
Materials
and Methods
Materials
Na-fluorohectorite (Na-Hec) with a nominal
composition of Na(Mg3–Li)Si4O10F2 (x = 0.5 and 0.7) was prepared
via melt synthesis according to published procedures.[29,32] Therefore, the synthesis was carried out in gastight molybdenum
crucibles. NaF (99.995%, Alfa Aesar), LiF (>99.9%, ChemPur), MgF2 (>99.9%, ChemPur), MgO (99.95%, Alfa Aesar), and SiO2 (Merck, fine granular quartz, purum) were mixed according
to the nominal composition of Na-Hec. The crucible was heated to 1750
°C (15 °C/min), held at this temperature for 70 min, cooled
to 1300 °C (55 °C/min) and then to 1050 °C (10 °C/min),
and finally quenched by switching of the power. Subsequent long-term
annealing was used to improve charge homogeneity and phase purity,
resulting in phase pure and layer charge homogeneous materials. Na-fluorohectorite
with x = 0.3 (Na-Hec0.3) was prepared
after layer charge reduction of Na-Hec0.5 after repeated
Mg exchange employing the Hofmann–Klemen effect.[33] The layer charge was checked according to the
literature.[34] The cation exchange capacity
(CEC) was determined using BaCl2 following DIN ISO 11260
and determined to be 75, 129, and 185 mequiv/100 g for layer charges
of 0.3, 0.5, and 0.7 pfu, respectively. These results are in agreement
with calculated values of 78, 130, and 194 mequiv/100 g, respectively.
Ni-Hec was prepared by cation exchange of Na-Hec with a 0.2 M nickel
acetate solution (>10-fold excess of the CEC, five times), following
a published procedure.[30] The exchanged
Ni-Hec was washed five times with Millipore water.Cation exchange
of Ni-Hec with a long-chain n-alkylammonium solution
(C16, C16H33NH3Cl) was performed
with a 10-fold excess of CEC (80 °C, three times) to ensure complete
exchange. The obtained C16-exchanged Ni-Hec was washed five times
with ethanol/water (1:1) and once with ethanol (p.a.) and then dried
at 80 °C. The composition of Ni-Hec (x = 0.3 and 0.7) was determined via inductively
coupled plasma atomic emission spectroscopy (ICP-OES) according to
Loch et al.,[30] comparing the Ni content
of the pristine and C16-exchanged Ni-Hec. Approximately 20 mg of Ni-Hec equilibrated
at a relative humidity of 43% was weighed into 15 mL clean Teflon
flasks. C16-exchanged Ni-Hec was dried
at 80 °C prior to the measurement. After addition of 1.5 mL of
30 wt % HCl (Merck), 0.5 mL of 85 wt % H3PO4 (Merck), 0.5 mL of 65 wt % HNO3 (Merck), and 1 mL of
48 wt % HBF4 (Merck), the sample was digested in a MLS
1200 Mega microwave digestion apparatus for 6.5 min and heated at
600 W (MLS GmbH, Mikrowellen-Labor-Systeme, Leutkirch, Germany). The
closed sample container was cooled to room temperature, and the clear
solution was diluted to 100 mL in a volumetric flask and analyzed
on a PerkinElmer Avio 200 spectrometer.
Powder X-ray Diffraction
Powder X-ray diffraction (PXRD)
experiments during adsorption of CO2 were conducted at
the KMC-2 beamline of the BESSY II light source at Helmholtz-Zentrum
Berlin.[35] A capillary-based sample cell
system, centered in the synchrotron beam, was connected to a gas dosing
system (Teledyne ISCO 260D). The temperature of the sample was directly
measured by a K-type thermocouple mounted close to the measurement
point and connected to a Eurotherm indicator unit 32h8i. A 0.01 mm
wall thickness quartz capillary (Hilgenberg) with a diameter of 0.5
mm was glued in a 1/4 in. VCR weld gland (Swagelok).
Before the measurements, the samples were filled in capillaries and
dried for at least 2 h at 150 °C under high vacuum (10–6 mbar) in an ex situ dedicated capillary drying
station. Subsequently, it was connected via a Swagelok thread to the
gas handling system providing CO2 of quality N55 (99.9995%).
