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Kinetic analysis of the gas-phase reactions of methacrolein with the OH radical in the presence of NOx

Abstracts

An explicit chemical mechanism for the reaction of methacrolein (MTA) with OH radicals in NOx-air systems, was simulated by solving the corresponding ordinary differential equations using Runge-Kutta-4-semi-implicit method. The simulated results are consistent with the published experimental data and the model accounts for all the major pathways by which MTA reacts in NOx-air systems. An eigenvalue-eigenvector analysis is used to extract meaningful kinetic information from linear sensitivity coefficients computed for all species of the chemical mechanism at several time points. This method is used to get an objective condition for constructing a minimal reaction set. Also, a classic method called rate of production analysis (ROPA) was used for the study of the reactions relevance. Using the principal component information as well as the rate of production analysis the main paths of reaction are identified and discussed.

principal component analysis; eigenvalue-eigenvector analysis; rate of production analysis; methacrolein


Um mecanismo explícito para a reação da metacroleína (MTA) com radicais OH, numa mistura NOx - ar, foi simulado resolvendo as equações diferenciais ordinárias usando o método Runge-Kutta-4-semi-implícito. Os resultados simulados são consistentes com os dados experimentais publicados e o modelo explica as principais vias de reação para a oxidação da MTA com radicais OH na presença de NOx - ar. Usando uma análise dos autovetores e autovalores dos coeficientes de sensibilidade, para todas as espécies químicas envolvidas em diferentes tempos de reação, foi extraída informação cinética do sistema. Este método foi utilizado para reduzir o modelo cinético de forma objetiva. Foi utilizado, também, o método tradicional de análise de velocidade de produção (ROPA) para estudar a importância relativa das reações individuais. Usando a informação da análise de componente principal e da análise de velocidade de produção, foram identificadas as principais reações individuais.


Article

Kinetic Analysis of the Gas-Phase Reactions of Methacrolein with the OH Radical in the Presence of NOx

André Silva Pimentel ** e-mail: e-mail: pimentel@iq.ufrj.br , and Graciela Arbilla

Departamento de Físico-Química, Instituto de Química, Universidade Federal do Rio de Janeiro, Centro de Tecnologia, Bloco A, Sala 408, Cidade Universitária, 21949-900 Rio de Janeiro - RJ, Brazil

Um mecanismo explícito para a reação da metacroleína (MTA) com radicais OH, numa mistura NOx - ar, foi simulado resolvendo as equações diferenciais ordinárias usando o método Runge-Kutta-4-semi-implícito. Os resultados simulados são consistentes com os dados experimentais publicados e o modelo explica as principais vias de reação para a oxidação da MTA com radicais OH na presença de NOx - ar. Usando uma análise dos autovetores e autovalores dos coeficientes de sensibilidade, para todas as espécies químicas envolvidas em diferentes tempos de reação, foi extraída informação cinética do sistema. Este método foi utilizado para reduzir o modelo cinético de forma objetiva. Foi utilizado, também, o método tradicional de análise de velocidade de produção (ROPA) para estudar a importância relativa das reações individuais. Usando a informação da análise de componente principal e da análise de velocidade de produção, foram identificadas as principais reações individuais.

An explicit chemical mechanism for the reaction of methacrolein (MTA) with OH radicals in NOx-air systems, was simulated by solving the corresponding ordinary differential equations using Runge-Kutta-4-semi-implicit method. The simulated results are consistent with the published experimental data and the model accounts for all the major pathways by which MTA reacts in NOx-air systems. An eigenvalue-eigenvector analysis is used to extract meaningful kinetic information from linear sensitivity coefficients computed for all species of the chemical mechanism at several time points. This method is used to get an objective condition for constructing a minimal reaction set. Also, a classic method called rate of production analysis (ROPA) was used for the study of the reactions relevance. Using the principal component information as well as the rate of production analysis the main paths of reaction are identified and discussed.

Keywords: principal component analysis, eigenvalue-eigenvector analysis, rate of production analysis, methacrolein

Introduction

Methacrolein is an

a,b-unsaturated aldehyde. It is produced in a significant yield from the gas-phase reactions of isoprene, a vegetative emission

1-6, with OH radical in the presence of NO

x

7-10 and O

3

11-12. Since the emissions of isoprene may dominate over anthropogenic nonmethane emissions on regional and global scales

13-15, a knowledge of the atmospheric chemistry of methacrolein is a necessary input into the chemical mechanism for the atmospheric photooxidation of isoprene for use in airshed computers models

16-17. Under atmospheric conditions, the major loss process for methacrolein is calculated to occur by reaction with the OH radical

18.

