Significance
Aromatic hydrocarbons account for 20 to 30% of volatile organic compounds and contribute importantly to ozone and secondary organic aerosol (SOA) formation in urban environments. The oxidation of toluene, the most abundant aromatic compound, is believed to occur mainly via OH addition, primary organic peroxy radical (RO2) formation, and ring cleavage, leading to ozone and SOA. From combined experimental and theoretical studies, we show that cresol formation is dominant, while primary RO2 production is negligible. Our work reveals that the formation and subsequent reactions of cresols regulate the atmospheric impacts of toluene oxidation, suggesting that its representation in current atmospheric models should be reassessed for accurate determination of ozone and SOA formation. The results from our study provide important constraints and guidance for future modeling studies.
Keywords: aromatics, oxidation, ozone, secondary organic aerosol, air pollution
Abstract
Photochemical oxidation of aromatic hydrocarbons leads to tropospheric ozone and secondary organic aerosol (SOA) formation, with profound implications for air quality, human health, and climate. Toluene is the most abundant aromatic compound under urban environments, but its detailed chemical oxidation mechanism remains uncertain. From combined laboratory experiments and quantum chemical calculations, we show a toluene oxidation mechanism that is different from the one adopted in current atmospheric models. Our experimental work indicates a larger-than-expected branching ratio for cresols, but a negligible formation of ring-opening products (e.g., methylglyoxal). Quantum chemical calculations also demonstrate that cresols are much more stable than their corresponding peroxy radicals, and, for the most favorable OH (ortho) addition, the pathway of H extraction by O2 to form the cresol proceeds with a smaller barrier than O2 addition to form the peroxy radical. Our results reveal that phenolic (rather than peroxy radical) formation represents the dominant pathway for toluene oxidation, highlighting the necessity to reassess its role in ozone and SOA formation in the atmosphere.
Toluene is the most abundant aromatic hydrocarbon in the atmosphere and is emitted primarily from anthropogenic sources, i.e., from automobiles and industrial activities. Photochemical oxidation of toluene plays an important role in tropospheric ozone and secondary organic aerosol (SOA) formation, profoundly impacting air quality, human health, and climate (1–8). However, the detailed chemical mechanism of toluene oxidation in the atmosphere remains uncertain (4, 5). Oxidation of toluene is initiated by the hydroxyl radical (OH): the initial OH−toluene reaction results in minor H abstraction (about 10%) and major OH addition (about 90%) (9–20). The H-abstraction pathway leads to the formation of benzaldehyde, whose oxidative pathway is well established (4, 5). The OH addition pathway results in the formation of methylhydroxycyclohexadienyl radicals (the OH−toluene adducts), which subsequently react with O2 via three plausible pathways (Fig. 1), i.e., H abstraction to yield phenolic compounds and hydroperoxy radicals (HO2) (pathway I), O2 addition to form primary peroxy radicals or RO2 (pathway II), and H abstraction and subsequent O-bridge formation to aromatic oxide/oxepin (pathway III). Previous theoretical studies have suggested that the primary RO2 cyclizes to form bicyclic radicals, rather than reacting with NO to form alkoxy radicals under atmospheric conditions (16). The bicyclic radicals then undergo unimolecular rearrangement, followed by H abstraction, to form epoxide intermediates or react with O2 to form secondary RO2, followed by ring cleavage to produce small α-carbonyl compounds such as glyoxal and methylglyoxal (16, 21). The toluene−oxide/methyloxepin channel remains speculative, and several previous quantum chemical calculations have shown a high barrier for this pathway (22–26). Numerous experimental studies have been performed to investigate the products from the OH−toluene reactions (2–5, 18, 27). For example, previous studies have reported a highly variable yield of cresols (11, 12, 15, 18, 19, 27), ranging from 9.0 to 52.9%. In addition, the yields of glyoxal and methylglyoxal determined from the previous studies are also conflicting, ranging from <4% to about 39% for glyoxal and <4 to 17% for methylglyoxal (12, 13, 18). From an atmospheric modeling perspective (2–5), ozone formation from toluene oxidation is conventionally assumed with a large (65%) contribution from the production of RO2 (pathway II) and a minor (18%) contribution from HO2 formed with cresols (pathway I). Both RO2 and HO2 generated react with nitric oxide (NO) to yield nitrogen dioxide (NO2), which subsequently undergoes photodissociation to lead to ozone formation. In addition, aromatic ring cleavage from the primary RO2 and cresol pathways (pathways I and II) results in several products, including glyoxal, methylglyoxal, and low-volatility compounds that likely contribute to SOA formation (1–3, 8, 28–33).
