Next Article in Journal / Special Issue
Interfacial Mass Transfer in Trichloroethylene/Surfactants/ Water Systems: Implications for Remediation Strategies
Previous Article in Journal
Microstructure and Hydrogen Storage Properties of the Multiphase Ti0.3V0.3Mn0.2Fe0.1Ni0.1 Alloy
Previous Article in Special Issue
Effect of Pre-Treatment Conditions on the Activity and Selectivity of Cobalt-Based Catalysts for CO Hydrogenation
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

An Upper Limit to O2 Evolution as Test for Radical and Nonradical Mechanisms for the Fenton Reaction

by
Mordechai L. Kremer
Institute of Chemistry, Hebrew University, Jerusalem 91904, Israel
Reactions 2021, 2(3), 301-311; https://doi.org/10.3390/reactions2030019
Submission received: 13 May 2021 / Revised: 24 August 2021 / Accepted: 30 August 2021 / Published: 2 September 2021
(This article belongs to the Special Issue Feature Papers in Reactions in 2021)

Abstract

:
The origin of an upper limit to the amount of O2 evolved in the rapid reaction between Fe2+ and H2O2 was investigated at a high concentration of H2O2. Using a nonradical model, including the formation of a primary Fe2+–biperoxy complex with a diminished rate of formation of the active intermediate FeO2+, agreement has been reached for the first time with the experimental data obtained by Barb et al. A limited formation of O2 requires that a finite concentration of H2O2 should be present in the reaction mixture when [Fe2+] falls to zero. It has been shown that in Barb et al.’s model the condition for such a state ([Fe2+] = 0, [H2O2] > 0) does not exist. Free radical based models fail as mechanisms for the Fenton reaction.

1. Introduction

The question of the mechanism and intermediates in the reaction between Fe2+ and H2O2 (the Fenton reaction) has been the subject of intensive investigation for over a century [1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20]. The reaction has gained importance as a method for the elimination of industrial waste [1]. In a different field, interest is growing in the possible significance of intermediates of the reaction in processes occurring in living systems [2]. Basic questions relating to the mechanism of the reaction are, however, still open. One of them concerns the variation of the ratio of concentrations of products upon variation of concentrations of reactants. There are two processes occurring in the system: oxidation of Fe2+ by H2O2 and decomposition of H2O2 to O2 and H2O. Based on a hypothesis of Haber and Willstaetter regarding the role of free radicals in chemical reactions, Haber and Weiss have proposed a model of the mechanism of the Fenton reaction [3]. It claimed to explain the dependence of the ratio [O2]/[Fe3+], on the ratio [H2O2]o/[Fe2+]o ([O2] is the number of moles of O2 evolved per 1 dm3 of reaction mixture, the symbol [ ]o denotes initial concentration), by attributing it to a competition of the reactions of the radical OH· with Fe2+ and H2O2, respectively. According to this theory, there should be no upper limit to the amount of O2 evolved upon increasing the ratio [H2O2]/[Fe2+] in the reaction mixture. This prediction was found to be in contradiction to the experiment. Using high [H2O2]o/[Fe2+]o, Barb et al. observed a rapid evolution of O2 followed by a slow one [4]. They found that using [H2O2]o ≥ 0.5 mol dm−3, the amount of O2 evolved in the rapid phase reached a limit. A revision of the Haber Weiss model was suggested by a modification of the O2 evolution step (see further on for details). It appears, however, that in spite of this and numerous other studies, no positive evidence has yet been provided that the revised scheme does account for the existence of an upper limit. Since the existence of the limit is an experimental fact, it was the aim of the present study to investigate its origin and to give a quantitative explanation for it.