In this work, the gas-phase reactions of methacrolein (hereafter MTA, CH2=C(CH3)CHO) with OH radicals in NOx-air systems are simulated and an eigenvalue-eigenvector analysis of the linear sensitivity coefficients, called Principal Component Analysis19, is used to assess the parameter-concentration interdependence and obtain a reduced mechanism.

Reaction rate analysis for complex kinetic systems includes the solution of a mathematical model, i. e., a set of coupled kinetic ordinary differential equations, the study of the effects of parameter changes on the results and the exploration of important reaction pathways19-25. This information is important to decide which reactions should be included in a atmospheric photochemical mechanism and, also, which reactions should be experimentally studied. A good mechanism should be as simple as possible and the number of its parameters and components should be minimum.

Only one experimental study has been conducted for the MTA reaction with OH radicals26. In this study the products of MTA oxidation were measured and identified, obtaining directly quantitative yields for hydroxyacetone (HOCH2C(O)CH3) , methylglyoxal (CH3COCHO), formaldehyde (HCHO) and peroxymethacryloyl nitrate (hereafter PMN, CH2=C(CH3)C(O)OONO2). The authors have also discussed and recommended a mechanism to represent the MTA + OH chemistry. Nevertheless, to our knowledge, the solution of kinetic differential equations and a sensitivity analysis of the mechanism have not been done up to now.

Since the calculated results from a deterministic model are strictly a function of its parameters and variables as time, temperature and pressure, in these simulations the initial conditions for the simulations were those of the experimental work26 in order to compare the calculated and laboratory smog chamber results.

The Chemical Mechanism

As experimentally determined26 MTA reacts essentially with OH radicals by H-atom abstraction, with an overall rate constant of 3.35 x 10-11 cm3 molecule-1 s-1 at 298 K27.

The complete chemical mechanism is listed in Table 1. It includes 38 species and 50 reactions. It was proposed on the basis of previous mechanisms28,29 and of the known MTA26 and PMN30 chemistry. Thermal rate constants were either taken from literature31-34 or estimated by comparison with similar compounds35 when there was no available information. As photochemical reaction rates are dependent on the experimental conditions and were not reported by Tuazon and Atkinson26 they were estimated on the basis of the methacrolein photooxidation experimental data26.

Methodology

As usual, the chemical process can be described by a system of kinetic differential equations,

where c(t) is the n-vector of species concentrations with c(t = 0) = c0 and k is the m-vector of kinetic parameters. For complex systems a numerical solution is required. The available methods to solve the differential equations and to investigate the main features of the mechanism are fully discussed in the literature19,24,25,36-38.

In investigating a chemical mechanism, it is important to assess the effects of parameter uncertainties on the predicted concentrations of the various intermediate and product species. This analysis is known as sensitivity analysis and is useful in determining the main reaction path. An element of the first order local concentration sensitivity matrix, Sij is given by

and is the linear approximation of concentration change of species i at the time t2 caused by the differential change of the parameter of reaction j at time t1 from value kj0 to kj. In this work the parameters are the photochemical coefficients and the thermal rate constants.

Sensitivity coefficients are normalized in order to eliminate their dependence on the dimensions of the kinetic model. The parameter-concentration interdependence may be described in two ways: by the overall sensitivities, which are the sum of the squares of the normalized sensitivities, and by the principal component analysis of the normalized sensitivity matrix. The overall sensitivities give the effect of a single parameter on a concentration group. The principal component analysis consists in the identification of the parameters group which has joint influence on a concentration group. This method is a kind of factor analysis and its main goal is to decry those hidden factors which have generated the dependence or variation in responses.

The eigenvectors of the matrix STS, where S is the array of sensitivity coefficients, identify parameter groups while the eigenvalues give information about the effectiveness of these parameter groups for the change of species concentrations. A parameter is considered important if it belongs to a large element of an eigenvector corresponding to a large eigenvalue. The principal component of the system is the linear compound

whose coefficients are the characteristic vector elements associated with the eigenvalue. The importance and usefulness of the component would be measured by the total variance magnitude attributable to it, that is by the ratio of its eigenvalue to the sum of all eigenvalue.

An alternative way and more classical method for the investigation of the reactions relevance is the rate of production analysis called ROPA38,39. This method calculates the contribution of each reaction step to the total production rate of each species using concentration data and the rate coefficients. Although very simple to implement, this method gives results which are rather difficult to interpret in a correct way and sometimes leads to misleading conclusions. Thus, the combination of species reduction and rate sensitivity analysis25 seems to be a more effective way for this purpose, the rate of production analysis is a classic method for the identification of important reaction pathways. This methodology requires the calculation of the Pij matrix elements40,41, which show the contribution of reaction j to the rate of production of species i.