All in situ measurements were carried out at 26 °C.
The diffraction experiments were conducted in transmission geometry
in the 2θ range of 2.5–14.5° using monochromatic
synchrotron radiation (λ = 1.5406 Å). A full 360°
rotation of the capillary in the beam was implemented by a script-controlled
step motor. The diffraction images from the two-dimensional detector
(Bruker Våntec 2000) were integrated using proprietary software.
NIST silicon SRM 640a was used as the external standard for peak positions.
Gravimetric Adsorption
CO2 adsorption measurements
were conducted with an IsoSORP gravimetric sorption analyzer from
Rubotherm. Each sample was prepared by being degassed at 120 ±
5 °C overnight under high vacuum. For each sample, three measurements
were conducted with equilibration times of 1, 2, or 4 h at each pressure
step from vacuum to 35 bar. The temperature was measured with a Pt-100
sensor placed directly underneath the sample crucible. It was surrounded
by a double-walled thermostat controlled by a circulating water bath
CC-K6 from Huber. The temperature stability of the sample was within
22.5 ± 1 °C. The suspension balance has a resolution of
0.01 mg and a reproducibility of <0.002% rdg (≈0.002 mg).
The data for pressure, temperature, and sample weight were continuously
recorded. The measured quantity is the excess adsorbed amount, which
is obtained by correcting for the buoyancy of the skeletal volume
of the sample material and the suspended metal parts (including the
sample holder). The skeletal volume of the three samples was determined
by individual helium isotherms. The buoyancy of the suspended metal
parts was obtained by a blank measurement with CO2. The
densities of helium and CO2 for the given pressure and
temperature conditions were obtained from the equation of state data
provided by NIST.[36]
Computational Methodology
First-principles calculations
based on the DFT were conducted to evaluate basal separation distances
and adsorption energies. The simulations were performed using the
Siesta package.[37] The double-zeta plus
polarization (DZP) and spin-polarized localized atomic orbital basis
sets with a 400 Ry energy cutoff were used. The corrected generalized
gradient approximation developed by Berland and Hyldgaard[38] was employed to account for the van der Waals
interactions. On the basis of the crystallographic structure of our
previous work,[14] the layer charges were
modified by substituting Mg with Li atoms in the supercell (multiple
unit cells). We systematically explored four layer charges (0.25,
0.5, 0.75, and 1.0 pfu), which were chosen to resemble the experimental
stoichiometry. These charges were balanced with the interlayer Ni
cations. For each stoichiometry, distinct Li and Ni interlayer atomic
sites were fully considered and sampled for total energy minimization.
Results and Discussion
Structure Determination
Ni-Hec0.5 forms
an ordered interstratification of a condensed [Ni(OH)0.83(H2O)1.17]0.371.17+ species
in one interlayer and hydrated Ni2+ cations in the adjacent
layer.[30] Due to the similar electron densities
of the two interlayer species, the superstructure reflection is expected
to be weak and was therefore amplified by enhancing the electron contrast
of the interlayers. Cation exchange of the noncondensed Ni2+ interlayer cations with long-chain n-alkylammonium
(C16, C16H33NH3Cl) led to a clearly
visible superstructure as observed by PXRD.[30] This procedure was used to identify a comparable condensed species
and a possible superstructure in Ni-Hec0.7 and Ni-Hec0.3.Similar to Ni-Hec0.5 (Figure 7 of ref (30)), C16-exchanged Ni-Hec0.7 shows a clearly visible reflection of an ordered interstratified
superstructure (Figure S1). The basal spacing
of 40.5 Å [coefficient of variation (CV) of 0.79] can be explained
by the formation of an ordered interstratification of two strictly
alternating interlayer species. The condensed nickel hydroxide species
with a basal spacing of 14.5 Å and a paraffin-like arrangement
of C16 cations with a basal spacing of 26 Å form a corrensite-like
structure during the C16-exchange. The chemical composition was determined
with ICP-OES according to Loch et al.,[30] giving a composition of [[Ni(OH)1.49(H2O)0.58]0.530.58+]Int.1 [[Ni(H2O)6]0.382+]Int.2 [Mg4.6Li1.4]⟨Si8⟩O20F4 for Ni-Hec0.7.Na-Hec0.3, which was used for the preparation of Ni-Hec0.3, cannot be obtained directly from melt synthesis. Thus,
it requires a layer charge reduction procedure prior to cation exchange,[39] which in turn lowers the layer charge homogeneity
compared to those of Ni-Hec0.5 and Ni-Hec0.7. Therefore, C16-exchanged Ni-Hec0.3 showed no superstructure
reflection (Figure S2). A basal spacing
of 17.7 Å (CV = 0.42) is characteristic for a bilayer arrangement
of C16[33,34,40] in the interlayer
space, indicating an occupation of C16 in every interlayer, and is
in accordance with the layer charge of 0.3 pfu. The structure can
consequently be seen as a random interstratification of condensed
and noncondensed interlayer species with a composition of [[Ni(OH)1.10(H2O)0.90]0.100.90+]Int.1 [[Ni(H2O)6]0.252+]Int.2 [Mg5.4Li0.6]⟨Si8⟩O20F4.
