Fischer–Tropsch Synthesis on the Al2O3-Modified Ordered
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Transcript of Fischer–Tropsch Synthesis on the Al2O3-Modified Ordered
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7/26/2019 FischerTropsch Synthesis on the Al2O3-Modified Ordered
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Catalysis Today 265 (2016) 2735
Contents lists available at ScienceDirect
Catalysis Today
j ournal homepage : www.elsevier .com/ locate /cattod
FischerTropsch synthesis on the Al2O3-modified ordered
mesoporous Co3O4with an enhanced catalytic activity and stability
Chang-Il Ahn,Jong Wook Bae
School of Chemical Engineering, Sungkyunkwan University (SKKU), Suwon, Gyeonggi-do440-746, Republic of Korea
a r t i c l e i n f o
Article history:
Received 26 June 2015
Received in revised form 19 August 2015
Accepted 10 September 2015
Keywords:
FischerTropsch synthesis
Ordered mesoporous Co3 O4Al2O3 modification
Structural stability
Deactivation
a b s t r a c t
Ordered mesoporous Co3O4 metal oxide synthesized by nano-casting method using a hard template of
KIT-6 was subsequently modified with Al component to increase catalytic activity and structural sta-
bilities even under H2-rich FischerTropsch synthesis (FTS) conditions. While using a highly ordered
mesoporous Co3O4 for FTS reaction, a significant structural change by forming larger cobalt aggregates
and encapsulated cokes accelerated a catalyst deactivation. By introducing an irreducible Al species on
the inner surfaces or in the main frameworks ofmesoporous Co3O4, the ordered mesoporous structures
ofCo3O4 were successfully maintained even after FTS reaction. These modifications ofthe mesoporous
Co3O4 structures were carried out by adding a pillaring material of aluminum oxide or by preparing
mesoporous mixed binary metal oxides with the partial formation of a spinel CoAl2O4 phase, and a
higher structural stability and activity were observed due to the suppressed collapses ofthe mesopore
structures of Co3O4 . The improved stability of the Co3O4 mesopores seems to be related with a lower
mobility ofan irreducible Al2O3pillar by strongly interacting with the inner surfaces ofthe mesoporous
Co3O4or by enhancing the interactions ofCo3O4with Al2O3in a main framework ofmixed binary metal
oxides. 2015 Elsevier B.V. All rights reserved.
1. Introduction
FischerTropsch synthesis (FTS) reaction has been well known
to be an efficient chemical conversion process using the synthe-
sis gases, which can be synthesized from the reforming of natural
gas or coal (or biomass) gasification, to produce some clean fuels
or petrochemicals [13]. The cobalt-based FTS catalysts have the
advantages such as a higheryieldfor linearhydrocarbons at a lower
operating temperature with a suppressed water gas shift activity
compared to the iron-based FTS catalysts [4]. The supported FTS
catalysts can be prepared by supporting cobalt nanoparticles on
the highly porous irreducible metal oxides with a high dispersion
of them, however, significant aggregations of the cobalt nanopar-
ticles with the reoxidation to form an inactive cobalt species and
the possible deposition of heavy waxes (or coke precursors) during
the FTS reaction haven been known for the main reasons for cat-
alyst deactivations [4]. To overcome these general disadvantages
of supported catalysts, ordered mesoporous supports such as the
ordered mesoporous silica, carbons or transition metal oxides have
been widely investigated in the field of heterogeneous catalysis due
Corresponding author.
E-mail address: [email protected] (J.W. Bae).
to their well-developed regular mesopore structures with a higher
surface area [2,3] through well-known nano-casting methods for
some applications of battery technologies and oxidation catalytic
reactions and so on [5,6]. However, the direct applications of the
transition metal oxides for some catalytic reactions have been lim-
ited dueto their structureinstabilityunder H2-richconditions [7,8].
Thephasetransformationfrom metal oxidesto metallic species can
cause a severeaggregationand a structural collapse of thereducible
mesoporous transition metal oxide frameworks resulted in accel-
erating catalyst deactivation. As far as we know, these deactivation
mechanisms may be main reasons for the small research reports
concerning practical applications of mesoporous transition metal
oxides for the FTS reaction till now.
In the present study, we investigated two possible methodolo-
gies to suppress the structural collapses of the mesoporous Co3O4even under the reductive CO hydrogenation conditions by intro-
ducing an irreducible aluminum oxide in the mesoporous surfaces
[10] or by preparing mixed binary metal oxides of CoAlOx in the
main frameworks of Co3O4 to elucidate the roles of aluminum
oxide on the surfaces or mainframes of mesoporous Co3O4. These
modifications of the mesoporous Co3O4 with irreducible Al2O3species showed a stable activity by maintaining regular meso-
porous structures during the FTS reaction. The improved catalytic
activity and structural stability of the mesoporous Co3O4 were
http://dx.doi.org/10.1016/j.cattod.2015.09.047
0920-5861/ 2015 Elsevier B.V. All rights reserved.