Fig. 1.
Competing oxidative pathways of the ortho OH−toluene adduct: (pathway I) H abstraction to o-cresol, (pathway II) O2 additiion to form primary o-RO2 and subsequent ring cleavage to form glyoxal and methylglyoxal, and (pathway III) H abstraction followed by O-bridge formation to 1,2-toluene oxide. The chemical mechanism currently adopted in atmospheric models (5) assumes a dominant primary RO2 production (pathway II) but a minor cresol formation (pathway I).
In this study, we evaluated the detailed oxidation mechanism of the OH−toluene reactions by combining direct experimental measurements and quantum chemical and kinetic rate calculations, to improve the understanding of the pathways leading to ozone and SOA formation in the atmosphere.
Results
Fig. 2A depicts a mass spectrum (m/z = 95 to 135) of the OH−toluene reactions in the presence of O2 and NO under our typical experimental conditions (SI Appendix, Fig. S1 and Table S1). The peaks at m/z = 107 and 109 correspond to protonated benzaldehyde (C7H7O+) and cresols (C7H9O+), respectively. The peak at m/z = 125 is attributed to dihydroxymethylbenzenes (C7H9O2+), corresponding to the secondary products from the subsequent oxidation of cresols initiated by OH (33), to be discussed below. Although the oxide/methyloxepin intermediates correspond to the same molecular weight (MW) as cresols, their formation is excluded because of a large activation barrier for this pathway (16). Fig. 2B displays single-ion monitoring of the three products, i.e., benzaldehyde, cresols, and dihydroxymethylbenzenes, versus consumed toluene. The ion−molecule reaction rate constants calculated using the average dipole orientation (ADO) theory (34–36) are 4.1 × 10−9 cm3·molecule−1·s−1, 2.5 × 10−9 cm3·molecule−1·s−1, 3.6 × 10−9 cm3·molecule−1·s−1, and 2.1 × 10−9 cm3·molecule−1·s−1 for benzaldehyde, cresols (averaged over o-, p-, and m-cresol), dihydroxymethylbenzenes (averaged over 1,2-dihydroxy-3-methylbenzene and 1,2-dihydroxy-4-methylbenzene), and toluene, respectively. The yields of those products are quantified to be (11.3 ± 2.0)% for benzaldehyde, (39.0 ± 5.0)% for cresols, and (8.9 ± 1.3)% for dihydroxymethylbenzenes. Table 1 summarizes our measured product yields, along with comparison with the previous studies.
Fig. 2.
Detection and quantification of products from OH-initiated oxidation of toluene. (A) Mass spectral scan (m/z = 95 to 135) of the OH−toluene reactions under a typical experimental condition. (B) Plot of ktol/kprod × ∆Sprod versus ∆Stol. The slope of the line corresponds to the product yield.
Table 1.
Product yields from OH-initiated oxidation of toluene in the presence of O2 and NO
Product yield | ||
Product | Previous work | This work* |
Benzaldehyde (MW = 106) | 11†, 5.3‡, 6.0§, 4.9¶, 5.8#, 6.5‖ | 11.3 ± 2.0 |
Cresols (MW = 108) | 52.9‡, 15.3§, 28.1¶, 17.9#, 17.2**, 25.2‖ | 39.0 ± 5.0 |
Dihydroxymethyl-benzenes (MW = 124) | 8.9 ± 1.3 | |
MW = 96 (unidentified) | ∼5 | |
Glyoxal (MW = 58) | 9.8†, 4.1‡, 23.8§, 39.0†† | |
Methylglyoxal (MW = 72) | 10.6†, 5.5‡, 16.7§, < 4%¶ | <2 |
Epoxides (MW = 140) | 7.2¶ | <1 |
The yield represents the sum of all isomers, if applicable. Each value represents an average of more than 15 measurements at various experimental conditions (SI Appendix, Table S1). The uncertainty reflects both random error due to data scattering and systematic error related to the ion−molecule rate constants and possible fragmentation of the proton transfer reactions. Experimental conditions: [toluene] = (0.2 to 2) × 1012 molecules·cm−3, [NO] = (0.5 to 2) × 1012 molecules·cm−3, [O2] = (0.7 to 1.5) × 1015 molecules·cm−3, and [OH] = (0.8 to 8) × 1010 molecules·cm−3.