In Situ Powder X-ray Diffraction
The
evolution of the (001) or (002) Bragg reflection upon CO2 exposure for Ni-Hec dried at 150 °C
with a layer charge of 0.3, 0.5, and 0.7 pfu is shown in Figures –3. As no ordered superstructure is
observed for Ni-Hec0.3 after C16 exchange, these results
represent the (001) Bragg reflection of a random interstratification
(Figure ), while for
Ni-Hec0.5 and Ni-Hec0.7, it corresponds to the
(002) reflection of an ordered interstratification (Figures and 3). Similar to what was observed for Ni-Hec0.5 by Hunvik
et al.,[14] with an increasing pressure of
CO2 the Bragg reflection moves to lower q values as a result of the swelling process. Swelling is an inherent
one-dimensional process, in which the Bragg reflections gradually
move as the number of swollen interlayers increases and thus the relative
contribution of the interstratified stacks becomes larger.
Figure 1
Evolution of
the (001) Bragg reflection as a function of pressure
at 26 °C for Ni-Hec0.3 recorded via PXRD. The bottom
left panel shows the measured pressure of CO2 applied on
the sample as a function of time, and the bottom right panel shows
a contour plot in which the horizontal axis corresponds to the d spacing (d = 2π/q). The vertical axis corresponds to time scaled by the same horizontal
axis as for the pressure, and the color gradient represents the intensity.
In the top panel, the evolution of the (001) Bragg reflection is plotted
with colors indicating the approximate pressure.
Figure 3
Evolution
of the (002) Bragg reflection as a function of pressure
at 26 °C for Ni-Hec0.7 recorded via PXRD. The bottom
left panel shows the measured pressure of CO2 applied on
the sample as a function of time, and the bottom right panel shows
a contour plot in which the horizontal axis corresponds to the d spacing (d = 2π/q). The vertical axis corresponds to time scaled by the same horizontal
axis as for the pressure, and the color gradient represents the intensity.
In the top panel, the evolution of (002) Bragg reflection is plotted
with colors indicating the approximate pressure.
Figure 2
Evolution
of the (002) Bragg reflection as a function of pressure
at 26 °C for Ni-Hec0.5 recorded via PXRD. The bottom
left panel shows the measured pressure of CO2 applied on
the sample as a function of time, and the bottom right panel shows
a contour plot in which the horizontal axis corresponds to d spacing (d = 2π/q). The vertical axis corresponds to time scaled by the same horizontal
axis as for the pressure, and the color gradient represents the intensity.
In the top panel, the evolution of the (002) Bragg reflection is plotted
with colors indicating the approximate pressure.
Evolution of
the (001) Bragg reflection as a function of pressure
at 26 °C for Ni-Hec0.3 recorded via PXRD. The bottom
left panel shows the measured pressure of CO2 applied on
the sample as a function of time, and the bottom right panel shows
a contour plot in which the horizontal axis corresponds to the d spacing (d = 2π/q). The vertical axis corresponds to time scaled by the same horizontal
axis as for the pressure, and the color gradient represents the intensity.