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calculated to compare the surface composition changes before and
after FTS reaction. Transmission electron microscopy (TEM) anal-
ysis was also carried out to verify the changes of the local surface
morphologies on the fresh and used mesoporous Co3O4 catalysts
using TECNAI G2 operated at an accelerating voltage of 200 kV.
Catalytic activity test of the as-prepared mesoporous Co3O4catalysts were carried out in a stainless steel fixed-bed tubular
reactor having an outer diameter of 12.7 m m using 100 m g of
the catalyst after mixing with 1.0 g of gamma-Al2
O3
as a diluent
with the a granule size of 60100m. Prior to the FTS reac-
tion, the mesoporous Co3O4 catalysts were reduced in situ at
400 C under a flow of 5%H2 balanced with N2 for 12 h. After
the reduction, the reactor temperature was cooled down to room
temperature and the reactant of syngas having a feed gas com-
position of H2/N2/CO = 62.84/5.60/31.56 was introduced. The FTS
reaction was performed for around 2060h under the following
reaction conditions; T= 2 30 and 240 C, P=2.0MPa, and weight
hourly space velocity (WHSV)= 24000 L (mixed gas)/(kgcat h). The
effluent productsfrom thereactorwereanalyzedby using an online
gas chromatograph (YoungLin Acme 6500, GC) equipped with GS-
GASPRO capillary column connected to flame ionization detector
(FID) for the analysis of hydrocarbons, and Carboxen 1000 packed
columnconnectedto TCDfor theanalysis ofCO, CO2, CH4 andH2. CO
conversion was calculated using the variations of CO moles before
and after FTS reaction corrected by using the area changes of inter-
nalstandardgas andthe product distributions were also calculated
based on the total carbon balances. In addition, the reaction rate
wasdefinedas thereactedCOmol/(gcat s)andtheTOFwasdefined
as the reacted CO molecules/(surface cobaltatoms), where the rate
and TOF were calculated using the results of FTS reaction at around
20h on stream.
3. Results and discussion
3.1. Physicochemical properties of the Al-modified mesoporous
Co3O4
The surface area, pore volume and average pore diameter of the
mesoporousCo3O4catalystswith theirpore size distributions were
measured by N2sorption method, and the results are summarized
in Table 1 and Fig. 1. As shown in Fig. 1, the presence of the meso-
pore structures was clearly observed with a type IV isotherm and
H1 hysteresis on the mesoporous Co3O4 catalysts. In addition, the
hysteresis pattern on the comparative bulk-Co3O4suggests a typi-
cal non-porous material structure. The sharp peak intensities with
a pore size around 4 nm were observed on the Al-modified meso-
porous Co3O4 catalysts such as the meso-Co3O4, Al/meso-Co3O4,
and Al/meso-CoAlOx, however the bulk-Co3O4 showeda broadpore
size distribution between 10 and 100nm in pore size as shown
in an inset of Fig. 1. The broad pore size distribution on the bulk-
Co3O4 seems to be attributed to the inter-particular pores of Co3O4nanoparticles byshowing a lower surface area of 32m2/g andlarger
pore diameter of 20.3nm. The surface areas of the mesoporous
Co3O4 catalysts were significantly decreased after Al modification
from 104m2/g on the meso-Co3O4 by showing a bimodal pore
size distribution to 98m2/g on the Al/meso-Co3O4and 47m2/g on
the Al/meso-CoAl0.25Ox by showing an unimodal size distribution
with a sharp peak intensity at around 4nm in size. The observa-
tion strongly suggests that Al2O3pillar was highlydispersed on the
inner surfaces of the meso-Co3O4 and the meso-CoAlOx without
significant aggregation of Al2O3 pillar or a possible structural col-
lapse during the preparation steps [8,10,11]. The pore volume and
average pore diameter were also observed with a similar trend by
showing the respective values of 0.070.19 cm3/g and 4.76.1 nm
except for the bulk-Co3O4 as summarized in Table 1. The slightly
Fig. 1. N2
adsorptiondesorption patterns and pore size distributions of the fresh
mesoporous Co3O4catalysts.
increased average pore diameter of 6.1 nm on the Al/meos-Co3O4from that of 5.0 nm on the meos-Co3O4can be possibly attributed
to the formation of inter-particular pores originated from the par-
tially collapsed Co3O4 and Al2O3 pillar at around 50nm (an inset
of Fig. 1). Interestingly, the ordered mesoporous structures were
well developedon the Al/meso-CoAl0.25Ox and Al/meso-CoAl0.13Ox,
which seems to have a positive effect for a superior catalytic activ-
ity and stability through a facile transport of heavy hydrocarbons
formed during FTS reaction [10].
