Tom M.
Nolte‡
*ab,
Thomas
Nauser
b and
Lorenz
Gubler
a
aElectrochemistry Laboratory, Paul Scherrer Institut, 5232 Villigen PSI, Switzerland. E-mail: t.nolte@science.ru.nl
bEidgenössische Technische Hochschule (ETH) Zurich, Laboratory of Inorganic Chemistry, Vladimir-Prelog-Weg 1, 8093 Zurich, Switzerland
First published on 23rd December 2019
Both synthetic polymers (membranes, coatings, packaging) and natural polymers (DNA, proteins) are subject to radical-initiated degradation. In order to mitigate the deterioration of the polymer properties, antioxidant strategies need to be devised. We studied the reactions of poly(α-methylstyrene sulfonate), a model compound for fuel cell membrane materials, with different degrees of polymerization with OH˙ radicals as well as subsequent reactions. We observed the resulting OH˙-adducts to react with oxygen and eliminate H2O, the relative likelihood of which is determined by pH and molecular weight. The resulting radical cations can be reduced back to the parent molecule by cerium(III). This ‘repair’ reaction is also dependent on molecular weight likely because of intramolecular stabilization. The results from this study provide a starting point for the development of new hydrocarbon-based ionomer materials for fuel cells that are more resistant to radical induced degradation through the detoxification of intermediates via damage transfer and repair pathways. Furthermore, a more fundamental understanding of the mechanisms behind conventional antioxidants in medicine, such as ceria nanoparticles, is achieved.
The hydroxyl radical (HO˙) can be particularly detrimental to the polymer as it initiates degradation. HO˙ reacts with aromatic compounds with typical rate constants in the range of the diffusion limit of 109–1010 M−1 s−1.3,4 However, the nature of follow-up reactions, intermediates and the associated kinetics are rarely considered. The final result of HO˙ attack may be chain oxidation (e.g., hydroxylation), crosslinking, or chain fragmentation.5 These different mechanisms of polymer aging depend on the chemistry of the polymer. Thus, strategies to prevent aging ought to take these pathways into account (Fig. 1). For example, ‘repairing’ intermediates formed upon radical attack may be accomplished with suitable additives, i.e., antioxidants (e.g. in Fig. 1, reaction 11).6
There is an analogy to oxidative stress in living cells: here, it is the characteristic of imbalance between reactive oxygen species (ROS) generation and an organism's endogenous defenses. OH˙ is generated from ‘leakage’ of electrons along the cellular electron transport chain, and can react with cell constituents (DNA, proteins). As a consequence, oxidative stress is the basis of many serious diseases such as cancer. Nature has its way of detoxifying radicals, i.e., using vitamins and enzymes. When these endogenous mechanisms to combat oxidative stress fall short, we can consider treatment via synthetic alternatives. Ceria nanoparticles (CNPs) are promising inorganic antioxidants for many biomedical applications. CNPs have demonstrated antioxidant enzyme-mimetic activity, as well as the capacity to scavenge a variety of ROS in both cell and animal models. Concomitantly, a reduction in DNA damage (e.g. in lung cells) has been observed.7 Cerium ions or ceria particles are also used to mitigate degradation in PFSA-type fuel cell membranes8via direct scavenging of OH˙, and potentially H˙:9,10
Ce3+ + HO˙ + H+ → Ce4+ + H2O (k1 = 3 × 108 M−1 s−1![]() | (1) |
The antioxidant properties of CNPs are dependent, also, on the ability to undergo redox cycling between the valences Ce3+ and Ce4+ ions (as CeO2−δ) on the surface of CeO2 or Ce2O3 CNPs in aqueous solution.11 Radical scavenging by Ce3+ is very effective in PFSA membranes, because the lifetime of HO˙ is on the order of microseconds, thus with a relatively small concentration of Ce3+ of ∼0.1 M over 90% of HO˙ are quenched.5 The ratio of Ce4+ to Ce3+ is influenced by the chemistry of the medium. For example, H2O2 and HO2˙, which are also present in a fuel cell membrane,12 can reduce Ce4+ to Ce3+:13
Ce4+ + H2O2 → Ce3+ + HO2˙ + H+ (k2 = 1 × 106 M−1 s−1![]() | (2) |
Ce4+ + HO2˙ → Ce3+ + O2 + H+ (k3 = 2.7 × 106 M−1 s−1![]() | (3) |
An intermediate formed as a result of OH˙ attack on arylenes is the aromatic radical cation (Ar˙+) (compound E, Fig. 1), produced by acid-catalyzed elimination of H2O (reaction 9, Fig. 1) from the OH-adduct (compound B, Fig. 1).15,16 Since proton exchange membrane fuel cells operate under acidic conditions, elimination of H2O is usually fast.15–17 The redox potential E° of Ce4+/Ce3+ of 1.44 V18 is favorable as compared to E°(Ar˙+/Ar) = 2.0–2.4 V.19 In previous work using poly(α-methylstyrene sulfonate) (PAMSS) oligomers as model aromatic compound, we found that the lifetime of the radical cation increases with the degree of polymerization, potentially due to π–π interactions, and does not produce benzyl radicals due to the presence of the α-methyl group.20 PAMSS is well soluble in water making it a viable candidate to study the kinetics of its reaction with Ce3+ in aquo. PAMSS represents a constituent of a fuel cell membrane. Though other model compounds representing polyarylene type polymers (e.g. polysulfones) are conceivable, they are beyond the current scope.