2. The Mechanism

Barb et al. measured the amount of O2 gas evolved in the time interval of 0–3 min [4]. The first measurement was made at 5 s. Linear [O2] vs. time plots were obtained with positive intercepts on the [O2] axis (Figures 1 and 6 in Reference [4]). The existence of these intercepts implied that there was a short and rapid reaction in the system before the first measurement of [O2] could be made. Since a point at 5 s on a time scale extending from zero to 3 min appears near the origin of the time scale, the intercept on the [O2] axis could be identified, in good approximation, with [O2] evolved in the rapid phase. The problem of finding a mechanism for a satisfactory interpretation of the experimental results in the rapid phase presented a serious challenge as no [O2] vs. time and [Fe2+] vs. time data (or their equivalents) were available in the time interval of 0–5 s, only the values of [O2] at its end in a series of experiments (experimental difficulties being due to gas evolution in the reacting solution in optical measurements, danger of explosion in a closed stopped flow apparatus, etc.). The following interpretation is based on a nonradical model [10,11]. It is presented in Figure 1. It assumes the formation of an active intermediate FeO2+, formed from a precursor complex Fe2+·H2O2 (C1). In addition, and as a modification of an earlier version of the model, it includes the formation of a biperoxy complex (C2) yielding FeO2+ at a lower rate than C1 (step 10). This extension proved to be necessary to account for the existence of a limit to the amount of O2 formed in the reaction at high [H2O2]. Neglecting the slow step 10, the mechanism has one path for oxidizing Fe2+ to Fe3+ (reactions (1)-(3)-(5),) and two reaction cycles ((1)-(3)-(4)-(1) and (1)-(3)-(6)-(7)-(1)) for the production of O2. Steady state has been assumed to exist for [FeO2+], but not for [C1] and [C2]. Steady state existed necessarily for [FeOFe5+]. Its presence in the system was discovered only when [H2O2] was reduced to the 10−5 molar range [10]. A total of 105 fold higher [H2O2] reduced [FeOFe5+] to the steady state range. Assuming negligible rate constants for the back reactions k2, k8, k11, the following rate equations were obtained
d[C1]/dt = k1 [Fe2+] [H2O2] − (k3 + k9 [H2O2]) [C1]
d[C2]/dt = k9 [H2O2] [C1] − k10 [C2]
d[Fe3+]/dt = 2 vR R2
d[O2]/dt = vR (R1 + R3)
vR = k3 [C1] + k10 [C2]
[FeO2+] = vR/(k4 [H2O2] + k5 [Fe2+] + k6 [Fe3+])
R1 = [H2O2]/([H2O2] + (k5/k4) [Fe2+] + (k6/k4) [Fe3+])
R2 = [Fe2+]/((k4/k5)[H2O2]+[Fe2+]+(k6/k5)[Fe3+])
R3 = [Fe3+]/((k4/k6) [H2O2] + (k5/k6) [Fe2+] + [Fe3+])
[Fe2+] = [Fe2+]o − [Fe3+] − [C1] − [C2]
H2O2] = [H2O2]o − 2 [O2] − 0.5 [Fe3+]
In the calculation of [H2O2], [C1] and [C2] could be neglected because of the large excess of [H2O2] over [Fe2+] in the experiments. The differential equations were integrated numerically by using the method of Gear. The initial value of [Fe2+] in the simulations was 4 × 10−2 mol dm−3. To cover the range of [H2O2] in the experiments of Barb et al. (Figure 6, pH = 1.8, T = 0 °C, [4]), seven simulation runs were performed at seven [H2O2]o with equal intervals between them in the range 0.5–3.5 mol dm−3 (among them concentrations identical with those used in the experiments). [Fe3+], [C1] and [C2] at time = 0 were set to zero. Trial values of rate constants k1, k3, k9, k10, k4/k5, k6/k5 were inserted as initial parameters. (Other rate constants appearing in the rate equations were calculated as combinations of the parameters of the basis set.) [C1], [C2], [Fe3+] and [O2] vs. time curves were simulated. For a successful simulation, the convergence of all [O2] vs. time curves at 5 s at the target value of 1.40 × 10−2 mol dm−3 (upper limit at pH = 1.8 in the experiments of Barb et al. [4]) was a necessary but not sufficient condition. As around 5 s, or before it, there is a sharp fall in the rate of O2 evolution, the limit must be approached in all runs with diminishing slopes of the [O2] vs. time curves. To this end, simulations were continued beyond 5 s and values obtained at 6, 7, and 8 s were also included in the summation of squared deviations of calculated values of [O2] from 1.40 × 10−2 mol dm−3. The total sum of squared deviations was minimized by varying rate parameters using a combination of Migrad and Simplex minimum searching routines.