Wide angel powder XRD patterns of the fresh mesoporous
Co3O4catalysts are displayed in Fig. 2(A), and the calculated aver-
age particle sizes of Co3O4 were also summarized in Table 1. Thespinel structures of Co3O4crystalline phases were clearly observed
atthe2valuesof 19.0,31.2, 38.5,44.8,59.3and 65.2,whichcanbe
corresponding to the characteristic crystalline Co3O4 diffractions
of (1 1 1), (2 2 0), (3 1 1), (4 0 0), (5 1 1) and (4 4 0) planes [12]. The
particle sizes of Co3O4were further calculated by DebyeScherrer
equation using the most intense characteristic diffraction peak at
2=36.8. The particle sizes of the mesoporous Co3O4 catalysts
even after Al modification were found to be around 15.916.9 nm,
which could be a grain size of main framework of cobalt oxides,
except for the bulk-Co3O4with a particle size of 27.9nm. The par-
ticle sizes of metallic cobalt were calculated by using the equation
of d(Co0)=0.75d(Co3O4) [13], and the calculated particle sizes of
metallic cobaltwerefoundto beabove12 nmon allthe mesoporous
Co3O4 catalysts, which has been generally known to be a trivialeffect to the intrinsic activity for the FTS reaction due to its charac-
ter of structure insensitivity above 8 nm in size [4]. Therefore, the
different intrinsic catalytic activity of the turnover frequency (TOF)
on the mesoporous Co3O4catalysts seems to be mainly attributed
to the other characteristics such as the mesoporosity with its sta-
bility and the mass transport of products of heavy hydrocarbons
and so on. Even though the spinel structure of the cobalt aluminate
of CoAl2O4was not clearly observed by the XRD analysis due to an
identical diffraction peak position with Co3O4 [14,15], a possible
formation of cobalt aluminate on the Al/meso-Co3O4, Al/meso-
CoAl0.25Ox and Al/meso-CoAl0.13Ox seems to be a main reason for
an enhanced structural stability and activity by forming a particle
size of around 16nm, which corresponds to a main frameworks
granule size of Co3O4. As shown in Fig. 2(B), the characteristic 2D
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Table 1
Characteristics of the Al-modified ordered mesoporous Co3 O4catalysts.
Catalysts BET XRD H2-Chem. TPR XPS
Surface
area
(m2/g)
Pore
volume
(cm3 /g)
Pore
diameter
(nm)
Particle
size of
Co3O4 (nm)
Surface area
of cobalt
(m2/gCo)
Degree of
reduction
(%)a
BE (eV)of
Co2p3/2
BE(eV) ofAl2p IAl /ICob (103)
Fresh/used Fresh/used Fresh/used
Bulk-Co3O4c 32 0.22 20.3 27.9 12.1 98.2
Meso-Co3O4c 104 0.19 5.0 15.5 22.8 62.9 780.2/780.0 / /
Al/meso-Co3O4c 98 0.21 6.1 16.9 31.0 44.0 780.5/780.3 75.8/75.0 1.28/1.14
Al/meso-CoAl 0.13 Ox 68 0.10 4.7 15.9 8.4 50.4 781.0/780.9 74.4/74.2 2.12/2.15
Al/meso-CoAl 0.25 Ox 47 0.07 5.5 16.4 10.9 50.3 778.8/778.7 74.2/73.8 4.36/4.31
a The degrees of reduction of catalysts were calculated using TPR data with an amount of H2 consumption below 450C divide d by t ot al H2 consumption in the full
temperature ranges.b Thevalues of theintensity ratio ofIAl /ICo were calculated using theintegrated area of each peak by correcting thearea usingthe atomicsensitivityfactors (ASF) with the
values ofSCo=4.5 and SAl= 0.11.c The characterization results of the bulk-Co3O4 , meso-Co3O4 and Al/meso-Co3O4was partly reported in ourpreviousworks [8,10].
Fig. 2. (A)Wide-angle XRD patterns and (B)small angle X-ray scattering (SAXS)patternsof the fresh mesoporous Co3O4 catalysts.
hexagonal ordered mesostructures assigned to planes of (10 0),
(11 0), and (20 0) reflections [16,17] were clearly observed on the
ordered mesoporous Co3O4 before and after Al modification. The
peak intensity of (10 0) plane was observed much larger on the Al-
incorporated meso-Co3O4such as on the Al/meso-CoAl0.25Ox, and
it suggests the facile formation of well-ordered mesoporous struc-
tures on the mesoporous mixed oxides which is in line with the
results of N2sorption analysis.
3.2. Reducibility and structural stability of the Al-modified
mesoporous Co3O4
The reduction patterns of Co3O4 crystallites are known to fol-
low two-step reductions such as Co3O4CoOCo0. From TPR
analysis of the mesoporous Co3O4catalysts as shown in Fig. 3, the
stepwise reductions with two distinctive reduction peaks can be
assigned as the first reduction of Co3O4 to CoO at around 300C
and the second reduction of CoO to metallic cobalt above 400 C
[18,19]. In the case of the unmodified Co3O4, two H2 absorption
peaks of Co3O4were clearly observed at much lower temperatures
of 303 and 374 C on the bulk-Co3O4, and at the temperatures of
280 C and 493 C on the meso-Co3O4, which are also responsi-
ble for the typical two step reductions of Co3O4. Interestingly, a
higherreduction temperature shift of thesecond peak on themeso-
Co3O4 can be possibly attributed to the suppressed H2 transport Fig. 3. TPR profiles of thefresh mesoporous Co3O4 catalysts.