In the work reported here, we studied the interaction (reaction 11, Fig. 1) between Ce3+ and the aromatic radical cation of PAMSS (compound E) to investigate whether cerium could function as a regenerative antioxidant for repairing aryl-type polymers. To determine whether the repair pathway is viable we compared the regeneration kinetics with a potential side reaction, prominently, the reaction of the HO-adduct (compound B) with O2 (reactions 7/−7 and 8, Fig. 1). The degree of polymerization of PAMSS was varied from 1 to 1700 in order to study the effect of Ar˙+ lifetime and redox properties. The results of this study are of high relevance to material scientists and engineers looking to improve the durability of hydrocarbon based fuel cell membranes, as well as for medicinists aiming to elucidate and optimize antioxidant mechanisms.
N2O + eaq− + H2O → N2 + OH˙ + OH− (k4 = 9.1 × 109 M−1 s−1![]() | (4) |
OH˙ + PAMSS → PAMSS(–OH)˙ (k5) | (5) |
PAMSS radicals have relatively low extinction coefficients and side-reactions might be involved at high concentrations of radicals. To bypass and minimize this, we studied the reaction with OH˙ via competition with Fe(CN)64−:
OH˙ + Fe(CN)64− → OH− + Fe(CN)63− (k6 = 1.05 × 1010 M−1 s−1) | (6) |
At relatively low dose (∼10 Gy), the concentration of Fe(CN)64− was ∼50 μM and the concentration of PAMSS was varied. Under N2O saturated conditions the radiation chemical yield (G) of OH˙ is ∼5.6 × 10−7 mol J−1 and is unaffected by the PAMSS concentration (dilute solutions, ≤100 μM). Thereby, the absorbance at 420 nm (Fe(CN)63−, ε420 = 1040 M−1 cm−1) is solely affected by the PAMSS concentration via competition for OH˙. The absorption at 420 nm, virtually constant after ∼5 μs, was measured.
Control experiments were performed using different dose/Fe(CN)64− ratios, as well as direct observation (details in the ESI†).
PAMSS(–OH)˙ + O2 ⇌ PAMSS(–OH)(–O2)˙ (k7/k−7) | (7) |
The addition of O2 to hydroxycyclohexadienyl radicals was studied by varying the O2 concentration, and observing the effect on the kinetic trace of hydroxycyclohexadienyl radicals. Mixtures of N2O/O2 were used and the concentration of O2 in the samples was determined via the partial pressure of O2 and its solubility in water (1.25 mM at 1.0 atm). O2 concentrations ranged from 0 to 1.25 mM. Doses applied were ∼40 Gy. All experiments reported were reproduced at least five times.
The characteristic λmax for hydroxycyclohexadienyl-type radicals is ∼325 nm, Fig. 2. However, other species, among which the Ar–OH(–O2) radical adduct, absorbs also in this spectral range (Fig. 2B). Moreover, the addition of oxygen is reversible25 with an equilibrium constant K on the order of ≥103 M−1,25 because the reverse reaction is relatively slow (reaction −7, Fig. 1, with k−7 = 4.5(±0.9) × 103 s−1 as an upper limit for poly(styrene sulfonate) (PSS)26).
