4 |
Heterogeneous Interactions of the C, N, and S Cycles in the Atmosphere: The Role of Aerosols and Clouds |
| G. S. TAYLOR, M. B. BAKER AND R. J. CHARLSON |
The cycles of C, N and S interact in the atmosphere within the condensed phases of aerosol particles and clouds. Much of this interaction occurs in the aqueous phase due to the hygroscopic nature of compounds like NH4, HSO4 and the water solubility of trace gases, such as SO2 and NH3. In order to explore the nature of these interactions, the equilibria of the system H2O(1), SO2, NH3, H2SO4 and CO2 are examined. Subsequently, oxidation of S(IV) to S(VI) within the aqueous phase is considered as a function of NH3, H2O(1), and the source strength of S(IV).
The results are:The heterogeneous interactions of C, N, and S cycles within the atmosphere depend on the existence of aerosols and water clouds. * These particles provide sites for rapid reaction of key molecules that otherwise react slowly (or not at all) in the gas phase. Such reactions in or on particles are expected to be particularly important in situations where photochemistry is not effective (Shaw and Rodhe, 1981). In addition, many of the reaction products of gaseous N and S compounds are themselves liquids or solids of low vapour pressure under normal conditions and are found as aerosol particles. The water solubility of these reactions products allows their incorporation into cloud droplets and removal from the atmosphere by precipitation. The nature of the interactions of C, N, and S cycles thus will depend on the physical and chemical characteristics of both aerosols and clouds. In addition, these interactions cause shifts in chemical equilibria that in turn cause nonlinear responses of atmospheric concentrations and fluxes to changes in the source strength of materials injected into the air.
Atmospheric aerosols are chemically heterogeneous and are composed of large numbers of compounds. While it has been customary and useful to treat these simply as physically mixed systems (Junge, 1963), more recent results demonstrate clearly that both the chemical composition and chemical interactions of the tropospheric aerosol are strong and regular functions of particle size (Stevens et al., 1978). Most of the available data are from low altitudes in industrialized continental regions, but similar results are found in marine areas (Duce, Chapter 16, this volume).
*Aerosols are defined as suspensions in a gas of particles of liquid or solid material that are stable to either gravitational sedimentation or Brownian coagulation over some period of time. In the case of atmospheric aerosols, the relevant time scale is a fraction of an hour or longer. Thus, ordinary water clouds are aerosols; however, it is customary to designate water clouds separately as having a relative humidity over 100%. Fog may be defined as cloud in contact with the ground.
The mass or volume distributions of aerosols are consistent with the composition-size dependence and show that the particles have distinctly different chemical composition and morphology above and below 1 µm (Figures 4.1 and 4.2). The mass mode below 1 µm is often called the accumulation mode, because mass accumulates there due to condensation and coagulation. These same processes tend to mix internally the accumulation mode particles (i.e. each particle has some of each constituent). In contrast, the lack of condensation and coagulation of coarse mode particles, along with their mechanical origins, tends to leave these aerosols as an external mixture (i.e., individual particles may have different compositions). In addition, the coarse and accumulation modes are externally mixed with each other, and do not interact chemically to any known extent. Because of their chemical composition the sub-µm aerosols usually contain some liquid water in an aqueous phase.
Figure 4.1 The volume distributions of aerosols plotted as dV/d (log Dp) (linear) versus diameter (Dp) on a log scale. (Whitby and Sverdrup, 1980). Reproduced by permission of John Wiley & Sons, Inc.
The accumulation mode aerosols are to a large degree the result of interactions of C, N and S cycles, both within a condensed phase and via preceding gas-phase production reactions. From Crutzen's review of homogeneous reactions
(Chapter 3, this volume), gas phase production of H2SO4
(reactions R33
35) results either in nucleation with H2O of new particles of hydrated H2SO4 or in the condensation of H2SO4 and H2O
on the surfaces of pre-existing particles. Both of these possibilities are important. The former is a necessity for the creation of new particles in the absence of direct injection of particles into the atmosphere (e.g. from combustion). The latter results
in a build-up of the mass of sulphate compounds in the size class between 0.1 and 1 µm. Chemical reaction of NH3 with H2SO4 results in an aerosol of composition ranging from NH4HSO4 to neutralized
(NH4)2SO4. The reaction of
NO2 with OH produces HNO3, some of which may attach to or be dissolved in pre-existing aerosol particles.