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Fig. 4. TEM imagesof thefresh(A) bulk-Co3O4 , (B)meso-Co3O4 , (C) Al/meso-Co3O4 , (D) Al/meso-CoAl0.25 Ox catalysts.
rate by the trapped water generated during the reduction step in
the mesopores of the meso-Co3O4[2,8,20]. On the Al/meso-Co3O4,
two characteristic reduction peaksappearedat 371and 446Cwith
a medium reduction temperature of 402 C, which are also in line
with the typical stepwise reduction steps of Co3O4, and a shoulder
peak at 402 C may be originated from the aggregated cobalt parti-
cles during the synthesis steps through partial structural collapses
[8,10]. The shifts of reduction peaks to higher temperatures on the
Al/meso-Co3O4 compared to the meso-Co3O4 were attributed to
the dispersed Al2O3 pillar on the inner framework surfaces of the
mesoporous Co3O4 by forming a strong metal-support interaction.In addition,a reductionpeak at 724C on theAl/meso-Co3O4seems
to be originatedfrom a possibleformation of spinel structuralcobalt
aluminate [4]. Generally, it has been known that irreducible metal
oxides such as Al2O3, SiO2 and TiO2 can lead to the formation of
strong metal-support interactions on the supportedmetal catalysts
[4,21]. Even though these phenomena can show negative effects
in terms of catalytic activity due to the difficult reduction behav-
ior of the strongly interacted cobalt particles on the supports, the
enhanced structural stability can be originated from a strongly
interacted Al2O3 pillar on the meso-Co3O4and meso-CoAlOxeven
under H2-rich reaction conditions.
The reduction patterns on the Al2O3 incorporated Al/meso-
CoAlOx were similar with the Al/meso-Co3O4 by shifting to lower
temperatures, especially on the Al/meso-CoAl0.25Ox. The two stepreductions of Co3O4 particles were observed at around 330 and
490 C, and the medium temperature of 383C on the Al/meso-
CoAl0.13Ox seems to be originated from the aggregated cobalt
particles through a partial structural collapses [8,10]. Interest-
ingly, the higher temperature reduction peaks at a respective
654 and 611 C on the Al/meso-CoAl0.13Oxand Al/meso-CoAl0.25Oxcan generate a strong interaction between Co3O4 and impreg-
nated (or incorporated) Al2O3 species. This can be beneficial for
an enhanced structural stabilityof the mesoporous Co3O4catalysts
by forming spinel CoAl2O4phases possibly. The reduction degrees
ofCo3O4 particleswere foundto be lower on theAl-modifiedmeso-
porous Co3O4catalysts with the values of 44.0, 50.4, and 50.3% on
the respective Al/meso-Co3O4, Al/meso-CoAl0.13Ox and Al/meso-
CoAl0.25
Ox
compared to the meso-Co3
O4
with a value of 62.9%,
which strongly suggests the formation of new strong interactions
between Co3O4andAl2O3particles.In addition,the observed lower
reduction temperatures on the Al/meso-CoAl0.25Oxthan thatof the
Al/meso-CoAl0.13Ox seemsto be attributed to smaller total amounts
of Al2O3content n in the mesoporous Co3O4main frameworks.
To further verify the structural stability after Al modification on
the mesoporous Co3O4catalysts, TEM analyses were carried outon
the as-prepared catalysts as shown in Fig. 4 with magnified inset
figures. The bulk-Co3O4 showed the bundles of spheres with the
particle sizes of 2030 nm, and the ordered mesopore structures
on the meso-Co3O4 were clearly observed with an average porediameter around 5 nm. In addition, the observed different parti-
cle sizes of Co3O4 on the Al-modified meso-Co3O4 between XRD
and TEM analysis seems to be mainly attributed to a formation
of larger cobalt clusters in the frameworks of mesoporous Co3O4which could be the aggregates of the separate Co3O4grains mainly
measured by XRD analysis.The regularity of the mesoporous struc-
tures on the meso-Co3O4seems to be responsible for the observed
higher specific surface area of metallic cobalt compared to that of
the bulk-Co3O4. In addition, the typical ordered mesoporous struc-
tures with a pore diameter of 68 nm were clearly observed on the
Al/meso-Co3O4 which was also sustainedeven after the addition of
Al2O3 pillaring material. This observation suggests that the Al2O3pillar is well dispersed inside the mesopores of the meso-Co3O4. It
also suggests that Al2O3 particles can be strongly interacted withthe mesoporous Co3O4 surfaces by forming a strong metal-support
interaction (confirmedby TPR), which canplay an importantrole in
stabilizing the mesopore structures of Co3O4 under the reductive
FTS conditions. In addition, TEM images of the fresh Al/meso-
CoAl0.25Ox also support that the mesoporous frameworks of Co-Al
mixed oxides originated from vacant pores of the KIT-6 mesopores
are well developed with similar pore sizes of the Al/meso-Co3O4.
