Inorganic Chemistry
Forum Article
computed the reduction potential at pH 7 in aqueous solution
using quantum-mechanical calculations and Monte Carlo
statistical mechanical simulations. It was derived as an efficient
protocol to obtain the solvation free energy of HNO using
three different computational approaches. A combination of
linear response theory and continuum solvation approaches
(COSMO/SMD) for more than a hundred uncorrelated
structures obtained from Monte Carlo simulations was used
to obtain −4.62 kcal mol−1 as the solvation free energy of
HNO, which is at least 2 times greater than the value of −5 kJ
mol−1 previously estimated by Shafirovich and Lymar in 2002,
on the basis of chemically related compounds. Considering the
In this work, first of all, we developed a kinetic modeling
approach to analyze electrochemical HNO measurements, in
order to determine, for the first time, the direct kRXH,NO rate
•
constant for the reaction between NO and ascorbic acid,
cysteine, and H2S, as a proof of concept. These values are up to
6 times higher than the previously reported keff values. On the
other hand, we also showed that the reaction of the successive
attack by two •NO molecules to biologically compatible
compounds could produce HNO.
2. MATERIALS AND METHODS
2.1. Experimental Procedures. Reagents. Cobalt(II)
5,10,15,20-tetrakis[3-(p-acetylthiopropoxy)phenyl]porphyrin was
purchased from Frontiers Scientific. All other reagents were purchased
from Sigma-Aldrich and used as received. NO was generated
anaerobically by the dropwise addition of degassed water to a mixture
of 4 g of NaNO2, 8.5 g of FeSO4, and 8.5 g of NaBr. The produced
NO was passed through a NaOH solution to remove higher oxides
and bubbled into degassed water in order to get a saturated solution
of NO ([NO] = 2 mM). This solution was kept under a strictly
anaerobic NO atmosphere and injected into the electrochemical cell
using a gastight syringe. The solutions of H2S were prepared by
bubbling with H2S(g) and dissolving Na2S. The reaction rate obtained
was similar using both methods, so it does not seem to be influenced
by the typical impurities present in NaHS (it is enriched with
polysulfides).
•
2017 protocol, it seems reasonable to take for the NO/HNO
reduction potential in aqueous solution, the value obtained by
Rocha and co-workers, E°′ = −0.16 V at pH 7,29 showing that
it is a viable process under physiological conditions.
Liochev and Fridovich had discussed the possibility of the
production of NO/HNO within living cells.17 The equilibrium
•
redox potential for NO/HNO in the cell can be much less
negative because the [•NO]/[HNO] ratio can be high, and
according to the Nernst equation, its logarithm influences the
actual redox potential. In this context, using the E°(NO,H+/
HNO) ≈ −0.11 V, the calculated redox potential E′ at
micromolar and picomolar concentrations of NO and HNO,
respectively, is between −0.30 and 0 V at pH 7.4. These redox
values are compatible with the observed reactions of NO with
alcohols, thiols, and HS−, as will be described in more detail
below.
Amperometric measurements of the HNO concentration were carried
out as previously described.43−45 A three-electrode system consisting
of a Pt counter electrode, a Ag/AgCl reference electrode, and a
working electrode consisting of Au modified with a monolayer of
cobalt porphyrin with 1-decanethiol which was covalently attached.
The method was demonstrated to be specific for HNO, showing no
Pryor, De Master, and co-workers found that anaerobic
aqueous solutions of thiols and thiol-containing proteins
exposed to NO result in quantitative formation of the
corresponding disulfides (RSSR) or sulfenic acids RS−
OH.33,34 These reactions, which took place in minutes, were
shown to produce N2O. The authors disregarded HNO as a
reaction intermediate, possibly because of the lack of selective
detection methods for HNO, with all being indirect at the
moment (1980s and 1990s). In this context, during the past
decade, the biologically compatible chemical reduction of •NO
(nonenzymatic) as direct routes to HNO was explored by our
group.35−40 The reduction of •NO to HNO has to be
necessarily coupled to other reactions that produce com-
pounds such as N2O, driving the reaction forward and
overcoming an unfavorable thermodynamic barrier. This
chemical reductive route recently received key support,
showing that •NO can be converted to HNO by the
aforementioned thiols,37 but also by hydrogen sulfide,35,40,41
aromatic and pseudoaromatic alcohols (i.e., ascorbic acid,
tyrosine, and salicylic acid),36,39 and alkylamines.38 In all cases,
the final concentrations of nitrite in solution and the amount of
N2O in the reaction chamber headspace were determined.
Both were produced in approximately a 1:1 ratio, as was
expected to occur due to the reaction between HNO and •NO.
−
interference or spurious signal due to the presence of NO, O2, NO2 ,
and other RNOS. Signal recording was performed with a TEQ 03
potentiostat. For each case, we also confirmed that the maximum
employed concentrations of NO and all organic reductants produced
negligible signals by themselves.
•
2.2. Kinetic Modeling of Reactions of NO with Reductants
to Produce HNO. In previous work, we have utilized an HNO-
specific electrode for sensing HNO concentrations as functions of
time and applied it to the analysis of several reactions that were shown
to produce HNO, as well as reactions of HNO with different chemical
and biological targets.44−46 In order to retrieve detailed kinetic
information related to HNO generation and consumption, a fairly
complicated kinetic model is necessary, and we have developed and
used this model on occasions.44,46 In many other cases, we used, for
simplicity, the electric current traces obtained with the electrode in a
semiquantitative way. The electric current traces for HNO sensing
usually show a relatively fast increase, which peaks and then decays
with different rates. In a full kinetic analysis, the slope of the initial
increase, the peak current, and the shape and rate of the decrease of
the current after the peak all contain relevant information. In the
simplified approach, only the peak current and position in time are
used. The peak current is transformed to a maximum concentration of
HNO, [HNO]max, by calibration with a standard curve derived from
the addition of Angeli’s salt (AS) to the cell, which has a known
decomposition constant. Then an effective rate velocity for each
experiment is derived as
−
2•NO + HNO → → → NO2 + N2O + H+
In previous work, we reported the effective rate constants keff
for the reactions of NO with the mentioned reductants in
anoxic conditions.42 These estimated values are a result of the
combined generation and consumption pathways. Because the
decay of HNO is extremely fast (see above), these values are
underestimations and imply that the “real” rate constants have
to be larger. A more detailed discussion of the relationship
between the “effective” and “real” rate constants is given in
Δ[HNO]max
v
≈
eff
Δtmax
The order of the reaction is also derived from a plot of veff as a
function of the reactant concentrations and a rate law is proposed,
from which an “effective” rate constant keff can be derived. This is an
empirical methodology that allows a comparison of several related
reactions and allows one to obtain kinetic information from an
otherwise very complicated reaction system.
B
Inorg. Chem. XXXX, XXX, XXX−XXX