In the top panel, the evolution of the (001) Bragg reflection is plotted
with colors indicating the approximate pressure.Evolution
of the (002) Bragg reflection as a function of pressure
at 26 °C for Ni-Hec0.5 recorded via PXRD. The bottom
left panel shows the measured pressure of CO2 applied on
the sample as a function of time, and the bottom right panel shows
a contour plot in which the horizontal axis corresponds to d spacing (d = 2π/q). The vertical axis corresponds to time scaled by the same horizontal
axis as for the pressure, and the color gradient represents the intensity.
In the top panel, the evolution of the (002) Bragg reflection is plotted
with colors indicating the approximate pressure.Evolution
of the (002) Bragg reflection as a function of pressure
at 26 °C for Ni-Hec0.7 recorded via PXRD. The bottom
left panel shows the measured pressure of CO2 applied on
the sample as a function of time, and the bottom right panel shows
a contour plot in which the horizontal axis corresponds to the d spacing (d = 2π/q). The vertical axis corresponds to time scaled by the same horizontal
axis as for the pressure, and the color gradient represents the intensity.
In the top panel, the evolution of (002) Bragg reflection is plotted
with colors indicating the approximate pressure.For dried Ni-Hec0.3, initially an asymmetric (001) Bragg
reflection at 0.563 Å–1 (d001 = 11.15 Å) under vacuum (0.07 bar) is observed
(Figure ). During
the CO2 exposure, no changes were observed at 1 and 2 bar
of CO2. As the pressure is increased to 5 bar, the peak
gradually shifts, and the sample starts to swell. At 11 bar, the intensity
is shifted from the educt to the product phase, slowly becoming more
symmetric toward the final pressure. At the final pressure of 50 bar
of CO2, a symmetric (001) Bragg reflection at 0.514 Å–1 (d001 = 12.21 Å)
is observed. The pressure was released quickly after CO2 exposure, and a symmetric peak appears, centered at 0.556 Å–1 (d001 = 11.30 Å)
(Figure S3). The symmetric peak indicates
a higher-order stacked structure, while the value of the basal spacing
reveals the release of most of the CO2.For dried
Ni-Hec0.5, initially a symmetric peak at 0.551
Å–1 (d002 = 11.39
Å) is observed, corresponding to the (002) reflection of the
ordered interstratified structure (Figure ). Similar to the observation of Hunvik et
al.,[14] up to 10 bar the shifts are marginal
for each pressure step. At 10 bar, the reflection gradually shifts
toward the product phase, ending up at 15 bar as a symmetric peak
with only minor changes, before reaching the final pressure. At the
final pressure of 60 bar, a symmetric peak at 0.512 Å–1 (d002 = 12.26 Å) is observed. When
the the pressure is decreased, CO2 is released and the
reflection shifts back to 0.547 Å–1 (d002 = 11.48 Å), forming a significantly
broader peak at higher d spacings compared to that
of the initial state. Compared to Ni-Hec0.3, the onset
of swelling is located at a higher pressure, while the end state after
pressure is decreased is less ordered, as judged from the peak broadening.