H2 chemisorption analysis was carried out on the mesoporous
Co3O4 catalysts to verify the active metallic surface area of cobalt
species, andthe results aresummarized in Table1. The larger metal-
lic cobalt surface areas of 22.8 and 31.0m2/gCo were observed on
the meso-Co3O4 and the Al/meso-Co3O4, respectively, compared
to that of bulk-Co3O4 with a value of 12.1m2/gCo. However, with
an incorporation of Al2
O3
particles on the Al/meso-CoAl0.13
Ox
and
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32 C.-I. Ahn, J.W. Bae / Catalysis Today 265 (2016) 2735
Fig. 5. Catalytic activities on the mesoporous Co3O4 catalysts with time on stream
(h).
Al/meso-CoAl0.25Oxmixed oxides, the metallic cobalt surface areas
were decreased to 8.4 and 10.9m2/gCo due to a smaller content
of cobalt species. In addition, from our previous study [10], thedecreased metallic surface area after the reduction treatment was
mainly attributed to the partial structure collapses of the meso-
Co3O4. Although the Al2O3 modified meso-Co3O4 has a smaller
metallic surface area than that of the meso-Co3O4 due to the
well-developed mesoporous structures, the structural collapse of
the ordered mesoporous structures without Al modification can
increase the structural instability during the reductionstep through
a intrinsicvolume contraction from Co3O4to metallic cobalt, which
resulted in showing a lower catalytic activity and stability. The
observed higher metallic cobalt surface area of the Al-modified
meso-Co3O4 suggests that the ordered mesoporous structures are
well preservedthrougha higherdispersionof theAl2O3 pillar inside
the pores of the meso-Co3O4 and meso-CoAlOx. Generally, it has
been also known that the irreducible metal oxide having a lowermelting point and smaller particle size can have a higher mobility
onthe surfacesat a much lowermeting temperature ofmetaloxides
during thermal treatment [21,22]. Based on the above phenomena,
a pillaring oxide of Al2O3 can be evenly dispersed on the inside
of the meso-Co3O4 or meso-CoAlOx surfaces which are verified
by the variations of specific surface areas after the Al impregna-
tion. The higher metallic cobalt surface area of the Al/meso-Co3O4suggests theformation of thestrongerinteractionbetween thesur-
faces of mesoporous Co3O4 with thermally stable Al2O3 particles
under a higher temperature reductive condition. In addition, with
the increase of the amount of Al2O3 in the main frameworks of
the meso-CoAlOx, the amount of active metallic cobalt sites can be
diminished by showing a lower metallic cobaltsurface area around
8.410.9m
2
/gCocompared to the Al/meso-Co3O4.
3.3. Activity and stability of the Al modified meso-Co3O4under
reductive conditions
The catalytic activities on the mesoporous Co3O4catalysts were
carried out at T=230 and 240 C, P=2.0MPa, and WHSV= 24000L
(mixed gas)/(kgcat h). As shown in Fig. 5 with the summarized
results in Table 2, the superior catalytic activity at 230 C was
observedonthemeso-Co3O4 compared to the bulk-Co3O4 by show-
ing CO conversions of 6.1 and 11.7% with a similar trend of reaction
rates at steady-state, which can be induced from regular meso-
porous structures and suppressed paraffin wax deposition on the
activecobalt sites resulted in theenhancementof mass transportof
the heavier hydrocarbons formed as reported in our previous work
[8]. The TOFs (defined as number of reacted CO molecules/(surface
cobalt atom s )) were found to be similar values of 0.055 and
0.035 s1 on the bulk-Co3O4 and the meso-Co3O4 because of the
structure insensitive characters of the cobalt nanoparticles above
8nm in size [4,23,24]. A higher CH4 and a lower C5+ selectivity on
the meso-Co3O4 (i.e., 6.9% for CH4 and 81.8% for C5+) compared
to those on the bulk-Co3O4 (i.e., 3.1% for CH4 a nd 94.0% for C5+)
were attributed to the presence of the partially reduced cobalt
particles with a higher mesoporosity on the meso-Co3
O4
d ue to
a lower intrinsic activity for the secondary reactions of light olefins
to the heavy hydrocarbons [4,23,2527]. Based on our previous
work [20], the catalyst deactivation was mainly originated form
the structural collapses of the meso-Co3O4and the wax encapsula-
tion and filamentous carbon formation on the bulk-Co3O4surfaces
verified by thecharacterizationsof FT-IR,Raman andTEM analyses.
In addition, the possible catalyst deactivation by the deposition of
heavy wax components in the mesopores of meso-Co3O4 cannot
be overlooked [4], however, a collapse of regular mesopore struc-
tures seems to be more dominant deactivation mechanism of the
meso-Co3O4.