3. Results

To calculate meaningful values of standard deviations, the number of simulations was increased to 31 by changing [H2O2]o between 0.5 and 3.5 mol dm−3 in steps of 0.1 mol dm−3. The standard deviation of calculated [O2] values at 5 s from the target of 1.40 × 10−2 mol dm−3 was 1.4 × 10−4 mol dm−3. The optimal set of rate parameters together with conditional standard deviations were: k1 = (3.84 ± 0.13) × 10 mol−1 dm3 s−1, k3 = (1.19 ± 0.03) × 102 s−1, k9 = (3.16 ± 0.04) × 10 mol−1 dm3 s−1, k10 = 2.02 × 10−4 s−1, k4/k5 = (2.82 ± 0.06) × 10−3, k6/k5 = (1.52 ± 0.05) × 10−1. (Due to step 10 being a slow parallel path to FeO2+ formation, it was not possible to determine the conditional standard variation of k10.) Similar values of k1 and k9 indicate similar energetic conditions for the first and second H2O2 molecules to enter the coordination sphere of Fe2+ ions. The difference between them appears in the rate of their decomposition to yield FeO2+. Here C2 shows more stability and consequently lower rate constant of decomposition (k10 << k3). This difference is at the root of the existence of a limit to O2 evolution at high [H2O2]. In Figure 2, simulated curves of [O2] vs. t are shown at [H2O2]o = 0.5 and 3.5 mol dm−3, (triangles and squares, respectively) representing the lower and upper limits of the concentration range in the experiments.
[Fe2+]o = 4.00 × 10−2 mol dm−3
[H2O2]o = 0.5 mol dm−3 (triangles)  [H2O2]o = 3.5 mol dm−3 (squares)
k1 = 3.84 × 10 mol−1 dm3 s−1k3 = 1.19 × 102 s−1
k9 = 3.16 × 10 mol−1 dm3 s−1k10 = 2.02 × 10−4 s−1
k4/k5 = 2.82 × 10−3k6/k5 = 1.52 × 10−1
At high [H2O2], it showed a very rapid approach (measured on the timescale of milliseconds) to an upper limit of [O2]. The curve with low [H2O2] reached the same limit in about 1.5 s. Figure 3 presents calculated (circles) and experimental (triangles) values of the amount of O2 evolved at 5 s. Table 1 lists the numerical results.
Data both in the Figure and in the Table show that agreement has been reached between calculated and experimental values of [O2] evolved in 5 s both showing constancy in the range of [H2O2]o = 0.5–3.5 mol dm−3. (It may be added at this point that a previous attempt to account for the existence of the upper limit to O2 evolved; using the nonradical model without the inclusion of C2, was not successful [11].)