From ref. 9.
From ref. 11.
From ref. 12.
From ref. 18.
From ref. 19.
From ref. 27.
From ref. 15.
From ref. 13.
The yield of 11.3% for benzaldehyde determined in our present work is in agreement with the previous studies reporting a range of 5 to 12% (9, 11, 12, 18). We determined a lower limit of 47.9% for the total branching ratio of the cresol pathway (pathway I), including those from the combined formation of cresols and dihydroxymethylbenzenes. Our estimated cresol yield is much higher than that from most of the previous studies (12, 15, 18, 19, 27). For example, another experimental investigation using a flow reactor in conjunction with chemical ionization mass spectrometry (CIMS) detection reported yields of 28.1% at m/z = 109 and 23.5% at m/z = 125 (18). Although the sum of the two peaks from that work is comparable to our present value, the authors attributed the peak m/z = 125 to dienedial, which was speculated to form from O2 addition to the OH−toluene adduct followed by breaking of the OH group (18). In addition, it was commented on by Jenkin et al. (37) that the experimental work by Baltaretu et al. (18) might be complicated by possible interferences, because both radicals and the reactants were premixed with high concentrations in the side arm of the flow reactor. Also noticeably, we measured a negligible yield of methylglyoxal (less than 2%), in contrast to the fact that the previous environmental chambers studies consistently observed large amounts of small α-carbonyl compounds (glyoxal and methylglyoxal) as the ring-opening products (12). The negligible formation of methylglyoxal in our current work is also distinct from our previous study of the OH−m-xylene reactions, in which larger amounts of methylglyoxal and the coproducts of glyoxal and methylglyoxal were detected and quantified (35). Baltaretu et al. (18) also reported a small methylgyoxal yield, i.e., less than 4%, consistent with our present work. We did not detect any compound with an MW similar to that of expoxides and estimated the epoxide yield to be less than 1%. Bartolotti and Edney (38) suggested the formation of epoxide intermediates based on the large stability for epoxides, which was further corroborated by Yu and Jeffries (39), who found experimental evidence for epoxides by detecting compounds with MW matching a series of epoxides resulting from the OH−toluene system. However, isomerization of bicyclic radicals to the more stable expoxide radicals has been shown to possess significantly higher barriers than those of O2 addition to form bicyclic peroxy radicals (16, 26).
To further elucidate the toluene oxidation mechanism and corroborate our experimental results, we performed quantum chemical calculation for OH addition to the ortho, meta, and para positions of toluene and the subsequent reactions with O2. The potential energy surface diagrams of the toluene reactions are displayed in Fig. 3. OH addition at the ortho position occurs with the lowest activation energy (Ea) of 1.2 kcal⋅mol−1 and the largest reaction energy (ΔEr) of −15.5 kcal⋅mol−1 among the three pathways (Fig. 3A and Table 2). The kinetics calculations presented in Table 2 show a rate constant of 2.7 × 10−12 cm3·molecule−1·s−1 for OH ortho addition at 298 K, which is an order of magnitude higher than those of OH addition to the meta and para positions. The branching ratio (Γ) of OH ortho addition is estimated to be 76%. The energetics, rate constants, and branching ratios of the OH−toluene reactions are summarized in Table 2, along with comparisons with previously published experimental and theoretical results.
Fig. 3.
Potential energy surfaces of the OH−toluene reaction. (A) Addition to the ortho, meta, and para positions and the subsequent reactions with O2. (B) Addition of OH to o-cresol and the subsequent reaction with O2. The number denotes the energetics in kcal·mol−1.