HNO3 can be neutralized by NH3 forming NH4NO3 in the condensed phase of accumulation mode aerosols. Sulphate and nitrate combined with ammonium usually are the dominant inorganic species formed in the accumulation mode by direct gas-particle conversion. In addition, a wide variety of organic materials are often found in this same size range, although their total mass is usually considerably less than the mass of sulphates and nitrates, The gas-phase interactions discussed by Crutzen
(Chapter 3, this volume) thus have direct implications for the formation and composition of submicrometer aerosols.
Figure 4.2 A conceptual representation of the volume or mass distributions of aerosols as related to source, transformation and sink processes. Fine particulate matter also contains some primary emissions such as C (0) (elemental carbon) and Pb. Ordinate is as in Figure 4.1 (Shaw and Stevens, 1980), Reproduced by permission of New York Academy of Sciences
Besides such gas phase interactions, C, N, and S compounds interact within the condensed, aqueous phase of aerosols and clouds, with chemical reactions resulting in an increased mass of dissolved substances. In particular, the oxidation of SO2 in the liquid phase of clouds results in increased amounts of dissolved SO42-. Since most clouds evaporate and do not result in precipitation, the dissolved material is released back to the atmosphere in the accumulation mode of the aerosol. There are several known reaction mechanisms of SO2 and its dissociation products in the aqueous phase. Among the more likely are oxidation by O3 and H2O2 (Penkett et al., 1979) although oxidation by O2 may be of some importance. No single mechanism can be identified yet as the most important one.
The lifetimes in air of the two mass modes are also distinctly different, largely due to the different mechanisms of removal, Particles greater than several µm tend to be removed by sedimentation and usually have lifetimes of much less than a day, Particles below 1 µm diameter have very small sedimentation velocities (<10-2 cm s-1) and are removed from the air mainly by incorporation into cloud droplets and precipitation, As a result, their lifetime is dictated by the period between precipitation events, and typically is a few days to perhaps a few weeks in mid-latitudes. As a result of little, if any, extensive interaction of the gas phase with the coarse mode, there is little interaction of C, N and S cycles with particles much above ca, 1 µm in size. Although we will emphasize sub-µm particles, we note the importance to precipitation chemistry of below-cloud scavenging by rain of basic soil dust. We also leave open the question of coarse-particle interaction with NOx and HNO3.
Clouds of liquid water have droplets from ca 5 to 50 µm diameter, typically yielding liquid water contents of perhaps
0.1
0.5 g m-3;
some vigorously precipitating clouds may have water contents in excess of
0.5 g m-3. Fogs have somewhat lower liquid water contents, typically below
0.1 g m-3,
as well as somewhat smaller droplets. The water in clouds and fogs contains soluble salts from the remains of condensation nuclei, water soluble gases (e.g.
CO2, SO2, NH3, etc.) as well as suspended but insoluble materials (e.g. mineral grains and soot). The lifetime of an individual cloud droplet is often a fraction of an hour though several hours may be possible in fog. Since only a small fraction of clouds result in precipitation, aerosol particles take part in the
condensation
evaporation cycle many times before precipitation can remove them. In the physical process of cloud nucleation, the chemical property of water solubility of the nuclei is a dominant factor. Due to the solubility of the key compounds (ammonium sulphates and nitrates) the products of interaction of N and S cycles in the atmosphere are probably the dominant cloud condensation
nuclei. To illustrate the ways in which the cycles of C, N, and S influence each other within aerosols and clouds, we will select a limited family of interactions as useful examples. After choosing the system,
NH3
CO2
SO2-H2SO4
H2O(1),
we will examine the characteristics of the equilibria that control the interactions of the dissolved
species. We can then investigate chemical reactions that occur within this system in the presence of O2, O3, and H2O2. This allows consideration of the response of sulphate production in
aerosols and clouds to changes in the source strengths of
SO2 and NH3. The results allow an understanding of the nonlinearity of sulphate production in response to varying
SO2 strengths.