4. Discussion

To investigate the source of convergence of [O2] vs. time curves at 5 s, the terms contributing to the rate of O2 formation were examined. These were vR, R1, R2 and R3. By definition, R terms vary between 0 and 1, some decreasing and some increasing in the course of the reaction. Plots of the terms R1 (circles), R2 (squares) and R3 (triangles) are shown in Figure 4. (Initial conditions [H2O2]o = 2 mol dm−3 and [Fe2+]o = 4 × 10−2 mol dm−3 and [Fe3+]o = 0.) Plots were obtained by entering the numerical values of the rate parameters and of their combinations into Equations (7)–(9). The following results were obtained:
  • The starting value of R1 was 0.12. It rose in 0.2 s to 0.59 and remains constant.
    (Although [H2O2] is decreasing, R1 is increasing due to the steep decrease in the [Fe2+] term in the denominator.)
  • The starting value of R2 was 0.88. It decreased in 0.2 s to practically zero.
  • The starting value of R3 was 0. It rose in 0.2 s to 0.41 and remained constant.
These results showed that, except for a short initial period, all R terms were constant during the time interval ending at 5 s. The reason for the particular shape of the [O2] vs. time curves must therefore be found in the time variation of vR. Since k3 >> k10, the time variation of vR was determined almost entirely by the time variation of [C1] but indirectly also by that of [C2]. Figure 5 shows this variation. In the Figure, plots of [C1] vs. t (triangles) and [C2] vs. t (squares) are shown at [H2O2]o = 0.5 mol dm−3 (empty markers) and 3.5 mol dm−3 (full markers). The form of the curves in the Figure is the result of two opposing effects of [H2O2] on the kinetics of the reaction. At high [H2O2], the rate of formation of C1 was high, [C1] reaching a (relatively) high maximum. Up to the maximum, conversion of C1 into C2 decreased the rate of increase of [C1]. After the maximum, it increased the rate of decrease of C1. The second effect was more pronounced as [C2] was higher after the maximum than before it. At low[H2O2], there was slow accumulation of C1 with a low maximum of [C1].
There was little formation of C2 with little retardation of the increase in [C1] and little acceleration of its decrease. Because of the rapid fall of [C1] after the maximum at a relatively high value of [H2O2] and its damped change at low [H2O2], the decreasing parts of [C1] vs. time plots a high and low [H2O2] had a point of intersection. This implies, that up to the point of intersection, the rate of formation of the active intermediate FeO2+ (vR ≈ k3 [C1]) was higher with high [H2O2], but after the point of intersection, it became relatively higher with lower [H2O2]. Since under the conditions of the experiments [Fe2+] << [H2O2], practically all FeO2+ will produce O2. Therefore, vR can be equated, in good approximation, with the rate of production O2 (vO2). We can summarize the results of this section as follows. Denoting high and low [H2O2] by (a) and (b), and the time interval up to and after the point of intersection by (α) and (ß), respectively, we have the following relationships between rates of evolution of O2 in the two phases of the reaction in the time interval 0–5 s:
vO2(aα) > vO2 (bα) and vO2(aβ) < vO2(bβ)
This is shown in Figure 6. Full triangles represent simulations with [H2O2]o = 3.5 mol dm−3 (case a), empty triangles with [H2O2]o = 0.5 mol dm−3 (case b).
The two curves have a point of intersection at about 40 ms. The similarity between the corresponding curves of [C1] in Figure 5 and of vO2 in Figure 6 is clear. The total amount of O2 evolved at high and low [H2O2] during the time interval 0–5 s can be written as