Results and Discussions

The full mechanism and rate constants are presented in Table 1. The reduced mechanism was obtained after elimination of the unimportant reactions (denoted by # in Table 1) on the basis of the principal component analysis described below. The rank of reactions ordered by overall sensitivities and rates is shown in Table 2. We calculated normalized sensitivities for all species at time points 1.9, 6.9, 11.9, 15.9, 19.9, 24.9 and 40.9 min. Eigenvalues of STS and the corresponding eigenvectors are listed in Table 3.

In the conditions of the modeling, the main source of hydroxyl radicals is the reaction (5) (HO2 + NO ® OH + NO2) which follows the photolysis of the ethyl nitrite (CH3CH2ONO + hn ® CH3CH2O + NO) and the oxidation of the CH3CH2O radicals (CH3CH2O + O2® CH3CHO + HO2). Reaction (5) accounts for ca. 95% of OH radical formed and the only significant sources of NO are the photodecomposition of ethyl nitrite (7%) and NO2 (93%), reactions (36) and (10), respectively. Since photolysis light intensities during the experiments were not reported26, the ethyl nitrite photodecomposition coefficient was estimated from the experimental concentration profiles of MTA as a function of time (Fig. 1). This method of parameter estimation is supported by the facts discussed above: in the smog chamber conditions, the only significant source of hydroxyl radicals is ethyl nitrite phololysis and MTA reacts primarily with OH radicals. The selected values gave consistent results for other photodecompositions and are also in agreement with the value reported in literature42 for NO2 in the same experimental conditions. The set of reactions (Table 1) accounts for the MTA photooxidation in good agreement with experimental data (Fig. 1). As presented in Fig. 2, simulated results for the formation of the main products where hydroxyacetone and methylglyoxal show a good agreement with experimental data. On the other hand, formaldehyde and peroxymethacryloyl nitrate (Figs. 3 and 4), show a slight deviation mainly for longer times.





In these simulation conditions, formaldehyde is formed both from acetaldehyde, the initial product of ethyl nitrite photolysis, reaction (36), and by the sequence of reactions initiated by OH radical oxidation of MTA, reaction (20):

CH2=C(CH3)CHO + OH + (O2)

® 0.42 HOCH

2C(O

2)(CH

3)CHO + 0.08 O

2CH

2C(OH)(CH

3)CHO + 0.50 CH

2=C(CH

3)C(O)OO + 0.50 H

2O

The rate of production analysis shows that 52.5% of formaldehyde is formed initially through the reaction sequence (20), (28), (29), (30), (31) and (32), 25.4% through the reaction (13), CH3O + (O2) ® HCHO + HO2, and 22.1% through the reaction sequence (20), (23) and (24), which involve the reaction of O2CH2C(OH)(CH3)CHO with NO. The CH3O radical is formed through reactions (15) and (14) from CH3CO3 which is a secondary product of MTA oxidation, see reaction (32), and a product of acetaldehyde photooxidation, reaction (12). For longer times, t > 10 min, the relative importance of these paths is changed and 80.9% of formaldehyde is formed through the reaction sequence (20), (23) and (24), 10.0% through the reaction sequence (20), (28), (29), (30), (31) and (32), and 9.1% through the reaction (13), CH3O + (O2) ® HCHO + HO2. Under the modelling conditions, the decomposition reactions of formaldehyde, reactions (11), (49) and (48), are initially 11% of the total and after this the yield increases up to 45% at the end of reaction. As observed experimentally26,42, the formed formaldehyde reacts essentially with OH radicals which are in relatively high concentrations (calculated values about 0.6-1.3 x 107 molecule cm-3). In comparison with the OH radical reaction (11) (HCHO + OH + (O2)

® HO

2 + CO + H

2O), the photochemical decompositions (39) and (40) (HCHO + (2 O

2) +

hn ® 2 HO

2 + CO and HCHO +

hn ® H

2 + CO) are of non-negligible importance (30-40%).

In the conditions of this simulation, the formation of acetaldehyde and peroxyacetyl nitrate (PAN) can be attributed to the photooxidation of ethyl nitrite26,42. In comparison with OH radical reaction (CH3CHO + OH + (O2)

® CH

3CO

3 + H

2O), the acetaldehyde photochemical decompositions (CH

3CHO + (2 O

2) +

hn ® CH

3O

2 +HO

2 +CO) are of non-negligible importance, as shown by the principal component analysis.

