Table 2 Results of vapor-phase study
Notes and references
Cs0 in
catalyst conversion
(%)
Benzene
† EPR experiments were performed on a Bruker ER-200D electron-
paramagnetic-resonance analyzer at 298 K. The authors wish to thank Dr.
Paul Krusic and Mr. Steven Hill of the DuPont Company for their assistance
with these measurements.
Benzene
charge/ml
Catalyst/
g
Cs°
turnovers
Time/
h
(%)
‡ Batch reactions were performed in a stainless-steel, ‘tubing-bomb’ reactor
(2.54 cm o.d., 1.77 cm i.d. 15 cm long, capped with a hex nut and plug,
internal volume: 12 cm3). Catalyst and benzene were loaded in an argon-
atmosphere glove box. Extreme care was taken to eliminate air and water
contamination of the experiment. The reactor was sealed with a titanium
gasket, removed from the glove box and placed in a fluidized sand bath
maintained at the reaction temperature. After the desired reaction time was
reached, the reactor was quenched in water and the products were analyzed
by gas chromatography, confirmed by mass spectrometry.
§ A recirculating vaporizer/condenser reactor was constructed for the
experiments. Catalyst was loaded in an argon atmosphere glove box.
Extreme care was taken to eliminate air and water contamination of the
experiment. Argon cycled through the system at 1500 sccm in the following
order: bubbled through a temperature controlled (298 K) vessel containing
100 ml of benzene that was dried and deoxygenated over molecular sieves
and lithium ribbon; the benzene rich (5 mol%) argon passed through a flow
controller, a diaphragm pump and to the catalyst bed; the stream was heated
to 723 K and flowed through the catalyst bed (1.5 g of catalyst containing
15% by weight Cs, 0.025 s per pass contact time); the reacted stream then
returned to the bottom of the benzene vessel in which the biphenyl was
trapped due to its low vapor pressure (0.005 bar at 298 K) to repeat the cycle.
Products were analyzed by gas chromatography. No terphenyl was
detected.
¶ The control (untreated catalyst) and benzene treated samples were
prepared for transmission electron microscopic (TEM) studies by deposit-
ing them dry on carbon-coated Cu TEM grids. The grids were examined in
a JEOL 2000FX S/TEM fitted with a Noran energy dispersive spectroscopic
elemental analyzer. The control sample consisted of disordered appearing
carbon with the Cs dispersed uniformly throughout the support. While we
were not able to image individual particles of Cs on the carbon support,
elemental analysis confirmed the presence of Cs everywhere in the sample.
The used catalyst appeared similar to the control sample in microstructure
as well as elemental composition with the Cs dispersed uniformly
throughout the support. However, we observed a small fraction of the
carbon to have ordered to graphitic nanoparticles and microscopic sheets of
graphitic/turbostratic carbon during the benzene reaction process. No Cs
was detected in these ordered pockets of carbon. Based on the TEM
analysis, we estimate the amount of ordered carbon in the benzene-treated
sample to be approximately 5% on a volume basis.
100
50
50
1.5
1.0
1.1
1.0
15.0
14.9
15.8
0.0
2.40
2.60
2.75
0.00
20.43
16.70
15.15
—
96
72
72
96
50
Cs°
+
NPC
2e–
[Cs/NPC]*
+
2e– 2[Cs/NPC]+
2[Cs/NPC]*
2C6H6
• –
+
2C6H6
[C6H6–C6H6]2–
• –
2C6H6
[C6H6–C6H6]2–
[C6H5–C6H5]2–
C6H5–C6H5
+
H2
[C6H5–C6H5]2–
2e–
+
2e–
+
2[Cs/NPC]+
2[Cs/NPC]*
Scheme 1 Plausible catalytic mechanism.
near 2.5% benzene conversion. In this manner 29.8 mmol of
benzene were converted to biphenyl in 96 hours over 1.46 mmol
of caesium supported on NPC. This amounts to more than 20
turnovers based upon the total molar caesium content of the
catalyst. The experiment was repeated twice with essentially the
same result. Again, a control experiment using pure NPC did
not produce detectable levels of biphenyl.
Since Cs/NPC can facilitate the breaking of the C–H bond in
benzene (460 kJ mol21), we conclude that the metal provides,
through its powerful electropositive nature, the electrons
necessary to initiate the process. The carbon mediates the
reaction by acting as the electron repository, stabilizing the
intermediate radical anions. In the mechanism proposed by
Matsuzaki and coworkers,13 hydrogen and electron transfer are
critical steps. The carbon may aid in these steps by promoting
the net redox chemistry. Protons generated in the reaction can
couple to produce dihydrogen with the carbon supplying the
electrons to mediate the process. Additionally, the electron
exchange between neutral benzene and the radical anion is
facile (Ea ≈ 12 kJ mol21),15 and the carbon may stabilize the
intermediate radical anions produced in this chemistry, making
the net chemistry catalytic rather than stoichiometric. A
plausible catalytic mechanism is shown in Scheme 1. Since the
EPR measurements indicate caesium promotes its electron into
the local carbon structure, in essence NPC acts as a macro
radical anion that may be thought of as [Cs+/NPC·2]. From this
vantage point we can begin to see why the material may be so
able to promote demanding redox chemistry.
Finally, we have previously shown that caesium, when
loaded at high ratios (2/1 Cs0/C w/w), promotes the rearrange-
ment of the amorphous NPC to nanotubes, polyhedra and other
crystalline structures;16 transmission electron microscopy¶ of
the catalyst before and after benzene treatment indicates that
approximately 5% (by volume) of the carbon has transformed to
ordered structures. This limited conversion of the amorphous
NPC as compared to previous work16 may be attributed to the
combined effects of lower caesium content and the competitive
reaction with benzene. In conclusion, since the phenyl radical
anion is extremely difficult to produce and especially consider-
ing that deuterium exchange with methane has been shown,2
these results indicate an entirely new class of radical chemistry
may be open to heterogeneous-catalytic exploration in the
future.
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in press.
Communication 8/06604C
2680
Chem. Commun., 1998, 2679–2680