Crystal Growth & Design
ARTICLE
character, the interactions with SO3ꢀ groups are favored over the
interactions with water molecules.
AEPF-4. Dehydration proceeds in one stage with a weight loss
of ∼4.0% at ∼150 °C consistent with the removal of the water
molecules present in the compound (calc. 3.8%). The second
step at ∼490 °C corresponds to the complete decomposition of
the anhydrous compound. The calculated weight loss for the
whole process (61.1%) is in good agreement with the experi-
mental value of 60.9%. PXRD pattern shows strontium sulfate
(celestine) as a main final product (PDF = 5-593).
Mg2þ ion (hexa-coordinated), which can be considered as a
hard acid ion, is normally present as a 0D hexaaquo species that
forms charge-assisted hydrogen bonds with sulfonate ligands.2ꢀ10
However, by using solvothermal conditions, we were able to
obtain the first MOF-type Mg based disulfonate, in which the
ligand directly coordinates with Mg2þ ions to build a 2D net
(AEPF-2).
AEPF-5. The complete decomposition of the compound
proceeds in one step at ∼518 °C. The calculated weight loss
for the whole process (53.7%) is in good agreement with the
experimental value of 52.9%. The PXRD pattern shows barium
sulfate (Barite) as a main final product (PDF = 24-1035).
Catalytic Activity Tests. Alkenes Hydrogenation. The
catalytic hydrogenation of unsaturated compounds represents
one of the earliest examples in heterogeneous as well as homo-
geneous catalysis.18 However, because of its high industrial
potential, this particular conversion is even currently intensively
investigated.19 Nowadays, a new class of hydrogenation catalysts
is required to develop cheap and environmentally friendly alter-
natives, because traditional hydrogenation catalysts are based on
precious metals (Pt, Pd, Rh, Ir, Re).20 In fact, non-transition
metal catalysts such as NaH, KH, MgH2, or LiAlH4 are indust-
rially used, although they need forcing conditions (150ꢀ225 °C,
60ꢀ100 bar H2) and give predominantly oligomeric or poly-
meric subproducts.21 In this way, the possibility to use alkaline-
earth elements based catalysts in hydrogenation processes has
been recently reviewed by Harder.22 Two years earlier, the good
performance of calcium and strontium homogeneous catalysts in
alkenes hydrogenation has been also shown.23
Continuing with our previous studies on the catalytic activity
of alkaline-earth MOFs, in which we showed the high catalytic
activity in hydrogenation processes under mild conditions of a
flexible calcium MOF,24,25 AEPF-2, AEPF-3, AEPF-4, and
AEPF-5 were tested as catalysts for the hydrogenation of alkenes
using styrene as substrate model under mild conditions (see
Experimental Section, Section S6). The obtained results are
summarized in Figure 8 and Table 2. The best results were
obtained with AEPF-2, for which the total and selective hydro-
genation of styrene to ethylbenzene was achieved after 4 h (TOF =
38.8 hꢀ1). It is worth highlighting that in all cases 100% selec-
tivity was achieved toward ethylbenzene, in contrast with the
behavior of previously reported calcium and strontium homo-
geneous catalysts.23
For Ca2þ (hexa-coordinated) and Sr2þ (hepta-coordinated)
ions, 3D nets with related topologies were obtained (AEPF-3
and AEPF-4 , respectively) (Figures 4 and 7). The increase in the
net dimensionality is explained on the basis of the decrease in the
charge/radius ratio. It is worth mentioning that both ions present
different coordination numbers: 6 for Ca2þ and 7 in the case of
Sr2þ, the latter additionally coordinating to one water molecule
decorating the net. Thus, in AEPF-4 the presence of coordinated
water molecules changes the bond directionalities in the inor-
ganic layer, giving rise to a new net with point symbol (43.63)2-
(46.67.82).
For Ba2þ (octa-coordinated) ion, a 3D net has been obtained
(AEPF-5) (Figures 6 and 7). The remarkable increase in the
polarizability and atomic radius for Ba2þ ion results in an increase
in its number of coordination. AEPF-5 exhibits a more compli-
cated net with point symbol (411.610)(43.63)(45.65), which
corresponds, as in the case of AEPF-4, to a new topological
type. On the other hand, the presence of a hepta,- tetra-, and
three-connected three-nodal inorganic layer in AEPF-5 forces
the aromatic rings to be much closer than in the other
compounds, giving rise to πꢀπ, and π
O stacking interac-
tions, along the (010) direction (distances of 3.15 and 3.76 Å,
respectively).
3 3 3
Infrared Spectroscopy Studies. IR spectra of AEPF-2,
AEPF-3, AEPF-4, and AEPF-5 show the presence of both υas
and υs of the SO3 groups found at 1240ꢀ1180 (υas) and
1100ꢀ1040 (υs) cmꢀ1, the aromatic CꢀH stretching mode
being situated in the area of 3100ꢀ2860 cmꢀ1 (see Support-
ing Information, Figures S9ꢀ10). For AEPF-2 and AEPF-4,
IR spectra show additional bands in the ꢀOH stretching mode
region (3750ꢀ3200 cmꢀ1), which correspond to the coordi-
nated water molecules present in these materials (see Sup-
porting Information, Figure S9).
Thermal Behavior. TGA curves for AEPF-2, AEPF-3,
AEPF-4, and AEPF-5 are shown in Supporting Information
(Figures S15ꢀS16). The exceptional thermal stability is to be
emphasized for all four MOF materials. Thus, TGA results for the
thermal decomposition for the four compounds reveal that their
frameworks are stable up to ∼500 °C in air; above this
temperature the frameworks decompose completely.
AEPF-2. Dehydration proceeds in one stage with a weight loss
of ∼8.5% at ∼180 °C consistent with the removal of the water
molecules present in the compound (calc. 8.4%). The second
step at ∼500 °C corresponds to the complete decomposition of
the anhydrous compound. The calculated weight loss for the
whole process (90.6%) is in good agreement with the experi-
mental value of 88.5%. The PXRD pattern shows magnesium
oxide as a main final product (PDF = 45-946).
AEPF-3. The complete decomposition of the compound
proceeds in one step at ∼500 °C. The calculated weight loss
for the whole process (66.5%) is in good agreement with the
experimental value of 67%. The PXRD pattern shows calcium
sulfate (anhydrite) as a main final product (PDF = 37-1496).
All catalysts employed in styrene hydrogenation were recov-
ered by centrifugation, washed with toluene, and then character-
ized by PXRD. Comparison of the PXRD patterns before and
after the catalytic reaction confirm the robustness of the four
compounds in the studied conditions (see Supporting Informa-
tion, Figures S19ꢀS22).
A mechanism for the alkaline-earth MOF-mediated hydro-
genation, based on the H2 heterolytic cleavage, could be analo-
gous to that proposed by Harder et al. for soluble calcium hydride
complexes,22,23 in which the catalytic activity is explained by the
formation of Ca-hydride intermediate species. Taking this into
account, the observed decrease in the catalytic activity in the
AEPF-2 > AEPF-3 > AEPF-4 > AEPF-5 direction can be
explained by the loss of Lewis acidity in the Mg(II) > Ca(II) >
Sr(II) > Ba(II) direction (Figure 8 and Table 2).
Recycling Experiments. Alkenes Hydrogenation. To in-
vestigate the lifetime and the stability of the better catalyst in
styrene hydrogenation (AEPF-2), a recycling experiment was
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dx.doi.org/10.1021/cg200078j |Cryst. Growth Des. 2011, 11, 1750–1758