O2(a) = O2(aα) + O2(aβ) and O2(b) = O2(bα) + O2(bβ)
Considering the inequalities in Equation (10), the difference in rates during phase α between case a and b are larger than the reversed differences during phase β. The duration of phase β is, however, considerably longer than that of phase α, (about 125 times longer in the present case). Thus, in case b, a lesser amount of O2 produced during phase α may be balanced by a larger amount produced during phase β. The extent of balancing depends on the amounts of O2 produced during phases α and β in cases a and b. The fact that in the simulations a constant amount of O2 was calculated in all runs in 5 s proves that for the sums in Equation (11) exists
O2(aα) + O2(aβ) = O2(bα) + O2(bβ) = constant
The existence of an upper limit to O2 evolved is thus due to the constancy of the sum of pairs of O2(xα) and O2(xβ) terms where x denotes any concentration of H2O2 between 0.5 and 3.5 mol dm−3.
Figure 7 shows the variation in time of the rates of reaction in the two O2 producing cycles denoted as v4 and v6, respectively. Their values are presented as empty triangles and full squares. Values of the total rate of evolution of O2, vO2 = v4 + v6, are shown as full triangles. Initially, [Fe3+] = 0 and vO2 = v4; the two curves coincided. As Fe3+ began to be formed, the rate of the Fe3+ ion catalyzed path of O2 evolution became significant too. The maximum of the total rate of formation of O2 occurred near 20 ms, while at about 100 ms, most of the O2 measured at 5 s had already been formed. It explains why it appeared as an initial burst (catalase burst). Reducing the concentration of [H2O2] by a factor of 103 to 104, the role of C2 in the mechanism became insignificant [10]. The influence of C2 on the kinetics of C1 at high [H2O2] provides indirect proof of the formation of the primary intermediate C1, until now only assumed to exist. It should be noted that the inclusion of C2 in the mechanism implies that when using the mixture Fe2+ + H2O2 in oxidation of substrates, the increase in [H2O2] beyond a certain limit decreases the efficiency of the mixture as it decreases the rate of formation of FeO2+. In agreement with this prediction, Barb et al. report that “dilute solutions of methyl orange are readily oxidized to colorless compounds by 10−4 mol dm−3 Fe2+ and 10−4 mol dm−3 H2O2 to give completely colorless solutions [4]. When the hydrogen peroxide concentration is increased, the extent of this oxidation is decreased, and with 1 mol dm−3 H2O2, no destruction of color is observed” (Ref. [4], p. 464). The simulations showed only the increasing part of the [C2] vs. t curve up to a plateau. Concerning the decreasing part, the half time of decay from the maximum value can be calculated to be 58 min, a time span much longer than that in which measurements were made (3 min). Therefore, in the time range of the experiments C2 can be regarded as an inert intermediate. The quantitative aspect of the discussion on this point is, however, only approximate, due to the difficulty of determining the value of k10 with sufficient accuracy.
The concept of FeO2+ as intermediate in the Fenton reaction has been supported by density functional studies of Baerends and coworkers and also by Lu and coworkers. They have shown that the energetically favorable path of the reaction between Fe2+ and H2O2 led to the formation of FeO2+ rather than free radicals [15,16].