This is likely a result of some interlayers still retaining CO2 (discussed below) and suggests that the cohesion of the layers
in this case is stronger than that in Ni-Hec0.3, preventing
the complete desorption of CO2. Included in the Supporting Information are neutron diffraction
measurements (Figures S4 and S5), where
the sample was given more time to equilibrate. Consequently, it is
clear that Ni-Hec0.5 returns to its initial state given
enough time under vacuum (0.003 bar), which confirms the influence
of the higher layer charge on CO2 adsorption.For
dried Ni-Hec0.7, a symmetric (002) Bragg reflection
of the corrensite structure at 0.548 Å–1 (d002 = 11.45 Å) is observed (Figure ). During the exposure to CO2, the peak shape remains almost unchanged until the pressure
reaches 32 bar, when the level of the product phase starts to increase
at the expense of the educt phase. At the final pressure of 50 bar,
a symmetric peak at 0.518 Å–1 (d002 = 12.11 Å) is observed. When the pressure is
subsequently reduced, the (002) Bragg reflection slowly returns to
higher q values, corresponding to a decrease in the
basal spacing. However, the sample does not reach its initial state
and a broad peak centered at 0.527 Å–1 (d002 = 11.90 Å) is observed, which is even
broader than in Ni-Hec0.5. Again, swelling and shrinking
in response to CO2 result in two well-defined states, where
the onset is at an even higher pressure than for the two previous
samples with lower layer charges (0.3 and 0.5 pfu).For the
X-ray diffraction experiments, the equilibration time was
shorter than for the neutron diffraction experiments (Figure S6). In the latter case, when the pressure
is decreased, the basal spacing of Ni-Hec0.7 does not return
to its initial state, indicating a certain retention of CO2 even after longer equilibration times at low pressure. Consequently,
the higher layer charge also assists in the retention of CO2 and confirms the influence of the layer charge on the swelling process.The three samples are compared in Figure , where the d spacing of
the most intense peak of the (001)/(002) Bragg reflection as a function
of pressure is shown. It is evident from the discussion above and Figure that Ni-Hec with
a higher layer charge shows a higher onset pressure for swelling upon
CO2 exposure and, concomitantly, greater retention of the
CO2. This results in a larger hysteresis loop starting
from Ni-Hec0.3 to Ni-Hec0.7, where Ni-Hec0.7 clearly resides in a partly swollen state even after the
CO2 pressure is decreased. The slightly higher basal spacings
of Ni-Hec0.3 and Ni-Hec0.5 might indicate a
certain retention of CO2 but are negligible compared to
that of Ni-Hec0.7 and can be due to a higher stacking order
or differences in the degree of condensation of the chlorite-like
layers.
Figure 4
Evolution of the most prominent feature of the (001)/(002) Bragg
reflection as a function of pressure at 26 °C for Ni-Hec0.3, Ni-Hec0.5, and Ni-Hec0.7. The arrows
show the swelling hysteresis with the increase or decrease in pressure.
Evolution of the most prominent feature of the (001)/(002) Bragg
reflection as a function of pressure at 26 °C for Ni-Hec0.3, Ni-Hec0.5, and Ni-Hec0.7. The arrows
show the swelling hysteresis with the increase or decrease in pressure.To quantify
CO2 uptake
as a function of the layer charge of Ni-Hec, gravimetric adsorption
measurements were performed. The gravimetric excess sorption of Ni-Hec
with the three different layer charges is shown in Figure . The respective densities
obtained from an He isotherm are listed in Table S1. In agreement with the PXRD results, the adsorption should
largely take place in the interlayer space, as the N2 physisorption
isotherm for Ni-Hec0.5 (Figure S7) shows only limited adsorption and no significant BET surface area
(1.8 m2/g). Included in Figure S8 are gravimetric data where the equilibration time at each pressure
step is 1, 2, and 4 h. We observed that the equilibration time has
no effect on Ni-Hec0.3. For Ni-Hec0.5 and Ni-Hec0.7, a dependency on equilibration is noticed in the decrease
in the size of the hysteresis loop with an increase in the equilibration
time. However, for all samples, the final uptake is unaffected by
exposure to CO2 with these equilibration times. The additional
buoyancy due to the increase in volume by the clay swelling in response
to CO2 is not included in the data presented in Figure . At the final pressure
with a fully swollen state, this will add an additional 3–4%
to the final excess adsorption capacity.
Figure 5
Comparison of the gravimetric
adsorption capacity in dried Ni-Hec
with layer charges Ni-Hec0.3, Ni-Hec0.5, and
Ni-Hec0.7 equilibrated for 4 h at each pressure step. The
arrows show the sorption hysteresis with the increase or decrease
in pressure.
Comparison of the gravimetric
adsorption capacity in dried Ni-Hec
with layer charges Ni-Hec0.3, Ni-Hec0.5, and
Ni-Hec0.7 equilibrated for 4 h at each pressure step. The
arrows show the sorption hysteresis with the increase or decrease
in pressure.For Ni-Hec0.3 (Figure ), the uptake of
CO2 starts immediately
between 2 and 6 bar. The uptake rises only slightly above 6 bar, until
the curve flattens around 20 bar, achieving a maximum uptake of 8.6
wt % (2.14 mmol/g) at 35 bar. Upon desorption, no significant mass
loss was observed until approximately 4 bar. Below that point, a large
step occurred and most of the CO2 is released when the
lowest pressure (0.02 bar) is reached. For Ni-Hec0.5 (Figure ), the uptake starts
immediately similar to Ni-Hec0.3 and follows a continuous
trend up to ∼12 bar, where the curve starts to flatten out.