Table 2.
Summary of activation energy (Ea, kcal·mol−1), reaction energy (ΔEr, kcal·mol−1), rate constant (k, cm3·molecule−1·s−1), and branching ratio (Γ) of the OH−toluene reactions at 298 K
Reactions | Quantity | Ortho | Para | Meta |
Toluene + OH → OH adduct | Ea | 1.2 | 2.1 | 2.7 |
ΔEr | −15.5 | −14.6 | −14.4 | |
k | 2.7 × 10−12 | 7.4 × 10−13 | 1.2 × 10−13 | |
Γ, % | 74*, 80.6†, 52‡, 59 | 21*, 14.3†, 34‡, 14 | 3*, 5.1†, 11‡, 5 | |
OH-adduct + O2 → cresol | Ea | 4.4§, 3.7 | 4.1 | 5.0 |
ΔEr | −26.3§, −28.7 | −26.8 | −27.0 | |
k | 1.6 × 10−15‡, 0.9 × 10−15§, 5.1 × 10−15 | 2.4 × 10−15‡, 1.7 × 10−15 | 1.2 × 10−16 | |
OH-adduct + O2 → RO2 | Ea | 7.5§, 7.1 | 0.8 | −0.4 |
ΔEr | −8.5§,−2.9 | −12.2 | −9.5 | |
k | 1.5 × 10−16‡, 2.8 × 10−16§, 1.0 × 10−17¶, 3 × 10−15 | 2.5 × 10−14‡, 1.5 × 10−14 | 4.5 × 10−15 | |
O-cresol + OH → DHMB | Ea | −0.4 | ||
ΔEr | −15.6 | |||
k | 4.3 × 10−11#, 4.3 × 10−11 | |||
DHMB + O2 → 1,2-dihydroxy-3-ethylbenzene | Ea | 2.2 | ||
ΔEr | −24.3 | |||
k | 5.4 × 10−12 |
The value is from the present work, except noted otherwise. Γ is calculated by excluding those from the OH ipso addition and the H-abstraction pathways.
From ref. 30.
From ref. 22, including a branching ratio of 3% for OH ipso addition.
From ref. 23, including a branching ratio of 15% for ipso position.
From ref. 26.
From ref. 10.
From ref. 41.
We further evaluated the competing reactions of the OH−toluene adducts with O2 lead to cresols (pathway I), organic peroxy radicals (RO2) (pathway II), and toluene oxide (pathway III). SI Appendix, Fig. S2 shows that the reaction of the ortho OH adduct with O2 to form 1,2-toluene oxide occurs with an Ea value of 33.6 kcal⋅mol−1 and a ΔEr value of 16.2 kcal⋅mol−1. Hence, the large activation energy and instability of the toluene oxide imply that its formation is thermodynamically and kinetically inhibited, in agreement with the previous studies (26). Our previous theoretical study indicated that, at each OH addition site, only one isomeric pathway via the peroxy radical is accessible for ring cleavage (16). On the basis of that study (16), the preferred peroxy radical corresponds to O2 additions at the C3 position (o-RO2 and p-RO2) for the ortho and para OH−toluene adducts, respectively, and at the C6 position (m-RO2) for the meta OH−toluene adduct. As illustrated in Fig. 3A and Table 2, the Ea value to form o-cresol is 4.4 kcal⋅mol−1, which is lower by 3.1 kcal⋅mol−1 than that to form o-RO2, and o-cresol is by 17.8 kcal⋅mol−1 more stable than o-RO2. The rate constant calculated is 1.6 × 10−15 cm3·molecule−1·s−1 for o-cresol formation (Table 2). In contrast, the Ea values to form p- and m-cresol are larger than those to form p- and m-RO2, although both p- and m-cresols are more stable (by about 15 kcal⋅mol−1) than p- and m-RO2, and the Γ values calculated are 9% and 3%, respectively, to form p- and m-cresol. The fate of the primary RO2 is governed by the competition between decomposition back to the OH−toluene adducts and O2 cyclization to form bridged bicyclic radicals. SI Appendix, Fig. S3 shows that the Ea values for RO2 decomposition are smaller than those of cyclization for p- and m-RO2. Considering the large differences in the relative stability between cresols and primary RO2 and the high Ea values for p- and m-RO2 cyclization, the majority of RO2 formed from the two channels shifts reversibly to cresols by equilibrium. Hence, we conclude that cresol formation represents the nearly exclusive pathway for the OH-addition reactions.