5. Free Radical Models of the Mechanism of the Fenton Reaction

In free radical models based on one-equivalent oxidation/reduction reactions, the precursor of O2 is the radical HO2·. The first model, proposed by Haber and Weiss, consists of the following steps:
Fe2+ + H2O2 → Fe3+ + OH· + OH
OH· + H2O2 → HO2· + H2O
HO2· + H2O2 → OH· + O2 + H2O
OH· + Fe2+ → Fe3+ + OH
It is a chain reaction in which (13) is the initiation step, (14) and (15) are chain carriers, and (16) is the chain termination step. OH· and HO2· are free radicals derived from H2O2. The balance between the oxidation of Fe2+ and O2 evolution depends on the ratio r = [H2O2]/[Fe2+], i.e., on the balance between reactions (14) and (16). At low r, (16) is dominant and the reaction is restricted to steps (13) and (16), resulting in oxidation of Fe2+ and no evolution of O2. At increasing r, (14) begins to compete with (16) and evolution of O2 accompanies the oxidation of Fe2+, as observed experimentally. In deriving rate expressions for the formation of products, free radical intermediates are assumed to be in steady states. Their concentrations are given by the equations
[OH·] = (k13/k16) [H2O2] and [HO2·] = {k13k14/(k15k16)} [H2O2]
The rate of O2 evolution becomes (Ref. [3], Equation (6))
d[O2]/dt = (k13k14/k16) [H2O2]2
This equation cannot be the correct expression for the rate of O2 evolution in the Fenton reaction. Namely, according to it, the rate should be no function of [Fe2+], thus that of r. The model, on the other hand, requires that d[O2]/dt should approach zero with decreasing r by increasing [Fe2+] at a finite [H2O2]. According to Equation (14) d[O2]/dt becomes zero only for [H2O2] = 0. The rate equation is therefore not consistent with the model: the Haber Weiss scheme falls short of accounting for the course and kinetics of the Fenton reaction.
A modification of the Haber and Weiss model has been suggested by Barb et al. [4].
Fe2+ + H2O2 → Fe3+ + OH· + OH
OH· + Fe2+ → Fe3+ + OH
OH· + H2O2 → HO2· + H2O
HO2· + Fe2+ → Fe3+ + HO2
HO2· + Fe3+ → Fe2+ + O2 + H+
The crucial change in the model is the replacement of H2O2 by Fe3+ in (22) as the O2 producing step. With this modification, the model ceases to be a chain reaction. Namely, there are three pathways along which the reaction can proceed: (1) (18)-(19) (Fe2+ oxidation), (2) (18)-(20)-(21) (Fe2+ oxidation), and (3) (18)-(20)-(22) (O2 evolution). The last one is a self-repeating cycle. The Barb model is not a chain reaction, because the initiation step (18) is part of the O2 producing cycle. (In a chain reaction the product forming cycle cannot include the initiation step). The following description of the course of the reaction is valid for concentrations of reactants used in the experiments of Barb et al.: [H2O2]o = 0.5–3.5 mol dm−3 and [Fe2+]o = 4 × 10−2 mol dm−3 [4]. Regarding rate constants, in the present context it is sufficient to note that rate constants of reactions involving free radicals (k19, k20, k21, k22) are extremely high while that of a reaction between an ion and a molecule (k18) is in comparison low. The kernel of the model is the cycle consisting of (18), (20), and (22). Their sum is 2 H2O2 = O2 + 2 H2O. It presents the path for the decomposition of H2O2. Fe2+ and Fe3+ ions participate in these reactions but are cancelled out in the summation. It means that they are neither formed nor consumed in the cycle; their concentrations remain constant. Thus, the cycle of the three reactions presents a scheme for the catalytic evolution of O2 by the pair Fe3+–Fe2+. Reactions (20) and (22) have high rate constants, while that of (18), is low; (18) is, therefore, the rate determining step in the cycle. In the absence of further reactions, there is mutual balance among the rates of the reactions of the cycle; all rates are equal. Reactions (19) and (21) act as perturbations; they remove the carriers of the cycle: HO2., OH· and Fe2+. At the start of the reaction, the course involves both the steps of the kernel and the perturbations. Due to perturbations, the rate of the evolution of O2 (22) will be less than the rate of production of free radicals (18), because a fraction of free radicals has been removed in perturbation reactions. In these reactions Fe2+ ions are oxidized to Fe3+. As a result, [Fe2+] and the rate of initiation becomes lower. A new cycle will end with an additional amount of Fe2+ ions oxidized to Fe3+. As the cycles are repeated, [Fe2+] will be reduced continuously until it will become negligible beside both [H2O2] and [Fe3+]. Perturbation reactions will then become insignificant and the course of the reaction will be reduced to reactions of the kernel. From this point on, O2 will be evolved in a steady state at a constant and low [Fe2+]; the reaction will become a catalytic decomposition of H2O2. With the existing rate constants, the rate of O2 evolution in the initial phase, in spite of perturbation reactions, is high (measured on a timescale of seconds). In the catalytic phase in contrast, the reaction is slow, even on the timescale of minutes. This description explains the observed “initial burst of O2”, the amount of which is not identical with “the total amount of O2 evolved in the Fenton reaction”. It represents only the amount of gas evolved during the rapid phase. To calculate its magnitude theoretically, the rate equations of Barb et al. were integrated numerically using their rate constants and the value of [O2] was determined at a point where both conditions v19/v20 < 10−3 and v21/v22 < 10−3 were satisfied [4]. The results have shown a definite dependence of this value on [H2O2]o (Ref. [11], Figure 3). It is concluded, therefore, that the existence of an upper limit in the amount of O2 evolved in the Fenton reaction during the initial burst at high [H2O2] has not been explained satisfactorily by the model of Barb et al [4].
A radical—radical reaction has also been suggested as the source of O2 [20].
HO2· + HO2· → O2 + H2O2
This reaction severs, however, the connection between O2 evolution and the regeneration of Fe2+, a phenomenon demonstrated experimentally (Ref. [4], p. 476). It is, therefore, unacceptable. The same applies also to the reaction
HO2· + OH· → O2 + H2O
This exhausts the possibilities of constructing mechanisms for the Fenton reaction based on free radicals.