As shown in Fig. 6(A) and (B), the particle sizes of cobalt after
the FTS reaction were increased up to 50100 nm on the used
meso-Co3O4 with the complete structural collapse of mesoporous
Co3O4, and the particle size of cobalt on the used bulk-Co3O4was more significantly increased from 30nm to above 100nm
[8,10]. The morphologies of deposited carbons were significantly
different by showing an encapsulation of the aggregated cobalt
particles with amorphous carbons on the bulk-Co3O4 which can
disrupt the transport of reactants to the active cobalt sites, and a
growth of filamentous whisker carbons on the meso-Co3O4which
is likely to form on the surfaces of metallic crystallites having a
weak metal-support interaction with a small cobalt particle size
[28,29].
To stabilize the ordered mesoporous Co3O4 structures with
lower carbon depositions, the modification with irreducible metal
oxide of Al2O3 was further applied to the meso-Co3O4 by pillar-
ing Al2O3 into the mesopores or by preparing mixed-metal oxide
frameworks such as CoAlOx. As shown in Fig. 5 and summarizedin Table 2, a significant increase of activity and stability on the
Al/meso-Co3O4 was observed at T=230C with CO conversion
above 83%during 40h on streamwithouta significant deactivation.
The reaction rate and TOF were also dramatically increased on the
Al/meso-Co3O4 with values of 82.8 [reacted COmol/(gcat s)] and
0.153 [reacted CO molecules/(surface cobalt atom s)] compared to
the unmodified meso-Co3O4. A slight increase of CH4selectivity of
11.6%and decrease ofC5+ selectivity of 77.3% on the Al/meso-Co3O4can be attributed to the formation of the strongly interacted Al2O3pillaringoxide withthe surfaces of meso-Co3O4 whichalso resulted
in forming a largely oxidized electronic states of cobalt particles
by decreasing the adsorption properties of H2 and increasing CH4selectivity possibly due to a known relatively fast formation rate of
light hydrocarbons [4,10,3032]. However, the strong interactionsbetween the metallic cobalt surfaces of the meso-Co3O4 frame-
works and the Al2O3 pillar can stabilize the mesopore structures
even under FTS reaction condition by maintaining stable catalytic
activity. As shown in Fig. 6(C) with the magnified inset TEM image,
the ordered mesoporous structures with a pore size of around6 nm
on the used Al/meso-Co3O4 were well maintained after the FTS
reaction for 40h with local aggregations of the mesoporous Co3O4and without filamentous carbon formations. The structural stability
on the Al/meso-Co3O4 was improved because of an even distri-
bution of the thermal stable Al2O3 pillar inside the meso-Co3O4pores, which resulted in showing a higher catalytic activity and
stability. Since the collapses of the mesopore structures of the
Al/meso-Co3O4 were also insignificant under H2 reduction pre-
treatment as confirmed by our previous study through N2sorption
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Table 2
Catalytic performances on the Al-modified ordered mesoporous Co3O4 catalysts.
Catalysts Reaction Temp. (C) Reaction duration (h) Activitya Product distribution (C-mol%)
CO conv. (C-mol%) Rateb TOFb C1/C2C4/C5+ Olefins in C2C4(%)
Bulk-Co3O4 230 20 6.1 5.8 0.055 3.1/2.9/94.0 43.4
Meso-Co3O4 230 20 11.7 10.9 0.035 6.9/11.3/81.8 61.1
Al/meso-
Co3O4c 230
20 88.2 82.8 0.153 11.6/11.1/77.3 11.6
40 83.6 9.7/11.9/78.4 16.5
Al/meso-
CoAl0.13 Ox 240 20 93.9 88.2 0.406 8.3/6.1/85.6 7.5
60 91.3 6.4/5.4/88.2 16.5
Al/meso-
CoAl0.25 Ox240
20 95.8 90.0 0.234 13.4/7.5/79.1 4.2
60 85.9 12.1/8.8/79.1 25.2
a The FTS reaction was car ried out at t he f ollo wing con ditions ; T= 230 and 240 C, P=2.0MPa, WHSV=24000L/(kgcath), and a feed gas composition of
H2/N2/CO= 62.84/5.60/31.56.b Thereactionrate was definedas thereacted COmol/(gcats) andthe TOFwas definedas thereacted CO molecules/(surface cobalt atom s),where therate andTOF were
calculated using thereactiondate at around20 h on stream.c The results of theAl/meso-Co3O4 was reported in our previous work [10].
and TEM analysis [10], the highlyorderedmesoporous structuresof
the Al/meso-Co3O4seems to be maintained through the formation
of thestrong interaction between thereducible cobaltparticles and
the irreducible Al2O3pillaring metal oxide.