At 35 bar, a maximum excess adsorption of 6.5 wt % (1.59 mmol/g) was
achieved, lower than the uptake observed for Ni-Hec0.3.
Upon desorption, only a small mass loss until approximately 8 bar
can be observed, after which most of the CO2 is released
at the lowest pressure (0.01 bar) and approximately 0.5 wt % CO2 remained in the sample. For Ni-Hec0.7 (Figure ), only a minor uptake
before 13 bar is found, which significantly increases until 30 bar
after which the curve flattens. At 35 bar, a maximum excess adsorption
of 4.5 wt %, 1.08 mmol/g, is observed. Upon desorption, the sample
does not release any significant amount of CO2 above 12
bar. Ultimately, between 2 and 2.5 wt % of CO2 was retained
in the sample.The shape of the adsorption isotherms resembles
that of the water
adsorption isotherms for Na-Hec,[28,41] where the
adsorption occurs between two discrete states. Due to the limited
adsorption of Ni-Hec0.7 before the pressure threshold,
any significant adsorption of CO2 in the bulk can be ruled
out, which would otherwise produce a more gradual adsorption isotherm.
This is consistent with the swelling observed by in situ PXRD that occurs only between two defined states.In terms
of uptake, layer charge plays a distinct role, with a
higher uptake for a lower layer charge. At 35 bar, the CO2 uptake values are 8.6, 6.5, and 4.5 wt % for Ni-Hec with layer charges
of 0.3, 0.5, and 0.7 pfu, respectively. Previously, we demonstrated
that the adsorption mechanism in Ni-Hec0.5 is controlled
by an interaction with the [Ni(OH)0.83(H2O)1.17]0.371.17+ species in the interlayer,[14] and the Ni2+ cations in the smectite-like
layers are unresponsive to CO2 under anhydrous conditions.
For the low-charge clay, less interlayer species is required to counterbalance
the layer charge, and therefore, more space is available in the interlayer
for CO2. This is also confirmed by the measured lower density
from the He isotherm (Table S1) for the
lower-charge clay, because greater formation of nickel hydroxide would
result in a higher density. Given the low density of [[Ni(OH)1.10(H2O)0.90]0.100.90+] species for Ni-Hec0.3 some of the CO2 may
be attached to the interlayer species, and some may be occupying the
interlayer space available between the condensed islands. Previous
observations of CH4 adsorption in hectorite with varying
layer charges find greater CH4 adsorption for a lower layer
charge.[7] In accordance with our conclusions,
this was related to more pore space being available due to fewer cations
being required in the interlayer to balance the lower layer charge.The hysteresis behavior is also influenced by the layer charge.
Ni-Hec0.7 (Figure ) starts adsorbing at much higher pressures than the two other
samples. A difference is also apparent in that for the lower-charge
samples (Ni-Hec0.3 and Ni-Hec0.5) almost all
of the CO2 can be released, whereas in the case of the
high layer charge (Ni-Hec0.7), CO2 remains in
the sample under the used conditions. A higher layer charge results
in stronger electrostatic cohesion between the clay layers, creating
a higher energy barrier for the CO2 to enter the interlayer.
A possible mechanism is illustrated in Figure , showing swelling that first occurs from
the edges of the clay particle. Upon desorption, the CO2 first leaves from regions near the edges. This could partially close
the exit paths, trapping some of the CO2 by the electrostatic
cohesion of the layers. This effect would be more important for a
higher layer charge and, consequently, result in the greater retention
we observe. This is similar to the so-called “ring mechanism”
proposed by Weiss et al.[42] for kaolinite
intercalation, which was also observed for Hec by Stöcker et
al.[43] Due to the large size of the tactoid,
intercalation occurs along all edges of the particle instead of via
a “one-sided wedge” mechanism.