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Fig. 2 (A) Spectrum of 5 μM poly(α-methylstyrene sulfonate) Mw = 354![]() ![]() |
The addition reaction was monitored at λ = 360 nm, chosen empirically such that both the relative absorption of the OH˙-adduct (relative to the Ar–OH(–O2) adduct) and absolute absorption are maximized (Fig. S4B, ESI†). Based on earlier results25,26 we identified the decay within ∼10–20 μs of the absorption maximum. The kinetic traces were fitted with pseudo-first order functions. This analytical setup minimized the need of fitting to equilibria or taking into account side reactions, such as ˙OOH elimination (reaction 8, Fig. 1, with k8 = 2.7(±0.3) × 103 s−1 for PSS18) to form a stable hydroxylated product (compound D). Thus, we can fit kinetic traces for the OH˙-adduct with minimal interference.25
Control experiments were performed using gas mixtures of Argon/O2 and N2O/O2 under low doses (∼10 Gy) to characterize the relevance of the yield of OH-adducts (details in Fig. S8, ESI†) on the apparent rate constants.
Rate constants for the elimination of OH−/H2O have previously been identified as ∼104 s−1 for a range of aryl-type OH˙-adducts,16 whereas for the reaction between radical cation and H2O (reaction −9, Fig. 1) values differ 101–10716 (k−9 = 1–2 × 104 s−1, Fig. 5 and Fig. S10–S12, ESI†). Thus, simultaneous production of radical cations via elimination (reaction 9, Fig. 1) from the PAMSS-OH˙ adduct (Fig. 2A) might obscure the depletion via reaction with Ce3+ (reaction 11, Fig. 1).
Bypassing the H2O/OH− elimination from PAMSS-OH˙ route, radical cations were produced by electron transfer to sulfate radicals (reaction 10, Fig. 1):
PAMSS + SO4˙− → PAMSS˙+ + SO42− (k10 = 0.6–1.0 × 109 M−1 s−1![]() | (8) |
Potassium peroxodisulfatesulfate (50 mM) was added to argon-saturated solutions at pH ∼ 2 (adjusted with H2SO4). Dose was ∼100 Gy, and tBuOH (100 mM) was added to scavenge the primary OH˙ radicals. Concentrations of PAMSS were used according to the degree of polymerization (e.g. 4.5 mM for PAMSS-354000). We varied the Ce3+ concentration to obtain pseudo first-order rate constants for the reaction:
Ce3+ + PAMSS˙+ → Ce4+ + PAMSS (k11) | (9) |
Polydispersity index | Molecular weight, Mw (Da) | k 5 (M−1 s−1) | k 5/nd | Source |
---|---|---|---|---|
a 4-tert-Butyl-benzenesulfonate.
b Using a Fe(CN)63−![]() ![]() ![]() ![]() ![]() ![]() ![]() ![]() |
||||
1 | 214a | 4.9(±0.1) × 109![]() |
4.9(±0.1) × 109 | This work, c.k. |
<1.5 | 2660 | 1.3(±0.2) × 1010![]() |
9.4 × 108 | This work, c.k. |
n/a | 2640 | 2.0 × 1010 | 1.5 × 109 | Dockheer et al.c![]() |
n/a | 6400 | 2.5(±0.5) × 1010 | 7.7 × 108 | Dockheer et al.c![]() |
<1.2 | 14![]() |
2.8(±0.2) × 1010![]() |
3.8 × 108 | This work, c.k. |
<1.2 | 73![]() |
9.4(±0.3) × 1010![]() |
2.5 × 108 | This work, c.k. |
<1.2 | 354![]() |
5.7(±0.2) × 1011![]() |
3.2 × 108 | This work, c.k. |
<1.2 | 354![]() |
5.8(±0.3) × 1011 | 3.2 × 108 | This work, direct obs. |
The apparent yield of adducts (absorption at 360 nm) under N2O atmosphere is less than twice that obtained under O2 (3.2 and 5.9 abs Gy−1, resp.), i.e. G(N2O)/G(O2)= 1.86 ± 0.04 (Fig. 4A). The ratio in yields of the primary radicals, G(OH˙, N2O) + G(H˙, N2O) = 0.622 and G(OH˙, O2) + G(H˙, O2) = 0.342, i.e. G(N2O)/G(O2) = 1.82, is similar. We infer that the absorption corresponds to 5–10% PAMSS-H˙ adducts. Nevertheless, measurement of k5via direct observation produced the same value as obtained via competition kinetics (Table 1), Fig. S1 (ESI†). The suite of control studies indicated the stability of the method (Table 1).