To further improve a structural stability of mesoporous metal
oxide catalysts, the Al2
O3
incorporated mixed metal oxides of
the Al/meso-CoAl0.13Ox and Al/meso-CoAl0.25Ox were prepared
by nano-casting method and the representative catalytic activi-
ties are summarized in Table 2 with the activity with time on
stream at T=240 C in Fig. 5. A higher catalytic activity and sta-
bility without significant deactivation (i.e., CO conversion of 93.9%
at 20 h and 91.3% after 60 h on stream) were observed on the
Al/meso-CoAl0.13Ox, and the activity was slightly decreased with
an increase of Al2O3 content in the mixed metal oxide structures
such as the Al/meso-CoAl0.25 Ox (i.e., Co conversion of 95.8% at
20h and 85.9% after 60h on stream). The reaction rates and TOFs
were also found to be higher on the Al/meso-CoAl0.13Ox with the
values of 88.2 [reacted CO mol/(gcat s)] and 0.406 [reacted CO
molecules/(surface cobalt atoms)] with a lower CH4 selectivity
of 8.3% and a higher C5+ selectivity of 85.6% than those on the
Al/meso-CoAl0.25Ox. Thesehigher catalyticactivityand stabilitycanbe mainly attributed to the stable maintenance of the mesoporous
frameworks by using Al2O3modifier through the formation of the
strongly interacted Al2O3 and a possible formation of the inac-
tive CoAl2O4 species on the Al/meso-Co3O4 and Al/meso-CoAlOx.
As shown in Fig. 6(D) with the magnified inset TEM image, there
were no large differences in the ordered mesoporous structures
between the fresh and used Al/meso-CoAl0.25Ox, which strongly
suggests thatthe structural collapse can be successfullysuppressed
by using the Al2O3 modifier to the mesoporous Co3O4 struc-
tures through pillaring method of irreducible Al2O3 or preparing
mixed metal oxide structures of meso-CoAlOx. In addition, the
increased C5+ selectivity with an increase of reaction time on all
the Al-modified mesoporous Co3O4can be attributed to thesurface
changes through the reconstruction andaggregation of cobalt parti-
cles or thecarbon depositions andso on [4,18,25,32]. The decreased
olefin selectivity on the Al-modified meso-Co3O4 compared to the
meso-Co3O4 seems to be attributed to the higher oxidation states
of cobalt particles or the increased surface acidity [4,16] dueto the
formation of the strong new interactions of Al2O3species with the
outer surfaces or the frameworks of the mesoporous Co3O4. It was
also supported from the measured isoparaffin percentage based
on the total paraffin in the range of C2C4 hydrocarbons with the
values of 3.73, 3.59, 2.29, 1.97 and 0% on the Al/meso-CoAl0.25Ox,Al/meso-CoAl0.13Ox, Al/meso-Co3O4, meso-Co3O4and bulk-Co3O4,
respectively.
Fig. 6. TEM imagesof theused (A)bulk-Co3O4 , (B)meso-Co3O4 , (C) Al/meso-Co3O4 , (D) Al/meso-CoAl0.25 Oxcatalysts.
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34 C.-I. Ahn, J.W. Bae / Catalysis Today 265 (2016) 2735
Fig. 7. XPS spectra ofCo2pon the mesoporous(A) fresh and (B) usedCo3O4 catalysts.
To further verify the possible reasons for the enhanced struc-
tural stability after the Al2O3 modification on the mesoporous
Co3O4, XPS analysis was also carried out on the fresh and used
FTS catalysts and the results are summarized Table 1 with the
XPS peaks of Co2p in Fig. 7. The values of BEs on the fresh meso-
porous Co3O4 were found to be in the ranges of 778.8781.0eV
and 778.7780.9eV on the used mesoporous Co3O4. In general,
the core level BEs of Co2p3/2 on the supported Co3O4 catalysts
have been reported to slightly increase compared to those of pure
Co3O4 nanoparticles due to the strong metal-support interaction
due to different surface properties of the supports such as acid-
ity or hydrophilicity and so on [33,34]. Therefore, the observed
slight increases of BEs after Al2O3modification on the mesoporousCo3O4 compared to the pure meso-Co3O4 may suggest the forma-
tion a new strong interactions between the Al2O3 pillar (or the
mixed metal oxides of CoAlOx) and the mesoporous Co3O4 sur-
faces. Due to the possible superposition of Co2p3/2 peak assigned
to the cobalt oxides with various oxidation states such as Co3O4,
CoO and CoAl2O4with the reference metallic cobalt BE of 780.0 eV
[35,36], the formation of spinel cobalt aluminate species cannot be
overlooked dueto a observed newreductionpeak ata higherreduc-
tion temperature above 600 C from TPR results after the Al2O3modification on the meso-Co3O4. In addition, a main aluminum
phase seems to be the stable gamma-Al2O3from the observed BEs
of Al at around 75 eV on the fresh and used mesoporous Co3O4catalysts without significant variations. The modification with a
thermally stable Al2O3 on the Al/meso-Co3O4 and Al/CoAlOx maybe related with an enhanced stability of mesopore structures by
partially forming CoAl2O4 spinel structures in the interfaces of
Al2O3and Co3O4particles possibly. This hypothesis was supported
by comparing the intensity ratio of Co2p3/2peak with that of Al2p
peak on the fresh and used catalysts as summarized in Table 1.
