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Nitrogen dioxide coefficients

Our analysis of the reaction of nitrogen dioxide molecules is not unique. The same type of path can be visualized for any chemical reaction, as Figure 6-20 shows. The reaction enthalpy for any chemical reaction can be found from the standard enthalpies of formation for all the reactants and products. Multiply each standard enthalpy of formation by the appropriate stoichiometric coefficient, add the values for the products, add the values for the reactants, and subtract the sum for reactants from the sum for products. Equation summarizes this procedure ... [Pg.407]

Gifford and Hanna tested their simple box model for particulate matter and sulfur dioxide predictions for annual or seasonal averages against diffusion-model predictions. Their conclusions are summarized in Table 5-3. The correlation coefficient of observed concentrations versus calculated concentrations is generally higher for the simple model than for the detailed model. Hanna calculated reactions over a 6-h period on September 30, 1%9, with his chemically reactive adaptation of the simple dispersion model. He obtained correlation coefficients of observed and calculated concentrations as follows nitric oxide, 0.97 nitrogen dioxide, 0.05 and rhc, 0.55. He found a correlation coefficient of 0.48 of observed ozone concentration with an ozone predictor derived from a simple model, but he pointed out that the local inverse wind speed had a correlation of 0.66 with ozone concentration. He derived a critical wind speed formula to define a speed below which ozone prediction will be a problem with the simple model. Further performance of the simple box model compared with more detailed models is discussed later. [Pg.226]

Ka can be defined as a gas-phase transfer coefficient, independent of the liquid layer, when the boundary concentration of the gas is fixed and independent of the average gas-phase concentration. In this case, the average and local gas-phase mass-transfer coefficients for such gases as sulfur dioxide, nitrogen dioxide, and ozone can be estimated from theoretical and experimental data for deposition of diffusion-range particles. This is done by extending the theory of particle diffusion in a boundary layer to the case in which the dimensionless Schmidt number, v/D, approaches 1 v is the kinematic viscosity of the gas, and D is the molecular diffusivity of the pollutant). Bell s results in a tubular bifurcation model predict that the transfer coefficient depends directly on the... [Pg.300]

Com. M., N. Kotsko, and D. Stanton. Mass transfer coefficient for sulfur dioxide and nitrogen dioxide removal in cat upper respiratory tract. In W. H. Walton. Ed. Inhaled Particles IV. Proceedings of the Fourth International Symposium on Inhaled Particles and Vapors, British Occupational Hygiene Society, Edinburgh, September, 1975. London Pergamon Press. Ltd. (in press)... [Pg.316]

Quantum Yields. In order to understand these data, it was necessary to obtain the absorption coefficients for the different gaseous substances nitrogen dioxide, nitrogen tetroxide, and nitrogen pentoxide. The oxygen is transparent. The following formula... [Pg.139]

The stoichiometry is more complicated here because 2 mol of dinitrogen pentoxide produce 4 mol of nitrogen dioxide and 1 mol of oxygen. So, it is no longer true that the rate of decrease of the reactant concentration equals the rates of increase of the product concentrations. However, this difficulty can be overcome if, in order to define the reaction rate, we divide by the coefficients from the balanced equation. For this reaction, we get the following. [Pg.596]

The absorption coefficient of nitrogen dioxide was measured for several mercury lines by Holmes and Daniels (5). The resolved spectra of the nitrogen dioxide-nitrogen tetroxide system were separated by Hall and Blacet (4)- The value they found for the absorption coefficient at 3660 A. was in essential agreement with that obtained by Holmes and Daniels. The absorption cross section of 6.8 X 10 sq. cm. for nitrogen dioxide at 3660 A. was calculated from the data of Holmes and Daniels. [Pg.411]

A is correct. The number of moles of gas is extra information. If the container began at 11 atm then each gas is contributing a pressure in accordance with its stoichiometric coefficient. When the reaction runs to completion, the only gas in the container is nitrogen dioxide, so the partial pressure of nitrogen dioxide is the total pressure. The volume of the container remains constant, so the pressure is in accordance with the stoichiometric coefficient of nitrogen dioxide. [Pg.186]