We performed additional calculations of the subsequent reactions of o-cresol with OH and O2 (Fig. 3B). OH addition at C3 position of o-cresol occurs with an Ea value of −0.4 kcal⋅mol−1 and a ΔEr value of −15.6 kcal⋅mol−1, corresponding to a rate coefficient of 4.3 × 10−11 cm3·molecule−1·s−1 to form the dihydroxymethybenzyl (DHMB) radical. Subsequently, the C3 DHMB radical undergoes readily H abstraction by O2, with an Ea value of 2.2 kcal⋅mol−1 and a ΔEr value of −26.5 kcal⋅mol−1, corresponding to a rate coefficient of 5.4 × 10−12 cm3·molecule−1·s−1 to form 1,2-dihydroxy-3-methylbenzene (MW = 124). In contrast, the formation of aromatic ketones (also MW = 124) is both thermodynamically and kinetically hindered (SI Appendix, Fig. S4). Hence, our theoretical calculations support the formation of dihydroxymethylbenzenes as the observed mass peak at m/z = 125. Our theoretical predictions agree with two previous experimental results, showing that the major oxidation products from the reactions of cresols with OH are dihydroxymethylbenzenes with a molar yield of 65 to 73% (33, 40). Furthermore, a fast rate constant of (1.6 to 2.1) × 10−10 cm3·molecule−1·s−1 for the reaction of dihydroxymethylbenzenes with OH has been reported (40, 41), indicating that the secondary products in the OH−toluene reactions undergo additional reactions with OH to form ring-opening products, including small α-carbonyl compounds (glyoxal and methylglyoxal), organic acids, and other low-volatility products (33).
As is evident from Table 2, our calculations of the energetics, rate constants, and branching ratios for the OH−toluene reactions compare favorably with the previously available experimental and theoretical results, considering the respective uncertainties. For example, our calculated rate coefficient of 4.3 × 10−11 cm3·molecule−1·s−1 for OH addition to o-cresol to form the DHMB radical is in agreement with the experimental value of (4.3 ± 0.5) × 10−11 cm3·molecule−1·s−1 by Coeur-Tourneur et al. (41). Additional structural parameters for the reactants, key intermediates, transition states, and products involved in the OH−toluene reaction system are shown in SI Appendix, Fig. S5.
Hence, our combined experimental and theoretical methods (42–60) provide kinetic and mechanistic insights into the OH−toluene reactions. In particular, the agreement between our experimental and theoretical results provides compelling evidence for the dominant cresol yield but a negligible formation of methylglyoxal from the initial steps of the OH−toluene reactions. In our work, we quantified only the most abundant peaks detected by our ion drift (ID)-CIMS scheme (using H3O+), accounting for about 64% of the toluene consumed. Another recent experimental study showed that OH addition to the aromatic ring of o-cresol leads to hydroxy, dihydroxy, and trihydroxy methyl benzoquinones and dihydroxy, trihydroxy, tetrahydroxy, and pentahydroxy toluenes, detected in the gas phase by CIMS (using CF3O− and H+•nH2O where n = 1, 2, …) and in the particle phase using offline direct analysis with real-time mass spectrometry (33).