The calculated values of IAl/ICo were found to be 1.28, 2.12 and
4.36 on thefreshAl/meso-Co3O4, Al/meso-CoAl0.13Ox and Al/meso-
CoAl0.25Oxrespectively, and the observed higher ratios ofIAl/ICoon
the fresh Al/meso-CoAlOx were attributed to a higher content of
Al2O3 species. In addition,a smallshoulderpeak intensityat around
785.0 eV on the fresh Al/meso-CoAlOx and Al/meso-Co3O4 can be
assigned to a shake-up process of a high spin Co2+ species, which
can be correlated with the formation of non-reducible inactive
cobalt aluminate species as well [37]. Therefore, the XPS spectra
of the Al2O3-modified mesoporous Co3O4 catalysts after FTS reac-
tion further revealedthatthe shake-up processof thehighspin Co2+
increased due to the additionally generated spinelcobalt aluminate
species during FTS reaction possibly, which can be mainly respon-
sible for the structural stability with a lower deactivation rate on
the Al/meso-Co3O4 and Al/meso-CoAlOx. Interestingly, the calcu-
lated values ofIAl/ICo were found to be 1.14, 2.15 and 4.31 on the
used Al/meso-Co3O4, Al/meso-CoAl0.13Oxand Al/meso-CoAl0.25 Ox,
respectively without significant variations compared to those of
the fresh catalysts. These observations also support that the Al2O3species as a pillaring material or as a mixed metal oxide forma-
tion seems to be thermally stable even under the FTS reaction by
not being segregated and by forming strong interactions with themesoporous Co3O4 surfaces and the framework structures of the
Al/meso-Co3O4and Al/meso-CoAlOxsufficiently.
In summary, the irreducible Al2O3 modification of the meso-
porous Co3O4 catalysts through the pillaring method or the
formation of mixed metal oxide of mesoporous CoAlOx can suc-
cessfully enhance the catalytic activity and stabilityby maintaining
stable ordered mesopore structures even under the reductive FTS
reaction conditions at a higher space velocity with a simultaneous
suppression of coke or wax deposition on the active cobalt metal
surfaces. The newlyformed strong interactions between Co3O4and
Al2O3particles by partially forming spinel structure of the inactive
CoAl2O4 species were the main reasons for the enhanced struc-
turalstability of the mesoporesof Al-modified Co3O4. Theimproved
structural stability of mesoporous Co3O4 was attributed to thelower mobility and thermal stability of the irreducible Al2O3 pil-
lar by strongly interacting with the inner surfaces of the ordered
mesoporous Co3O4 which were well verified by the surface char-
acterizations such as TEM, XPS and TPR analysis.
4. Conclusions
The FTS activity of the mesoporous Co3O4synthesized through
a well-known nano-casting methodusing the mesoporous KIT-6 as
a hard template was investigated. The mesoporous structures and
the enhanced structural stability of the mesopores after the mod-
ification with an irreducible and thermally stable metal oxide of
Al2O3showed an enhanced catalytic activity with less coke or wax
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C.-I. Ahn, J.W. Bae / Catalysis Today 265 (2016) 2735 35
deposition on the active sites. These improved activity and struc-
tural stability were mainly attributed to a lower mobility of the
Al2O3modifier by strongly interacting with cobalt particles on the
surfaces of themesoporous Co3O4or in themain frameworks of the
mixed metal oxide of CoAlOx. The formation of an inactive CoAl2O4spinel structure on the Al/meso-Co3O4and Al/meso-CoAlOxseems
to be responsible for maintaining the stable ordered mesoporous
structures even under the reductive FTS reaction conditions. The
irreducible Al2
O3
modification of the mesoporous structures of
Co3O4by pillaringAl2O3on thesurfacesof activecobalt particlesor
byforming mixed metal oxide of mesoporous CoAlOx canbe further
applied forthe FTS reaction working at a higher space velocity with
a lower coke or wax deposition on the active cobalt metal surfaces
due to its ordered mesoporosity and structural stability.
Acknowledgments
This work was also supported by the R&D Center for Valuable
Recycling (Global-Top R&D Program) of the Ministry of Environ-
ment with a project number of GT-14-C-01-038-0. The authors
acknowledge the financial support from the National Research
Foundation of Korea (NRF) grant funded by the Korea government
(NRF-2014R1A1A2A16055557). This work was supported by the
NationalResearchCouncil of Science and Technology(NST) through
Degree and Research Center (DRC) Program (2014). This work was
also supported by the Korea Institute of Energy Technology Evalu-
ation and Planning (KETEP) under Energy Efficiency and Resources
Programs with Project numbers of 20142010102790.
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