6. Conclusions

There are three basic facts for which any mechanism of the Fenton reaction must account:
  • Change in the ratio of concentrations of the products when the ratio of concentrations of reactants is varied.
  • Coupling of the evolution of O2 with the regeneration of Fe2+.
  • The existence of an upper limit to the amount of O2 formed when [H2O2] is increased beyond a certain value.
    The mechanism of Haber and Weiss fails to explain all three points.
    The mechanism of Barb et al. explains points one and two but fails to explain point three [4].
    The nonradical mechanism explains all three points.

Funding

The author received financial support for the research, authorship, and/or publication of this article; the research was supported by a grant from the Hebrew University for Emeriti. The help of Miss Ronnie Kremer with the artwork in Figure 1 is greatly appreciated.

Conflicts of Interest

The author declare no conflict of interest.

References

  1. Pignatello, J.J.; Oliveros, E.; MacKay, A. Advanced oxidation processes for organic contaminant destruction based on the Fenton reaction and related chemistry. Crit. Rev. Environ. Sci. Tech. 2006, 36, 1–84. [Google Scholar] [CrossRef]
  2. Burkitt, M.J. Chemical, Biological and Medical Controversies Surrounding the Fenton Reaction. Prog. React. Kinet. Mech. 2003, 28, 75–104. [Google Scholar] [CrossRef]
  3. Haber, F.; Weiss, J. The catalytic decomposition of hydrogen peroxide by iron salts. J. Proc. R. Lond. Ser. A 1934, 147, 332–349. [Google Scholar]
  4. Barb, W.G.; Baxendale, J.H.; George, P.; Hargrave, K.R. Reactions of ferrous and ferric ions with hydrogen peroxide. Part 1–the ferrous\ ion reaction. Trans. Faraday Soc. 1951, 47, 462–500. [Google Scholar] [CrossRef]
  5. Bray, W.C.; Gorin, M.H. Ferryl ion, a compound of tetravalent iron. J. Am. Chem. Soc. 1932, 54, 2124–2125. [Google Scholar] [CrossRef]
  6. Walling, C. Fenton’s reagent revisited. Acc. Chem. Res. 1975, 8, 125–131. [Google Scholar] [CrossRef]
  7. Walling, C. Intermediates in the Reactions of Fenton Type Reagents. Acc. Chem. Res. 1998, 31, 155–157. [Google Scholar] [CrossRef]
  8. Goldstein, S.; Meyerstein, D.; Czapski, G. The Fenton Reagents. Free Radical Biol. Med. 1993, 15, 435–445. [Google Scholar] [CrossRef]
  9. Dunford, H.B. Oxidations of iron(II)/iron(III) by hydrogen peroxide from aquo to enzyme. Coord. Chem. Rev. 2002, 233–234, 311–318. [Google Scholar] [CrossRef]
  10. Kremer, M.L. Mechanism of the Fenton reaction. Evidence for a new intermediate. Phys. Chem. Chem. Phys. 1999, 1, 3595–3605. [Google Scholar] [CrossRef]
  11. Kremer, M.L. New kinetic analysis of the Fenton reaction: Critical examination of the free radical–chain reaction concept. Prog. React. Kinet. Mech. 2019, 44, 289–299. [Google Scholar] [CrossRef] [Green Version]
  12. Gallard, H.; de Laat, J.; Legube, B. Effect of pH on the Oxidation Rate of Organic Compounds by FeII/H2O2. Mechanisms and simulation. New J. Chem. 1998, 22, 263–268. [Google Scholar] [CrossRef]
  13. de Laat, J.; Gallard, H. Catalytic Decomposition of Hydrogen Peroxide by Fe(III) in Homogeneous Aqueous Solution: Mechanism and Kinetic Modeling. Environ. Sci. Technol. 1999, 33, 2726–2732. [Google Scholar] [CrossRef]
  14. Bossmann, S.H.; Oliveros, E.; Göb, S.; Siegwart, S.; Dahlen, E.P.; Payavan, L., Jr.; Straub, M.; Wörner, M.; Braun, A.M. New Evidence against Hydroxyl Radicals as Reactive Intermediates in the Thermal and Photochemically Enhanced Fenton Reactions. J. Phys. Chem. A 1998, 102, 5542–5550. [Google Scholar] [CrossRef]
  15. Buda, F.; Ensing, B.; Gribnau, M.C.M.; Baerends, E. DFT Study of the Active Intermediate in the Fenton Reaction. Chem. Eur. J. 2001, 7, 2775–2783. [Google Scholar] [CrossRef]
  16. Lu, H.F.; Chen, H.F.; Kao, C.L.; ChaO, I.; Chen, H.Y. A computational study of the Fenton reaction in different pH ranges. Phys. Chem. Chem. Phys. 2018, 20, 22890–22901. [Google Scholar] [CrossRef] [PubMed]
  17. Rush, J.D.; Koppenol, W.H. The reaction between ferrous polyaminocarboxylate complexes and hydrogen peroxide: An investigation of the reaction intermediates by stopped flow spectrophotometry. J. Inorg. Biochem. 1987, 29, 199–215. [Google Scholar] [CrossRef]