The differences in the measured product yields between our present experimental work and the previous laboratory experiments are explainable by the distinct conditions among the various experimental studies. Although the environmental chamber method has been applied extensively in development of parameterizations of formation of ozone and SOA for atmospheric modeling purposes (5), there were several intricate difficulties for the chamber approach, which made it rather unsuitable for detailed kinetic and mechanistic investigations of atmospheric hydrocarbon chemistry. Specifically, the limitations in the earlier chamber studies included longer reaction times (minutes to hours), higher reactant concentrations, wall loss, and the lack of online detection and quantification of reactive reactants and products by advanced analytical instruments. For example, an earlier experimental study reported a yield of 25.2% for the cresols from the OH−toluene reactions (27). The concentrations of the reactants used in that study were about 4 × 1013 and 1 × 1013 molecules·cm−3 for toluene and NOx, respectively, and the OH concentration was not measured but was estimated from the decay in the toluene concentration. The concentrations of the reactants and products were measured by using offline gas chromatography with flame ionization detection. For the irradiation time of about 10 min during their chamber experiments, a lifetime of cresols was estimated to be about 230 s, using the rate coefficient of 4.3 × 10−11 cm3·molecule−1·s−1 for the reaction between cresols and OH from this work and another experimental study (40). Hence, there likely existed significant secondary reactions of cresols with OH in the earlier chamber investigations, responsible for the measured lower cresol yields in the majority of those studies (12, 19, 27).
On the other hand, the technique of high-pressure turbulent flow reactors in conjunction with CIMS detection has been developed for accurate kinetic measurements of atmospheric gas-phase reactions (35, 36). The main advantage of the fast-flow reactor system lies in the ability to isolate the individual reaction steps and intermediates (35, 36, 42–44, 48, 61). Specifically, the CIMS technique allows for online detection of many reactants, intermediates, and products with high sensitivity and selectivity (35, 36). In addition, the ID-CIMS method provides quantification of the gas-phase concentrations of the intermediates and products without the necessity of calibration, which is advantageous because of the general difficulty in obtaining the authentic standards for products of hydrocarbon reactions (34–36). Furthermore, a turbulent flow condition effectively minimizes the wall loss (35, 36). In our experiments, the reactant concentrations were (0.4 to 1.6) × 1012 and (5.4 to 19) × 1012 molecules·cm−3 for toluene and NO2, respectively, about one to two orders of magnitude lower than those of the environmental chamber studies (12, 19, 27). In addition, the OH concentration was directly quantified in our experiments, in a range of (0.8 to 8.0) × 1010 molecules·cm−3. Secondary reactions were effectively suppressed in our experiments because of the short reaction time in the flow reactor (on the order of about 50 ms). The lifetime of cresols was estimated to be about 2 s in our experiments, responsible for our measured high yield of cresols. Under our experimental conditions, the self-reaction of the OH−toluene adducts was unimportant on the basis of this rate constant reported previously (10); this reaction was estimated to be about one to two orders of magnitude lower than that of the OH−toluene adduct with O2. Furthermore, the absolute O2 concentration had no effect for the competing reactions between the cresol and primary RO2 pathways (i.e., pathway I vs. pathway II in Fig. 1), and the previous experimental results did not show a pressure dependence of the OH−toluene reaction system (61).
Also, our theoretical calculations indicate that formation of glyoxal and methylglyoxal via primary RO2 is minimal, consistent with the absence in the ring-opening α-carbonyl products detected in our experiments. It is anticipated that those species are formed as the multigeneration products from the cresol pathway (33), likely similar to the cases with their high yields in the previous chamber experiments (12, 13).
Conclusion
Photochemical oxidation of toluene contributes importantly to ozone and SOA formation in urban environments, with key implications for air quality and human health (1–3, 62). In addition, by directly scattering and absorbing solar radiation and indirectly serving as cloud condensation nuclei or ice nuclei, SOA represents the major component in global radiative forcing on climate (1–3). For toluene oxidation, ozone formation in current atmospheric models is represented mainly via primary RO2, with a minor contribution from cresols (5). In contrast, our experimental and theoretical results reveal the exclusive prompt productions of cresols and HO2, but insignificant formation of primary RO2 from the reaction of OH−toluene adducts with O2. HO2 is also produced from the reaction of cresols with OH, and further reactions of dihydroxymethylbenzenes with OH yield additional HO2 and RO2. As a result, the production of HO2 and RO2 along the phenolic pathway regulates the abundance of the total peroxy radicals, which facilitates the conversion between NO and NO2 (Fig. 4). In addition, the relative branching between the RO2 and cresol pathways likely affects the OH radical propagation and termination, which are also important for ozone formation.