We obtained larger values for k5 for larger molecular weights. However, when we express k5 per monomer unit, there is a notable decrease. The data match earlier observations by, e.g., Dockheer et al.20 for a more limited range of Mw (Table 1); we find our values either slightly lower or equal to what has been reported.
The influence of size could be expressed as k5 ∼ [n]0.60±0.08 (k5 ∼ [n]0.57 including Dockheer et al. data,20Fig. 6), wherein [n] is the degree of polymerization. Variation in the polydispersity index (PDI) between the polymers is not expected to influence the relationships obtained in this study (since PDI < 1.2). The “reaction exponent”, here 0.60 ± 0.08, is sometimes defined as θ:27,28
![]() | (10) |
In case the polymer dynamics are ‘Rouse-like’ (single un-entangled chain; no significant interactions between chain segments) z = 4. In turn, g = 0 represents a non-interacting electron–electron system (the correlation hole29 is screened out). Then, the reaction exponent is (3 + 0)/4 = 0.75. Indeed, k5 values are near the “diffusion control”: k5 ∼ [n]0.60, i.e. 0.60 ± 0.08 ≲ 0.75. Thus, kr is largely independent of the reactivity of the reaction site.
A neighboring monomer might interact with the radical site in such a way that its intrinsic reactivity is lowered, or the coiling of the polymer chain may decrease its accessibility. Values for propagation in radical polymerisations are typically 103±1 M−1 s−1,30i.e. slow due to steric crowding about the radical center. Based on this, we consider the value 5(±1) × 102 M−1 s−1 to correspond to reaction 12 (crosslinking and/or disproportionation, k12) in Fig. 1.
Protonation of OH˙-adducts occurs with a rate constant of k = 1–2 × 109 M−1 s−116 implying a pseudo 1st order rate constant of 1–2 × 102 s−1 at pH 7, whereas the elimination of OH− occurs with a rate on the order ∼104 s−1 for a range of aryl-type OH˙-adduct monomers.16 Thus, the value of 2.2(±0.5) × 103 s−1 might characterize reaction 9 (either elimination of OH− or acid-catalysed elimination of H2O, k9) of PAMSS-14
600(–OH˙) as denoted in Fig. 1, reaction 9/−9.
The yield of OH˙-adducts varied for different ratios of N2O/O2 and between pulses (Fig. 4A); the concentration of OH˙-adducts under N2O/O2 mixtures was directly proportional to the yield of OH˙, see Fig. 4A and Fig. S7 (ESI†). This was taken into account when evaluating the pseudo-first order reaction with O2 (reaction 7, Fig. 1):24 we consider the relative concentrations of OH˙-adducts. Thus, Fig. 4A was corrected for the adduct yields (maximum absorbance, at ∼2 μs), to give Fig. 4B.
Control studies indicated the stability of the method (Fig. S8, ESI†): H˙ is quenched by PAMSS, rather than O2. There is no difference between the k7 values obtained from series under argon or N2O. Therefore, PAMSS-14600(–H˙) adducts react slower with O2 than do PAMSS-14
600(–OH˙) adducts and do not contribute significantly to the result. Different initial yields of PAMSS-14
600(–OH˙) adducts (at t = 2 μs), do not appear to affect the results (Fig. 4C and Fig. S8, ESI†). Thus, in the range of 2 μs to 10–20 μs, there is no measurable equilibration or elimination of OOH˙ yet. Compared to 1.25 × 10−3 M for O2 (in O2 saturated solutions), the experimental series may also yield superoxide, O2˙− (Fig. S8-1A, ESI†), in 10 μM (higher-end estimation). In O2 saturated solutions (∼1.25 mM) G(OH˙) ∼ 2.8 × 10−7 mol J−1 and G(O2˙−) ∼ 3.4 × 10−7 mol J−1. The reaction between PAMSS-OH and O2 is thermodynamically favored (compared to that with O2˙−) based on the energies of their frontier orbitals:31 |ESOMO(O2) − ESOMO(PAMSS-OH˙)| < |ESOMO(O2˙−) − ESOMO(PAMSS-OH˙)|, i.e. ΔE ∼ 0.4 eV < ΔE ∼ 0.9 eV (in-house calculation32–34). The influence of O2˙− has not been reported in related studies (under high O2 concentrations25). Thus, the reaction between O2˙− and PAMSS-OH is of minor importance, and the rate constants for addition of O2 obtained in this study can be considered accurate.
