Pleas De ad l to o nn oT tr aa nd sj au cs t ti omn as rgins
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ARTICLE
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Bratford on Avon, UK) were used. Setup and kinetic ΔS = -65.0 ± 3.0 J K mol for the reaction of the iron H-HPTB
DOI: 10.1039/D0DT01764G
measurements procedure already were described in detail complex are similar to the data obtained for an iron 6-Me
previously. The kinetic data were analysed with the integrated complex
software Kinetic Studio (Version 5.02 Beta, TgK Scientific). For dichloromethane) described previously.30 This is the only report we
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(ΔH = +29 kJ mol
and
ΔS = -77 J K mol
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the investigation of MNIC formation a 4 ∙10 mol L iron(II)
are aware of, in which such a reaction has been described in the past.
Furthermore, activation parameters for the reaction of this complex
with dioxygen (ΔH = +17 ± 2 kJ mol and ΔS = -175 ± 20 J K mol )
also fit quite well our data for the [Fe (H-HPTB)(Cl) ] complex
chloride tetrahydrate solution with 2.5 times excess of
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triethylammonium chloride (10 ∙10 mol L ) was prepared. To
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check the NO dependency of MNIC formation, these
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experiments were also carried out with a 0.6 ∙10 mol L
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(
ΔH = +15.4 ± 0.6 kJ mol and ΔS = -121 ± 3 J K mol ) taking the
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complex solution (0.6 ∙10 mol L iron(II) chloride tetrahydrate,
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large errors of the values for the activation entropy into account. In
general, it is quite difficult to compare the activation parameters for
the formation of iron NO complexes because they have been
obtained under quite different reaction conditions.
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.5 ∙10 mol L triethylammonium chloride) in order to obtain
better conditions for pseudo first order with higher nitrogen
monoxide excess. For the investigation of DNIC formation a
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2
∙10 mol L iron(II) chloride tetrahydrate with five times
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excess (10 ∙10 mol L ) triethylammonium chloride and
Understanding the mechanisms of these reactions is not only
important for the biological systems described in the introduction
but furthermore for industrial setups, such as reactions in bubble
flow columns. Knowing kinetic parameters for these reactions e. g.
for the formation of MNIC allow further optimization of future
applications.
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triethylamine (2 ∙10 mol L ) was prepared (to avoid formation
of iron precipitation triethylamine was added at the end). The
complex solutions were prepared in a glove box and filled into
gastight syringes. For the reaction of the iron(II) bztpen complex
with nitrogen monoxide a 1 ∙10 mol L solution with
bis(acetonitrile)iron(II) triflate and bztpen in a ratio of 1:1 was
prepared. For the reaction of the diiron(II) H-HPTB complex with
nitrogen monoxide a 2 ∙10 mol L complex solution was
prepared with anhydrous iron(II) chloride in a 2:1 ratio of iron
salt to ligand.
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Conflicts of interest
There are no conflicts to declare.
In-situ preparation of nitrogen monoxide
A suspension of 90 g (0.32 mol) iron(II) sulphate heptahydrate Acknowledgements
in 200 ml (2.04 mol) sulphuric acid was filled in a dropping
The authors gratefully acknowledge financial support from the
German Research Foundation (DFG, Deutsche
Forschungsgemeinschaft) received within the scope of SPP 1740
Influence of local transport processes in chemical reactions in
funnel and added in small portions to 140 g (2.03 mol) sodium
nitrite in a Schlenk flask. Before starting to prepare nitrogen
monoxide the whole apparatus was flushed with nitrogen to
remove oxygen. The gas stream was then passed through wash
bottles filled with concentrated sodium hydroxide solution to
remove nitric dioxide and solid sodium hydroxide was used for
drying.
(
bubble flows), SCHI 377/13-1 and KL 624/18-1).
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FeSO4 + 3 H2SO4 + 2 NaNO2
2 2 4 3
2 NO + 2 H O + Fe (SO ) + 2 NaHSO4
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methanol using low temperature stopped-flow techniques.
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Activation
parameters
of
ΔH = +37.7 ± 0.7 kJ mol
and
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