Fig. 4.
Toluene oxidation and urban photochemical smog. The OH−toluene reactions lead promptly and dominantly to cresol formation, which regulates the impacts on air quality, human health, and climate. The phenolic pathway yields HO2 and RO2 that facilitate ozone production by converting NO to NO2, as photodissociation of NO2 occurs in the wavelength range of 400 nm to 650 nm (the symbol hv denotes the energy of a photon, where h is the Planck number and v is the frequency of light). Also, dihydroxymethylbenzenes generated from this pathway undergo subsequent reactions with OH to form the precursors for aerosol nucleation and growth, including small α-carbonyl compounds, organic acids, and other highly oxygenated low-volatility products.
The further oxidation of dihydroxymethylbenzenes by OH leads to formation of small α-dicarbonyl compounds (glyoxal and methylglyoxal), organic acids, and other low-volatility products (33, 40), which likely contribute to aerosol nucleation and growth by partitioning and particle-phase reactions (1, 63–65). In particular, the recent experimental study by Schwantes et al. (33) has identified a substantial fraction of highly oxygenated low-volatility products, contributing to 20 to 40% of SOA formation from the cresol oxidation initiated by OH radicals.
Our combined experimental and theoretical results show that the prompt formation of cresols and their subsequent oxidation largely regulate the atmospheric impacts of toluene oxidation (Fig. 4), indicating that the representation of the toluene oxidation mechanism should be reassessed in current atmospheric models. Future studies are necessary to incorporate the kinetic and mechanistic results from our present work into atmospheric models, to accurately assess ozone and SOA formation under polluted environments.
Materials and Methods
The experiments were performed using a fast-flow reactor in conjunction with ID-CIMS. Detailed description of the ID-CIMS technique can be found in our previous publications (42–44).
Quantum chemical calculations were performed with the Gaussian 09 suite of programs (45). Geometry optimization of the relevant species were executed at the M06-2X level with the standard 6-311G(d,p) basis set [M06-2X/6-311G(d,p)]. This level of theory has been successfully applied to atmospheric reactions (46, 47). The vibrational analysis was made at the same level of theory to characterize the nature of each critical point along the potential energy surface (PES) with a local minimum or a transition state (exactly one imaginary frequency) and to make zero-point-energy corrections. The minimum-energy path was constructed with the intrinsic reaction coordinate theory to confirm that the transition state connected with the minima along the reaction path. Because kinetic calculations of the organic reaction systems were highly sensitive to the predicted energetics (48–51), single-point energy calculations were performed to refine the PES using the QCISD(T)/6-311+G(2d,p) level. The dual-level potential profile along the reaction path was further refined with the interpolated single-point energy method (52), in which extra single-point calculations were performed to correct the lower-level reaction path. The dual-level dynamics approach was denoted as X//Y, where a single-point energy calculation at level X was carried out for the geometry optimized at a lower level Y. Using the Polyrate 2010A (53) and KiSThelp programs (54), the rate constants were calculated according to the canonical variational transition state theory (55–59), along with the small curvature tunneling correction (60).
Additional descriptions of the experimental conditions and the structure of the reactants, products, intermediates, and transition states are provided in SI Appendix.
Supplementary Material
Acknowledgments
This work was supported by National Natural Science Foundation of China (Grants 41675122, 41373102, 21577177, and 41425015), Science and Technology Program of Guangzhou City (Grant 201707010188), the Robert A. Welch Foundation (Grant A-1417), the Ministry of Science and Technology of China (Grant 2013CB955800), and a collaborative research program between Texas A&M University and the National Natural Science Foundation of China. B.P. was supported by a NASA Earth and Space Science Fellowship Program, and W.M.-O. was supported by the National Science Foundation Graduate Research Fellowship Program. Additional support for this research was provided by the Texas A&M University Supercomputing Facilities. The authors acknowledge the use of the Laboratory for Molecular Simulations at Texas A&M.
Footnotes
The authors declare no conflict of interest.
This article contains supporting information online at www.pnas.org/lookup/suppl/doi:10.1073/pnas.1705463114/-/DCSupplemental.
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