From fitting we obtained a rate constant k7 = 4.8(±0.4) × 106 M−1 s−1 for the reaction between PAMSS-14600(−OH˙) and O2 (see ESI† for other Mw) in Fig. 4C. The reaction of a carbon-centered radical with O2 to form the corresponding peroxyl radical generally proceeds with a rate constant on the order of 109 M−1 s−1.35 However, because of electron delocalization in allylic and dienylic C-centered radicals, oxygen binds relatively weakly, which results in slower and reversible O2 addition. These notions are in agreement with the data obtained. Other factors explaining the relatively low rate constants include steric hindrance (tert-butyl) and polarity (sulfate) but need to be studied in more detail.
There appeared to be an influence of molecular weight, as a k7 of 2.2(±0.3) × 107 M−1 s−1 was found for the 4-tert-butyl-benzenesulfonate (–OH˙) adduct. The data are in the same order as was found for PSS-1100(–OH˙): k = 3.0(±0.5) × 107.26 For the reaction between the OH˙-adducts and O2, k7 scales with n: k7 ∼ [n]−0.26±0.07. PSS data26 might be included in the analysis if no significant influence by the extra methyl group is expected on the reaction thermochemistry, relative to the effect of Mw (Fig. 6). The influence of polymer size on the reaction between PAMSS(–OH˙) and O2 (−0.26 ± 0.07) is different (2σ) from for the reaction between PAMSS and OH˙ (0.60 ± 0.08). Since there is only 1 reactive site on the polymer, no relationship with n (k7 ∼ [n]0) should be expected if diffusive or quantum-chemical effects are absent. Instead, the polymer dynamics i.e. diffusive pathway (z) and/or quantum-chemical properties (g) (eqn (10)) are affected (<0) by the breaking of aromaticity by OH˙ to produce the hydroxycyclohexadienyl radical. It is worth noting that hydroxycyclohexadienyl radicals are relatively electron-rich and non-planar (Fig. 1, compound B), which would disfavor π–π interaction.
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Fig. 5 (A and B) Kinetic traces for PAMSS-354![]() ![]() ![]() ![]() |
The radical cations showed longer lifetimes upon increasing the molecular weight of the polymer (Fig. 6 and Fig. S10 and S11, ESI†), with reaction exponents (k ∼ [n]0.09±0.03) similar to those for the reaction between the radical cation and Ce3+ (0.12 ± 0.01). Extrapolation of the data recorded in absence of O2 (under Ar), using a power function in Fig. 6 results in k = 1.6 × 104 s−1 for the first-order decay of the 4-tert-butylbenzenesulfonate radical cation (∼40 μs half-life). This is relatively low compared to simple arenes, or even tert-butyl-benzene cations (105–106 s−116). The mode of decay by the radical cations is uncertain. The α-methyl group prevents formation of a benzyl radical via a proton elimination (splitting) reaction and, instead, elimination of the sulfate was suggested20 or dealkylation (scission), Fig. 1. The cation might react intramolecularly with a nearby monomer,16 requiring a k of 106–107 s−1. This is unlikely based on thermodynamic grounds, and it would likely result a shift in λmax (for a similar radical cation), which was not observed. A radical–radical reaction would involve rate constants in the range of 108–109 M−1 s−1 (diffusion-limited, no thermodynamic arguments). This mechanism does not explain the size dependence observed and the decay that is still observed at very low concentrations, ∼104 s−1. Rate constants for addition of H2O to the radical cation (i.e. the backward reaction −9, Fig. 1) to form the water adduct are on the order of 102–103 M−1 s−1.16 The decay observed in acidic aqueous solution is given by k = 6 × 103–6 × 104 s−1. Addition of H2O to the radical cation would occur via direction of the lone pair into the SOMO of the radical cation. The cation, and by extension the energy of this SOMO, could be subject to intramolecular π–π interaction. As a result, the interaction can lower the rate of H2O addition. Taking the molar concentration of H2O for a dilute solution, k−9 would be 2(±1) × 106 M−1 s−1.