The 1st and 2nd principal components in Table 3 show that ethyl nitrite photodecomposition, reaction (36), oxidation of MTA, reaction (20), and OH/NO chemistry, reactions (4) and (5), are strongly coupled and are the most influential reaction sequence in the mechanism. Thus, a small deviation in k20 or j36 should largely affect the simulation results. The same conclusions were obtained in the simulation of methyl-tert-butyl ether (MTBE)43 and methyl vinyl ketone (MVK)44 photooxidation by OH radicals.

According to the magnitude of the eigenvalues and significant entries (³ 0.20) of the corresponding eigenvector, the individual reactions may be classified in three groups:

1) Eigenvalues

l

1 to l

31 are much larger than the remaining ones. Note that

Principal components y

1 to y

31 contain steps (3)-(10), (12)-(16), (18), (20)-(26), (28)-(36), (39)-(43), (46)-(47) and (50), forming the "basic" part of mechanism. According to y

1, the most influential reaction sequence is formed by (36), (20), (4) and (5). This first component emphasizes that the largest effect is brought about by setting the parameters j

36 and k

20. Reactions (4) and (5) largely affect the NO/NO

2 ratio and the simulated results. Due to the coupling of the individual reactions, this ratio not only depends on the rate of reactions (20) and (36) but also on all the reactions involving NO

x. Since j

36 is an estimated parameter, some deviations of the simulated results may be attributed to it. An uncertainty analysis of this parameter shows that a change of 10% in j

36 leads to a substantial change of all product concentrations (4.8% in hydroxyacetone, 4.4% in methylglioxal, 5.9% in peroxymethacryloyl nitrate and 7.3% in formaldehyde). The inclusion of another minor path of reaction, such the formation of alkylnitrates, might affect the NO/NO

x ratios in a non-negligible amount.

2) According

y

32 to y

39, reactions (11), (17), (19), (27), (44) and (48)-(49), are of "transitional" importance. As it will be shown, in spite of their small contributions they can not be removed from the mechanism.

3) Reactions (1), (2), (37)-(38) and (45) contained in

y

40 to y

49 with eigenvalues below 2.66 x 10

-2 are unimportant and can be eliminated.

As shown in Table 4, eliminating the last group of reactions causes small changes in concentrations. However, additional elimination of steps (11), (17), (19), (27), (44) and (48)-(49) (i.e. reactions of "transitional" importance) leads to large deviations (Table 4). Since all concentration changes should be small, no further mechanism reduction is possible.

The rank of reactions by overall sensitivity (Table 2) suggests that reaction 49 may be eliminated. However, this elimination leads to large deviations (e. g. at t = 40.9 min the deviation for HCHO is 5.9%). The rate reaction rank (Table 2) gives a different rank of reactions and is not an effective way of reducing a mechanism. Individual rates do not consider the interactions between reactions and may lead to incorrect conclusions about the relevance of individual reactions. Anyway, the rate of production analysis is a good method for the exploration of the reaction pathways and provides useful information as shown in the initial part of this discussion.

Conclusions

The proposed chemical mechanism gives satisfactory results for the oxidation of MTA by OH radicals in comparison with experimental chamber data. Unfortunately the experimental data were obtained for a rather narrow range of conditions. Since mechanism results are a function of initial conditions, the conclusions taken from the eigenvalue-eigenvector analysis are only valid for this set of conditions. Anyway, the results shows that the reaction mechanism is strongly coupled and confirms that the most influential reactions are ethyl nitrite photolysis, the MTA oxidation, PAN and HOx/NOx chemistry. This is in agreement with independent evidences that tropospheric chemistry is controlled by NOx concentrations and OH oxidation of volatile organic compounds.

On the basis of the calculated eigenvalues, the mechanism can be reduced to 45 reactions. Since reactions (21) - (35) form the basic part of the mechanism, the estimation of their rate constants may lead to a considerable uncertainty in the simulated results. Then, further experiments with this system, in order to study those reaction paths, would be important in the improvement of atmospheric photochemical mechanisms.

Acknowledgements

The authors gratefully acknowledge CAPES and FAPERJ for partial financial support, NCE/UFRJ for computing facilities on the SP2 supercomputer, and Prof. T. Turányi (Central Research Institute for Chemistry, Budapest, Hungary) for a free copy of the KINAL package.

Note

All calculations were performed using the KINAL package45.

References

Received: May 3, 1999

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  • Publication Dates

    • Publication in this collection
      01 June 2001
    • Date of issue
      Dec 1999

    History

    • Received
      03 May 1999
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