Angewandte Chemie International Edition
10.1002/anie.201810945
COMMUNICATION
phenoxide was obtained finally (Figure S10). Therefore, the
metallation strategy proposed here successfully decreased the
relatively low temperature (refluxing of solvents such as toluene,
[
21]
xylene or 2,2,2-trifluoroethanol) , only the N-containing rings
were involved in the hydrogen release due to the delocalized π
bond in the whole molecule after dehydrogenation. Furthermore,
sodium phenoxide can be prepared by reacting phenol and
NaOH; therefore, it can be mass produced at low cost. It is
stable in air and water and has a low vapour pressure. All these
characteristics make the sodium phenoxide-cyclohexanolate pair
d
ΔH through forming phenoxide-cyclohexanolate pair, leading to
lower T
d
.
The slow kinetics in hydrogen uptake and release at lower
temperatures shown in Figure 3a and 3b implies inefficient
catalysis of solid Ru/Al O or Pt/C on solid-state reactants.
2 3
Therefore, we dissolved and dispensed the reactant and catalyst
in water and re-investigated the properties of hydrogenation and
dehydrogenation. It should be noted that
a
very attractive hydrogen storage material for practical
applications. Further efforts should focus on materials
engineering including developing more efficient
sodium
cyclohexanolate hydrolyzes into NaOH and cyclohexanol under
the conditions applied in the experiment. Under these conditions, hydrogenation/dehydrogenation catalyst and reaction medium.
hydrogenation and dehydrogenation actually react via R (5),
d 2
which has a ΔH of 182 kJ/mol (ca. 61 kJ/mol-H obtained from
C80 in the Supporting Information). Although with a higher ΔH
d
,
Acknowledgements
the entropy contribution of water may compensate such an
enthalpy loss. As shown in Figure 3c, ca. 100% hydrogenation
of sodium phenoxide can be achieved in 7.5 minutes at 100°C
under 40 bar of hydrogen and in the presence of commercial
T.H. and P.C. acknowledge the supports provided by the
National Natural Science Foundation of China (21875246,
51671178, 51472237), DICP (DICP ZZBS201616), Sino-
5%Ru/Al
2 3
O catalyst. Under a milder condition of 30°C and 2 bar
Japanese Research Cooperative Program of the Ministry of
Science and Technology (2016YFE0118300) and iChEM·2011.
A.W. would like to acknowledge the financial support provided
by the National Science Foundation of China (NSFC)
hydrogen, hydrogenation of sodium phenoxide also can be
1
achieved within 90 minutes. Cyclohexanol was detected by
H
NMR (Figure S11). Previous studies also showed that the
[
15]
[16]
hydrogenation of hydrocarbons such as phenol and toluene
(
21773193) and the fundamental research Funds for the Central
can be facilely carried out under mild conditions. However,
dehydrogenation is usually kinetically problematic. Therefore,
much attention is given to dehydrogenation.
Universities (20720160031). T.A. and A.K. gratefully
acknowledge support from the Hydrogen Materials − Advanced
Research Consortium (HyMARC), established as part of the
Energy Materials Network under the U.S. Department of Energy,
Office of Energy Efficiency and Renewable Energy, Fuel Cell
Technologies Office. Pacific Northwest National Laboratory is a
multi-program national laboratory operated by Battelle for the
U.S. Department of Energy under Contract DE-AC05-
C
6
H
5
ONa (aq.) + H
2
O (l) + 3H
2
(g) ⇌ C
6
H11OH (l) + NaOH (aq.)
R (5)
Because cyclohexanol and NaOH are the hydrogenation
products, we conducted the dehydrogenation of cyclohexanol
and NaOH in aqueous solution catalyzed by commercial 5%Pt/C.
Both phenoxide and cyclohexanone were found in the
dehydrogenation products as shown in Figure 3(d) and Figure
S12. Selectivity to phenoxide is pH dependent, i.e., the
dehydrogenation of cyclohexanol in the presence of one equiv.
of NaOH (pH = 13.3) has a conversion of cyclohexanol and
selectivity to phenoxide of 56.9 % and 81.0 % after 20 hours
reaction; with excess NaOH (pH = 14.0), both the conversion
and selectivity reach 60.0 % and 91.7 % within the same periods
of time. Prolonging the reaction leads to >99% conversion of
cyclohexanol and selectivity to sodium phenoxide in aqueous
7
6RL01830.
Keywords: reversible hydrogen storage • metallation • organic
hydride • thermodynamic modification
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[
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1
(
00°C, which is substantially lower than the T
generally >300°C for thermal dehydrogenation) and for N-
heterocycles and substituted cycloalkanes (generally >170°C for
d
for cycloalkanes
[
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[
10, 20]
thermal dehydrogenation).
Although the dehydrogenation of
1,2,3,4-tetrahydroquinolines or indolines can be achieved at
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