Figure 6
Sketch of the CO2 adsorption process in clay. The CO2 penetrates
the clay from the edges of the clay platelet,
slowly expanding the clay as the CO2 enters. At full adsorption,
the clay is fully expanded. As the pressure is decreased, the CO2 molecules close to the edges are the first to leave the clay,
forming a pocket inside with trapped CO2. With a decrease
in the pressure and given enough time, the clay will slowly return
to its initial dry and collapsed state.
Sketch of the CO2 adsorption process in clay. The CO2 penetrates
the clay from the edges of the clay platelet,
slowly expanding the clay as the CO2 enters. At full adsorption,
the clay is fully expanded. As the pressure is decreased, the CO2 molecules close to the edges are the first to leave the clay,
forming a pocket inside with trapped CO2. With a decrease
in the pressure and given enough time, the clay will slowly return
to its initial dry and collapsed state.These results show a larger dependency on layer charge for CO2 adsorption and swelling compared to what has been observed
for H2O adsorption and/or swelling.[18,19] The crystalline swelling upon hydration of clays depends on the
Coulombic and van der Waals attraction, hydration and Born repulsion
and is inherently hysteretic.[44] For synthetic
saponites, where the charge is located in the tetrahedral sheet, swelling
upon exposure to water occurs at lower values of relative humidity
as the layer charge increases.[18] In addition,
the increase in layer charge led to an increasing amount of water
adsorbed in this clay mineral, due to the larger amount of interlayer
cations allowing greater hydration.[18] For
hectorite, on the contrary, with an origin of the layer charge in
the octahedral sheet, the water adsorption isotherms and the amount
of water adsorbed were independent of the location and the amount
of layer charge.[19] Water strongly interacts
with the interlayer cation, an interaction that is significantly stronger
than the Coulomb attraction between the layers and the interlayer
cation. For CO2, there is a weaker interaction with the
interlayer species than for water. The resulting layer–layer
repulsion force from the presence of CO2 could then be
comparable to the Coulomb attraction, which could explain the large
dependency of layer charge for CO2 swelling as opposed
to the H2O case.
DFT Calculations
This interpretation
is reinforced
by DFT simulations of the system. The cohesion energy of the layers
significantly increases with layer charge (Figure ). For the chlorite-like layer where the
CO2 is believed to enter, the value of the energy minimum
more than doubles. In addition, basal separation distances were determined
as a function of the surface charge. We observed that the equilibrium
configurations of dried smectites have a minor dependence (<0.1
Å) on the surface charge, which is in agreement with previous
studies.[26]
Figure 7
(a) Side view of the Hec molecular model
highlighting the atomic
configuration with a layer charge of 1.0 pfu (unit cell area of 9.2
Å × 5.3 Å) achieved by the substitution of two Mg atoms
with Li atoms. (b) Energy curves for the dehydrated smectite (D1) and for the β-Ni(OH)2 island
(D2) in the interlayer space considering
the role of the surface charges. The equilibrium position indicates
the basal separation distance, while the depth of the potential well
may be interpreted as the cohesion energy per unit cell. The basal d spacing can be obtained by the term (D1 + D2)/2. The inset shows
the energy minimum as a function of surface charge.
(a) Side view of the Hec molecular model
highlighting the atomic
configuration with a layer charge of 1.0 pfu (unit cell area of 9.2
Å × 5.3 Å) achieved by the substitution of two Mg atoms
with Li atoms. (b) Energy curves for the dehydrated smectite (D1) and for the β-Ni(OH)2 island
(D2) in the interlayer space considering
the role of the surface charges. The equilibrium position indicates
the basal separation distance, while the depth of the potential well
may be interpreted as the cohesion energy per unit cell. The basal d spacing can be obtained by the term (D1 + D2)/2. The inset shows
the energy minimum as a function of surface charge.
