Reactions of Diphenyl Ether with Chlorine and Bromine Atoms Around 750 K
FULL PAPER
•
addition of Cl to PhOPh is expected to be reversible to a liquid samples were injected at a split ratio of 1:15. Absolute con-
centrations were deduced from the peak areas, after calibration by
limited extent only.
injecting standard mixtures of known composition. A Hewlett
Anyway, in the chlorine case our observed product ratios
Packard 5890 GC-MS was used to identify unknown products.
PhCl/DF Ϫ as discussed in section (i) Ϫ entail nearly equal
Outflows of HCl or HBr were quantified by means of a Mettler
rates (activation barriers) for splitting and H abstraction.
DL25 automatic titrator. Exit non-condensable gases were analysed
This is in full accord with the observed E for the forward
Reaction 4 as reported by Grotheer and Louw.
Sidhu’s value of 19.5 kcal/mol inferred from the slow com-
a
using a Packard series 428 GC equipped with FID detector, Car-
boplot 007 column and a methanizer, calibrated by independent
injections of a standard gas mixture. The reaction of chlorine
[11]
Should
bustion of 2,4,6-Cl C H OH apply here, splitting would (atoms) was studied at 460Ϫ480°C by using diphenyl ether ad-
3
6
2
•
[14]
have been by far the major process. In our view, ArO ϩ mixed with tetrachloromethane and hexachloroethane
ArO combination, etc. must have been at least as impor- dence times of about 2 min. Experiments involving bromine atoms
tant as the S&T-type ArO ϩ chloroarene displacements.
As mentioned above for the bromine case, bond strengths
may vary, but the overall endothermicity for the latter type
and resi-
•
•
were carried out at 500°C, with comparable residence times. Br
2
was fed in from an impinger by a calibrated flow of nitrogen. Here
PhOPh was diluted with benzonitrile or p-difluorobenzene, both
less reactive in gas-phase halogenation than diphenyl ether.
[13,14]
•
of reaction (17 kcal/mol for our base case PhO ϩ PhCl)
Purity of Reagents: Tank N 99.99% was supplied by Hoekloos in
2
should not change drastically upon introducing (chlorine)
substituents Ϫ let alone that displacement becomes about
thermoneutral, or even exothermal, as advanced by Bozzeli
To the best of our knowledge there are no known
experimental data to support such a proposal.
a standard cylinder. Diphenyl ether (Merck, pro synthesis), tetra-
chloromethane (J. T. Baker, > 99%), hexachloroethane (Fluka,
pure), benzonitrile (Merck, pro synthesis), p-difluorobenzene
Fluka, pure) were checked by GC to be of adequate (> 99%) purity
and used as such. Reference compounds such as chlorobenzene,
bromobenzene, and dibenzofuran were high-grade (> 99.9) com-
[19]
et al.
(
•
Our results on the PhCl(Br) ϩ PhO systems, and vice
versa, imply that PhO has only a low reactivity in addition mercial products.
•
to benzene derivatives, even in the nearly neutral displace-
ment of Br. The reasons for that are not yet clear, but we
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wish to point out that Ϫ while phenoxy-type radicals are of
[
•
K. Tuppurainen, I. Halonen, P. Ruokojarvi, J. Tarhanen, J.
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key importance in antioxidant action Ϫ next to ArO (self
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[
•
•
[20]
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ArO ϩ ArЈOH Ǟ ArOH ϩ ArЈO hydrogen transfers,
1
595Ϫ1601 and references cited there.
•
we are unaware of other examples of ArO ϩ molecule reac-
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Experimental Section
[8]
All experiments were conducted in a cylindrical, stirred-tanktype
flow reactor of 680 ml volume placed in an electrically heated oven.
The temperature was controlled by a proportional regulator and
monitored with chromel-alumel thermocouples displayed on digital
thermometers (Therma 1, type ST-861Ϫ107). The upper and lower
ends of the oven were insulated by quartz wool. For further details
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J. G. P. Born, Ph. D. Thesis (in English), Leiden University,
1
992.
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I. W. C. E. Arends, R. Louw, P. Mulder, J. Phys. Chem. 1993,
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[
11]
H. H. Grotheer, R. Louw, 26th Symp. ( Int.) on Combustion,
Naples, Italy 1996, p. 2405Ϫ2411.
12]
[
[12]
H. H. Grotheer, R. Louw, Combust. Sci. Technol. 1998, 134,
31Ϫ49.
on this type of setup see ref.
Gas flows were regulated by needle
valves and measured with capillary flow meters. Liquid (organic)
reactants were introduced by means of a calibrated motorized syr-
inge pump (B. Braun, Melsungen, Perfusor VI type 871222/0) via
a gas-tight rubber septum and vaporized into the gas flow before
entering the reactor. The entrance and exit tubes of the reactor
were heated by wrapped heating tape to prevent condensation of
the less volatile organics. Condensable products were collected in
two cold traps. The first one contained aqueous potassium hydrox-
ide and toluene, and was cooled with ice. The second trap, with
toluene, was cooled by acetone with liquid nitrogen. For experi-
ments C1ϪC7 bromobenzene was used as an external standard and
for B1ϪB6 chlorobenzene. Aromatic compounds were quantified
with a Hewlett Packard 5890A gas chromatograph with FID using
a CP-SIL5-CB column (50 m ϫ 0.32 mm ID). 1-µL portions of
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E. C. Kooyman, Advances in Free-Radical Chemistry, vol. 1,
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W. Dorrepaal, R. Louw, Int. J. Chem. Kinet. 1978, 10, 249Ϫ275.
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1
961, 80, 526Ϫ532.
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I. W. C. E. Arends, Ph. D. Thesis (in English), Leiden Univer-
sity, 1993.
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M. Pecullan, K. Brezinsky, I. Glassman, J. Phys. Chem. 1997,
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01, 3305Ϫ3316 and references cited there.
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P. M. Sommeling, P. Mulder, R. Louw, Chemosphere 1994, 29,
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16, 9440Ϫ9447.
Received August 14, 1998
[O98382]
Eur. J. Org. Chem. 1999, 261Ϫ265
265