Fig. 2-20. Photodissociation coefficients for N02, HCHO, CHjCHO, and 0( D) produced from ozone, for ground-level, clear-sky conditions. Nitrogen dioxide diamonds are measurements of Madronich et al. (1983), solid points are data of Marx et al. (1984), the solid line represents calculations of Madronich et al. (1983) using the method of Isaksen et al. (1977), and the dashed line is for isotropic scattering. Formaldehyde open points are measurements of Marx el al. (1984), and the solid line represents calculations of Calvert (1980). Acetaldehyde triangles are measurements of Marx et al. (1984), and the solid line represents calculations of Meyrahn et al. (1982). Ozone solid points are measurements of Dickerson et al. (1979) and Bahe et al. (1980) normalized to 325 Dobson units of total ozone overhead, and the solid line represents calculations of Dickerson et al. (1979). Fig. 2-20. Photodissociation coefficients for N02, HCHO, CHjCHO, and 0( D) produced from ozone, for ground-level, clear-sky conditions. Nitrogen dioxide diamonds are measurements of Madronich et al. (1983), solid points are data of Marx et al. (1984), the solid line represents calculations of Madronich et al. (1983) using the method of Isaksen et al. (1977), and the dashed line is for isotropic scattering. Formaldehyde open points are measurements of Marx el al. (1984), and the solid line represents calculations of Calvert (1980). Acetaldehyde triangles are measurements of Marx et al. (1984), and the solid line represents calculations of Meyrahn et al. (1982). Ozone solid points are measurements of Dickerson et al. (1979) and Bahe et al. (1980) normalized to 325 Dobson units of total ozone overhead, and the solid line represents calculations of Dickerson et al. (1979).
Oxides of Nitrogen Nitric oxide (NO) and nitrogen dioxide (N02) are also characterized by small solubility in water (Henry s law coefficients 0.002 and 0.01 Matm-1 at 298 K). A negligible fraction of these species is dissolved in cloudwater, and their aqueous-phase concentrations are estimated to be on the order of 1 nM or even smaller. [Pg.303]

Locate the appropriate coefficients that describe empirically the temperature dependence of the specific heat for both carbon dioxide and nitrogen dioxide. The polynomial expression can be written generically in the following form ... [Pg.780]

Assumption the diffusion coefficient of gas unchanged component transport setting for mixed gas of methane, nitrogen and oxygen gas, ignore the water vapor, nitrogen dioxide and so on. In the numerical simulation of gas components need to maximum content of gas in the last. [Pg.844]

The first coefficient describes the most common case, namely how much entropy AS flows in if the temperature outside and (also inside as a result of entropy flowing in) is raised by AT and the pressure p and extent of the reaction are kept constant. In the case of the secmid coefficient, volume is maintained instead of pressure (this only works well if there is a gas in the system). In the case of J = 0, the third coefficient characterizes the increase of entropy during equilibrium, for example when heating nitrogen dioxide (NO2) (see also Experiment 9.3) or acetic acid vapor (CH3COOH) (both are gases where a portion of the molecules are dimers). Multiplied by T, the coefficients represent heat capacities (the isobaric Cp at constant pressure, the isochoric Cy at constant volume, etc.). It is customary to relate the coefficients to the size of the system, possibly the mass or the amount of substance. The corresponding values are then presented in tables. In the case above, they would be tabulated as specific (mass related) or molar (related to amount of substance) heat capacities. The qualifier isobaric and the index p will... [Pg.253]

Nitrogen monoxide can be oxidized to nitrogen dioxide and the equation is balanced by coefficients of 2 in front of the two oxides of nitrogen ... [Pg.277]

This is balanced by adding a coefficient of 2 in front of the nitrogen dioxide (nitrogen(iv) oxide) 2N02(g) + Hzd) HN02(aq) + HNOjlaq)... [Pg.278]

In other cases it is necessary to introduce two temperature coefficients depending on the field in order to accoimt for the influence of temperature. This is the case, for example, in the reduction of nitrogen dioxide by carbon monoxide. Figure 5.1 shows the shape of the curve in Arrhenius coordinates. [Pg.94]

NO , is removed from the atmosphere by several mechanisms including via the formation of low-volatility organic nitrates in reaction (3b) which are incorporated into aerosol and then undergo wet and dry deposition. In addition, nitrogen dioxide reacts with OH radicals with a rate coefficient of 1.19 x 10 cm molecule" s in 1 atmosphere of air at 298 K (Atkinson et al., 2004) and gives HNO3 which is removed by wet and dry deposition. In the presence of [OH] = 10 molecule cm the lifetime of NO2 with respect to reaction with OH is approximately 1 day. NO , has a relatively short atmospheric lifetime and is not transported directly from polluted to remote areas. [Pg.1384]

Reasonable prediction can be made of the permeabiUties of low molecular weight gases such as oxygen, nitrogen, and carbon dioxide in many polymers. The diffusion coefficients are not compHcated by the shape of the permeant, and the solubiUty coefficients of each of these molecules do not vary much from polymer to polymer. Hence, all that is required is some correlation of the permeant size and the size of holes in the polymer matrix. Reasonable predictions of the permeabiUties of larger molecules such as flavors, aromas, and solvents are not easily made. The diffusion coefficients are complicated by the shape of the permeant, and the solubiUty coefficients for a specific permeant can vary widely from polymer to polymer. [Pg.498]


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