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Fig. 6 Combined results for the reactions studied. Rate constants are plotted versus the degree of polymerisation, [n]. Literature data refer to Behar (1991),37 Behar and Rabani (1988),38 Bhardwaj et al. (2001)39 and Dockheer et al. (2010)26 for PSS and PAMSS, as well as control experiments. ‘Reaction exponents’: θ = 0.60 ± 0.08 for PAMSS + OH˙, θ = −0.12 ± 0.01 for PAMSS˙+ + Ce3+, θ = −0.26 ± 0.07 for PAMSS(−OH˙) + O2, and θ = −0.09 ± 0.02 for the first order decay of PAMSS˙+. |
As a validation exercise, experiments were conducted for a lower PAMSS (73800) and higher persulfate concentrations, as well as under higher pH (Fig. S12, ESI†). The same value for k11 was obtained for the series when fitting the kinetic traces over a short time regime, indicating the stability of the method. Nevertheless, the observed rate constants are higher at pH ∼ 3, as compared to pH ∼ 2. An offset of 2.9(±0.2) × 104 s−1 between regressions for pH ∼ 3 and pH ∼ 2 was obtained. The offset is partially attributed to the acid–base equilibrium (reaction, 9/−9, Fig. 1) (see previous section).
The influence of molecular weight on the reaction between the PAMSS radical cation and Ce3+ was considered. The ‘reaction exponent’ is −0.12 ± 0.01, i.e. k11 ∼ [n]−0.12±0.01. The value is similar to that observed for the reaction between the radical cation and H2O (previous section), −0.09 (Fig. 6). The negative values support the interpretation that the thermochemistry of the radical cation is affected intramolecularly. Intramolecular charge–radical stabilization has already been confirmed on a fundamental level: chemical reactivity is controlled by radicals flanking the charged groups or by charged groups flanking the radicals.36 For the radical cations, too, a significant stabilization is implied, which may be expressed as θ < 0, eqn (10). The radical cation is initially produced on the outer ‘surface’ of the polymer coil with a high degree of polymerization (diffusion limited). Quantum-chemical stabilization (g, eqn (10)) can be a π-donation into the outer-surface cation hole (i.e. the electron deficiency), effectively delocalizing (transferring) the cation hole to center of the polymer. It is conceivable that the polymer dynamics (z, eqn (10)) are also affected, for example, through bridging between polymer segments to facilitate radical stabilization.
Extrapolation of the data resulted in k11 = 6.4(±0.7) × 108 M−1 s−1 for the reaction between 4-tert-butyl-benzenesulfonate radical cation and Ce3+ (Fig. 6). No literature data could be found for reactions of Ce3+ with aromatic radical cations. However, the ferrous ion (Fe2+) reacts with (reduces) the radical cation of anisole with a rate constant of k = 6 × 108 M−1 s−1 (pH 1.0) and with pseudocumene and isodurene radical cations with k = 6(±1)107 M−1 s−1 (pH 2.5–3.5).16 These reactions are dependent on the ionic strength of the solution and, potentially, the polarity of the cation (Nolte et al., in prep.).32
The results of this study show that repair and stabilization of polymeric radicals can be achieved using cerium ions and neighboring groups via suitable thermochemical and kinetic interactions. This has ramifications for the design of durable arylene type fuel cell membranes and polymeric materials in general. The results also provide a basis for more fundamentally understanding the mechanisms behind conventional antioxidants in medicine, such as ceria nanoparticles, and represent a starting point for improvement of additives that detoxify radicals or intermediates formed therefrom, e.g., via damage transfer or repair pathways.
Footnotes |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c9cp05454e |
‡ Current address: Department of Environmental Science, Institute for Water and Wetland Research, Radboud University Nijmegen, 6500 GL Nijmegen, The Netherlands. |
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