Comparison to Other Systems
To compare our results
with similar measurements on a commercial Ni-exchanged Hec from Corning
by Cavalcanti et al.,[15] where the bulk
density (≈0.7 g/cm3) of the samples was used to
estimate the effective volume, we have to use the density acquired
from an He isotherm. The final uptake in Cavalcanti et al.[15] is readjusted to 7 wt %, by assuming that the
density is the same as that of our current Ni-Hec0.7. The
uptake behavior for this sample is in accordance with our observed
layer charge dependence, as shown in Figure , because the sample of Cavalcanti et al.[15] has a layer charge of ∼0.6 pfu on average.
Still, a direct comparison is difficult as the samples are different
in terms of origin, preparation, layer charge, and phase purity. Compared
to other clay minerals measured under similar conditions, like dried
SWy-2 and STx-1 where a maximum excess adsorption of 0.250–0.650
mmol/g under high pressure has been reported,[4,9−11] our results show a higher adsorption capacity. Compared
to the capacity of amine-modified montmorillonite (2.4 mmol/g),[45] our reported capacity is a little lower. However,
because both our current and previous[14] investigations indicate that only half of the interlayers are active
in the adsorption process, there is a potential to double the capacity
if [Ni(OH)2–(H2O)] islands can be condensed in all interlayers.
Figure 8
Comparison
of the adsorption capacity of Ni-Hec0.5 and
Ni-Hec0.7 compared with results on a Ni-Hec cation-exchanged
from a commercial Corning sample.[15]
Comparison
of the adsorption capacity of Ni-Hec0.5 and
Ni-Hec0.7 compared with results on a Ni-Hec cation-exchanged
from a commercial Corning sample.[15]
Conclusion
Our findings demonstrate
that the uptake of CO2 in the
interlayer of a clay mineral increases with a decrease in layer charge.
We suggest that this is due to more accessible space and adsorption
sites for CO2 within the interlayers. Moreover, the uptake
pressure threshold decreases with a lower layer charge, which we explain
by weaker cohesion between the layers.In future work, these
mechanisms will be examined for natural clay
minerals, such as montmorillonite. Performing the cation exchange
at a slightly increased pH (>8) is shown in the literature[46−48] to produce condensed chlorite-type interlayers only and therefore
may double the adsorption capacity for CO2. Given the compact
nature of clay minerals, this can make them volumetrically competitive
compared to MOFs and mesoporous carbon.[15] The mechanism for CO2 capture by clay minerals presented
here will also be investigated for a series of transition metals known
for their condensation tendency.The optimum layer charge for
Ni-Hec coincides with the layer charge
for natural montmorillonite, which is the main ingredient in commercial
bentonite. Therefore, the impact of our results could be important
for the implementation of clay minerals for industrial carbon capture,
separation, and sequestration processes. In addition, as clay minerals
are present in cap-rock formations for anthropogenic storage sites,
these results provide new knowledge that could be relevant for the
long-term stability of such reservoirs.
Authors: Herbert T Schaef; Narasimhan Loganathan; Geoffrey M Bowers; R James Kirkpatrick; A Ozgur Yazaydin; Sarah D Burton; David W Hoyt; K Sahan Thanthiriwatte; David A Dixon; B Peter McGrail; Kevin M Rosso; Eugene S Ilton; John S Loring Journal: ACS Appl Mater Interfaces Date: 2017-10-11 Impact factor: 9.229
Authors: Henrik Hemmen; Erlend G Rolseth; Davi M Fonseca; Elisabeth L Hansen; Jon Otto Fossum; Tomás S Plivelic Journal: Langmuir Date: 2012-01-10 Impact factor: 3.882
Authors: Matthias Stöter; Daniel A Kunz; Marko Schmidt; Dunja Hirsemann; Hussein Kalo; Bernd Putz; Jürgen Senker; Josef Breu Journal: Langmuir Date: 2013-01-16 Impact factor: 3.882
Authors: L Michels; J O Fossum; Z Rozynek; H Hemmen; K Rustenberg; P A Sobas; G N Kalantzopoulos; K D Knudsen; M Janek; T S Plivelic; G J da Silva Journal: Sci Rep Date: 2015-03-05 Impact factor: 4.379
Authors: Leide P Cavalcanti; Georgios N Kalantzopoulos; Juergen Eckert; Kenneth D Knudsen; Jon Otto Fossum Journal: Sci Rep Date: 2018-08-07 Impact factor: 4.379