.
Angewandte
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list of materials for experimental validation. From the
information obtained in these simulations, it was determined
that HKUST-1[12] (Figure S1) and NU-125[13] (Figure S2) were
prime candidates for further studies, based on their superior
ability to adsorb oxygen and currently known synthesis
techniques. These MOFs, along with UiO-66 (Figure S3),
a zirconium based MOF known for its exceptional stabili-
ty,[9a,14] an activated carbon (Norit SX ultra, herein referred to
as N-AC), and zeolite NaX were examined by measuring
oxygen isotherms up to 30 bar at multiple temperatures and
high-pressure oxygen isotherms up to 140 bar at room
temperature. The 30 bar metric was chosen due to safety
concerns with higher pressure oxygen at elevated temper-
atures (up to 348 K), whereas the 140 bar metric at ambient
temperature was chosen based on the standard pressure used
in medical oxygen tanks. N-AC was used as a baseline
sorbent, as previous works have shown that activated carbons
can provide high oxygen storage capacities.[7]
temperature and pressure dependence of adsorption over
wide ranges and is described in detail in the Supporting
Information.[15] At high pressures, adsorption is not likely to
form a monolayer as assumed by a Langmuir model, and the
Toth equation allows an extra empirical parameter for fitting.
This work focuses on the adsorption of oxygen at high
pressures; therefore, data were not obtained below 1 bar,
where high-energy sorbent–sorbate interactions occur. It was
observed that the isosteric heat of adsorption for N-AC
decreases as a function of increased loading at 298 K,
indicative of adsorption with a heterogeneous material. On
the other hand, HKUST-1, NU-125, and NaX each show
a relatively stable isosteric heat of adsorption with increased
loading at 298 K, indicative of adsorption dominated mainly
by geometric phenomena on a more homogeneous surface. It
is important to have a high capacity while minimizing the
strong interactions of the material with the adsorbate,
because these interactions typically dominate at pressures
below the working pressure of gas cylinders. Both HKUST-
1 and NU-125 contain coordinatively unsaturated copper
sites; however, these sites do not seem to preferentially
adsorb oxygen at the high pressures studied here. The
adsorption of oxygen was observed to be geometric in the
GCMC calculations and oxygen did not cluster at the Cu sites.
However, it has been shown that coordinatively unsaturated
metal sites can enhance the adsorption of oxygen at low
pressures.[16] Furthermore, the isosteric heat of adsorption for
HKUST-1 is higher than that for NU-125, likely due to the
smaller pore size and a higher concentration of Cu sites in
HKUST-1.
Excess oxygen isotherms for HKUST-1, NU-125, and
UiO-66 were measured for pressures up to approximately
30 bar at 298 K and are compared to N-AC and NaX in
Figure 2. At pressures less than 2 bar, the inset shows that
NU-125 and N-AC have similar O2 capacities, whereas
Based on the isotherms studied up to 30 bar, we decided
to investigate HKUST-1, NU-125, and N-AC further. These
materials were studied up to pressures of 140 bar at room
temperature and compared to NaX from Wang et al.,[8] with
the excess oxygen isotherms shown in Figure 3 and Table 1.
The isotherm for each material compares well to the
predicted outcome from the Toth model and the oxygen
isotherm predicted from the GCMC calculations (HKUST-
1 and NU-125 only; Figures S9–S12). NU-125 and HKUST-
1 have excess capacities of 98 and 75% greater than that of
the N-AC at 140 bar, respectively. Based on volumetric
Figure 2. Excess oxygen isotherms measured at 298 K up to 30 bar.
HKUST-1 has a slightly lower capacity. The isotherm for N-
AC curves downward, while the HKUST-1 and NU-125
isotherms remain much more linear. At 30 bar NU-125,
HKUST-1, and N-AC have excess O2 capacities of 8.3, 6.0,
and 5.0 molkgÀ1, respectively. In contrast, UiO-66 and NaX
have significantly lower capacities of 3.5 and 2.0 molkgÀ1,
respectively. Ideal materials exhibit oxygen isotherms char-
acterized by gradual slopes at low pressures, indicating
minimal sorbent–sorbate interactions at low pressures, and
high overall capacities at high pressures, thereby maximizing
working deliverable capacity.
Excess oxygen isotherms were measured at 298, 323, and
348 K for each MOF and N-AC (Figures S4–S7). From this
data and the oxygen isotherms of NaX reported elsewhere,[8]
the isosteric heat of adsorption of oxygen was calculated for
each material at 298 K using the Toth model (Table S1,
Figure S8). The Toth equation can be used to describe the
Figure 3. Excess oxygen adsorption isotherms measured at room
temperature up to 140 bar.
2
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Angew. Chem. Int. Ed. 2014, 53, 1 – 5
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