“…The extent of retained chlorine is within the range observed previously. 5 The error on the bromine analysis corresponds to a variance of ±72%, which reflects the variability of the bromine content observed in the different scans that ranged from 0–4.2 wt %. This dispersion indicates an uneven distribution of bromine throughout the areas examined.…”
Section: Resultsmentioning
confidence: 99%
“…A similar situation was previously reported for chlorine. 5 Small quantities (<1 wt %) of Si, Al, and S are additionally observed; the origins of these signals are unknown.…”
Section: Resultsmentioning
confidence: 99%
“…The following reaction scheme has recently been proposed by the authors to account for the reaction of CO and Cl 2 over activated carbon at 323 K to selectively produce COCl 2. 5 where eqs 6 – 9 constitute the reaction model to account for the reaction of CO (g) and Cl 2(g) over activated carbon (Donau Supersorbon K40) at 323 K to produce phosgene. K 1 and K 2 are equilibrium constants and k 1–3 are rate coefficients.…”
Section: Discussionmentioning
confidence: 99%
“…Chlorine adsorbed on Type I sites is designated by Cl′ (ad) , while chlorine at Type II sites is designated by Cl″ (ad) . 5 Importantly, chlorine atoms chemisorbed at Type I sites are thought to be in equilibrium with chlorine atoms residing in Type II sites ( eq 10 ). 5 …”
The effect of relatively
low concentrations of Br
2(g)
in the Cl
2(g)
feedstock
for phosgene synthesis catalysis
via the reaction of CO
(g)
and Cl
2(g)
over activated
carbon (Donau Supersorbon K40) is explored. Under the stated reaction
conditions and in the absence of a catalyst, BrCl
(g)
forms
from the reaction of Cl
2(g)
and Br
2(g)
. Phosgene
synthesis over the catalyst at 323 K is investigated for Br
2(g)
:Cl
2(g)
molar flow ratios in the range 0–1.52%
(0–15,190 ppm) and shows enhanced rates of phosgene production.
Maximum phosgene production is observed at a Br
2(g)
:Cl
2(g)
molar flow ratio of 1.52% (15,190 ppm), which corresponds
to an enhancement in the rate of phosgene production of ∼227%
with respect to the phosgene flow rate observed in the absence of
an incident bromine co-feed. A reaction model is proposed to account
for the experimental observables, where BrCl
(g)
is highlighted
as a significant intermediate. Specifically, enhanced rates of phosgene
production are associated with the dissociative adsorption of BrCl
(g)
that indirectly increases the pool of Cl
(ad)
available for reaction.
“…The extent of retained chlorine is within the range observed previously. 5 The error on the bromine analysis corresponds to a variance of ±72%, which reflects the variability of the bromine content observed in the different scans that ranged from 0–4.2 wt %. This dispersion indicates an uneven distribution of bromine throughout the areas examined.…”
Section: Resultsmentioning
confidence: 99%
“…A similar situation was previously reported for chlorine. 5 Small quantities (<1 wt %) of Si, Al, and S are additionally observed; the origins of these signals are unknown.…”
Section: Resultsmentioning
confidence: 99%
“…The following reaction scheme has recently been proposed by the authors to account for the reaction of CO and Cl 2 over activated carbon at 323 K to selectively produce COCl 2. 5 where eqs 6 – 9 constitute the reaction model to account for the reaction of CO (g) and Cl 2(g) over activated carbon (Donau Supersorbon K40) at 323 K to produce phosgene. K 1 and K 2 are equilibrium constants and k 1–3 are rate coefficients.…”
Section: Discussionmentioning
confidence: 99%
“…Chlorine adsorbed on Type I sites is designated by Cl′ (ad) , while chlorine at Type II sites is designated by Cl″ (ad) . 5 Importantly, chlorine atoms chemisorbed at Type I sites are thought to be in equilibrium with chlorine atoms residing in Type II sites ( eq 10 ). 5 …”
The effect of relatively
low concentrations of Br
2(g)
in the Cl
2(g)
feedstock
for phosgene synthesis catalysis
via the reaction of CO
(g)
and Cl
2(g)
over activated
carbon (Donau Supersorbon K40) is explored. Under the stated reaction
conditions and in the absence of a catalyst, BrCl
(g)
forms
from the reaction of Cl
2(g)
and Br
2(g)
. Phosgene
synthesis over the catalyst at 323 K is investigated for Br
2(g)
:Cl
2(g)
molar flow ratios in the range 0–1.52%
(0–15,190 ppm) and shows enhanced rates of phosgene production.
Maximum phosgene production is observed at a Br
2(g)
:Cl
2(g)
molar flow ratio of 1.52% (15,190 ppm), which corresponds
to an enhancement in the rate of phosgene production of ∼227%
with respect to the phosgene flow rate observed in the absence of
an incident bromine co-feed. A reaction model is proposed to account
for the experimental observables, where BrCl
(g)
is highlighted
as a significant intermediate. Specifically, enhanced rates of phosgene
production are associated with the dissociative adsorption of BrCl
(g)
that indirectly increases the pool of Cl
(ad)
available for reaction.
“…The gaseous reactants were pumped through the system using a peristaltic pump for 242 min. IR spectra were recorded 0, 3,6,9,12,15,19,22,25,28,39,40,100,161,221,282,342, 403, 363, and 524 min (fig. S23).…”
Section: General Description Of the Flow Setupmentioning
Chloride ions are efficient catalysts for the synthesis of phosgene from carbon monoxide and elemental chlorine at room temperature and atmospheric pressure. Control experiments rule out a radical mechanism and highlight the role of triethylmethylammonium trichloride, [NEt 3 Me][Cl 3 ], as active species. In the catalytic reaction, commercially available [NEt 3 Me]Cl reacts with Cl 2 to form [NEt 3 Me][Cl 3 ], enabling the insertion of CO into an activated Cl─Cl bond with a calculated energy barrier of 56.9 to 77.6 kJ mol −1 . As [NEt 3 Me]Cl is also a useful chlorine storage medium, it could serve as a catalyst for phosgene production and as chlorine storage in a combined industrial process.
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