  18. Masarwa, A.; Rachmilowich-Calis, S.; Meyerstein, N.; Meyerstein, D. Oxidation of organic substrates in aerated aqueous solutions by the Fenton reagent. Coord. Chem. Rev. 2005, 249, 1937–1943. [Google Scholar] [CrossRef]
  19. Kremer, M.L. Strong inhibition of the Fe3+ + H2O2 reaction by ethanol: Evidence against the free radical theory. Prog. React. Kinet. Mech. 2017, 42, 397–413. [Google Scholar] [CrossRef]
  20. Perez-Benito, J.F. Iron (III)–Hydrogen Peroxide Reaction: Kinetic Evidence for a Hydroxyl–Mediated Chain Mechanism. J. Phys. Chem. A 2004, 108, 4853–4858. [Google Scholar] [CrossRef]
Figure 1. The nonradical mechanism.
Figure 1. The nonradical mechanism.
Reactions 02 00019 g001
Figure 2. Simulated evolution of O2 in the Fenton reaction.
Figure 2. Simulated evolution of O2 in the Fenton reaction.
Reactions 02 00019 g002
Figure 3. Simulated and experimental limiting values of [O2], Simulated values (circles), experimental values (triangles). [H2O2]o = 0.5, 1, 1.5, 2, 2.5, 3, 3.5 mol dm−3. Other parameters as in Figure 2.
Figure 3. Simulated and experimental limiting values of [O2], Simulated values (circles), experimental values (triangles). [H2O2]o = 0.5, 1, 1.5, 2, 2.5, 3, 3.5 mol dm−3. Other parameters as in Figure 2.
Reactions 02 00019 g003
Figure 4. R terms as functions of time. R1 (circles), R2 (squares), R3 (triangles) [H2O2]o = 2 mol dm−3. Other parameters as in Figure 2.
Figure 4. R terms as functions of time. R1 (circles), R2 (squares), R3 (triangles) [H2O2]o = 2 mol dm−3. Other parameters as in Figure 2.
Reactions 02 00019 g004
Figure 5. Kinetics of [C1] and [C2] in the early phase. [C1] (triangles), [C2] (squares); [H2O2]o = 0.5 mol dm−3 (empty symbols); [H2O2]o = 3.5 mol dm−3 (full symbols). Other parameters as in Figure 2.
Figure 5. Kinetics of [C1] and [C2] in the early phase. [C1] (triangles), [C2] (squares); [H2O2]o = 0.5 mol dm−3 (empty symbols); [H2O2]o = 3.5 mol dm−3 (full symbols). Other parameters as in Figure 2.
Reactions 02 00019 g005
Figure 6. Rate of O2 evolution in the early phase. [H2O2]o = 0.5 mol dm−3 (empty triangles); [H2O2]o = 3.5 mol dm−3 (full triangles). Other parameters as in Figure 2.
Figure 6. Rate of O2 evolution in the early phase. [H2O2]o = 0.5 mol dm−3 (empty triangles); [H2O2]o = 3.5 mol dm−3 (full triangles). Other parameters as in Figure 2.
Reactions 02 00019 g006
Figure 7. Resolution of the rate of O2 evolution into H2O2 and Fe3+ dependent components. v4 (empty triangles); v6 (full squares); vO2 (full triangles); [H2O2]o = 2 mol dm−3; Other parameters as in Figure 2.
Figure 7. Resolution of the rate of O2 evolution into H2O2 and Fe3+ dependent components. v4 (empty triangles); v6 (full squares); vO2 (full triangles); [H2O2]o = 2 mol dm−3; Other parameters as in Figure 2.
Reactions 02 00019 g007
Table 1. Simulated and experimental values of [O2] evolved in 5 s.
Table 1. Simulated and experimental values of [O2] evolved in 5 s.
[O2]exp
mol dm−3
[O2]sim
mol dm−3
[H2O2]o
mol dm−3
1.40 × 10−21.41 × 10−20.5
1.40 × 10−21.38 × 10−2 1
----- 1.40 × 10−21.5
1.40 × 10−21.41 × 10−22
----- 1.41 × 10−22.5
----- 1.40 × 10−23
1.37 × 10−21.39 × 10−23.5
Standard deviation of 31 values of [O2]sim from 1.40 × 10−2 mol dm−3 (target) = 1.38 × 10−4 mol dm−3. Values of [O2]exp from the work of Barb et al. ([Fe2+]o = 4.00 × 10−2 mol dm−3, T = 0 °C, pH = 1.8, Ref. [4], Figure 6).
Publisher’s Note: MDPI stays neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Share and Cite

MDPI and ACS Style

Kremer, M.L. An Upper Limit to O2 Evolution as Test for Radical and Nonradical Mechanisms for the Fenton Reaction. Reactions 2021, 2, 301-311. https://doi.org/10.3390/reactions2030019

AMA Style

Kremer ML. An Upper Limit to O2 Evolution as Test for Radical and Nonradical Mechanisms for the Fenton Reaction. Reactions. 2021; 2(3):301-311. https://doi.org/10.3390/reactions2030019

Chicago/Turabian Style

Kremer, Mordechai L. 2021. "An Upper Limit to O2 Evolution as Test for Radical and Nonradical Mechanisms for the Fenton Reaction" Reactions 2, no. 3: 301-311. https://doi.org/10.3390/reactions2030019

Article Metrics

Back to TopTop