That the atmospheric cycles of C, N, and S interact within both aerosols and clouds is indicated by several observations:
Table 4.1 Typical composition of atmospheric aerosols, concentrations in µg m-3
|
|
||||
| a) Industrial Region* | ||||
| Specie or element | Concentration | |||
|
|
||||
| Diameter less than 2.5 µm | ||||
| SO42- | 1.0 |
|||
| Al | 0.008 |
|||
| As | 0.04 | |||
| Br | 0.01 |
|||
| C (graphitic) | 0 |
|||
| Cd | 0.02 |
|||
| Cl | 0.005 |
|||
| Cr | 0 |
|||
| Cu | 0.002 |
|||
| Fe | 0.02 |
|||
| K | 0.01 |
|||
| Mg | 0.006 |
|||
| Mn | 0.002 |
|||
| NH4+ | 0.5 |
|||
| Ni | 0.002 |
|||
| NO3- | 3.0 |
|||
| Pb | 0.5 |
|||
| Si | 0.06 |
|||
| Ti | 0.03 |
|||
| V | 0.004 |
|||
| Zn | 0.003-0.06 | |||
| Diameter greater than 2.5 µm | ||||
| Al | 0.3 |
|||
| Si | 1.0 |
|||
| P | 0.03 |
|||
| S | 0.2 |
|||
| Cl | 0.2 |
|||
| Ca | 0.4 |
|||
| Fe | 0.3 |
|||
|
|
||||
| *Adapted from Charlson et al. (1978) and Stevens et al., (1978). | ||||
| b) Background Aerosol† | ||||
|
|
||||
| Concentrations (µg m-3)
|
||||
| Specie | Continental boundary layer |
Marine boundary layer |
Free troposphere |
|
|
|
||||
| SO42- (excess)‡ | < 0.2 |
0.3 |
< 0.1 |
|
| NH4+ | 0.04 |
< 0.01 |
< 0.02 | |
|
|
||||
| †from Huebert and Lazrus (1980). | ||||
| ‡SO41- (excess) is the amount of SO42- remaining after the amount from sea-salt is subtracted | ||||
| based on either Na+ or Cl |
||||
Table 4.2 Example cloud water composition, µeq litre-1
|
|
||
| Mean of | Mean of | |
| Petrenchuk and | Scott and | |
| Specie | Drozdova (1966) | Laulainen (1979) |
|
|
||
| H+ | 100 | 150 |
| NH4+ | 800 | 430 |
| Na+ | 120 | 53 |
| K+ | 100 | 44 |
| Ca2+ | 400 | 90 |
| Mg2+ | 100 | 4 |
| SO42- | 1500 | 460 |
| NO3- | 90 | 330 |
| Cl- | 300 | 35 |
|
|
||
Table 4.3 Inorganic composition of rain and snow water, Forshult Station, Sweden
1975
1979 (incl)*
|
|
||
| Quantity | ± 25% range | |
|
|
||
| 21 | ||
| Amount of precipitation (mm) | 42 | 57 |
|
|
||
| Specie (µeq litre-1) | ||
|
|
||
| 49.8 | ||
| SO42- | 72.8 | 100.0 |
| 8.6 | ||
| Cl- | 13.5 | 19.8 |
| 12.6 | ||
| NO3- | 21.7 | 40.3 |
| 3.3 | ||
| NH4+ | 13.4 | 24.2 |
| 1.7 | ||
| K+ | 3.8 | 9.6 |
| 6.0 | ||
| Na+ | 11.8 | 18.0 |
| 5.8 | ||
| Mg2+ | 9.6 | 14.0 |
| 16.1 | ||
| Ca2+ | 22.1 | 39.5 |
| 25.1 | ||
| H+ (from pH) | 50.1 | 79.4 |
|
|
||
| *Data courtesy of R. Söderlund, IMI Network, Department of Meteorology, University of Stockholm, S-106 91 Stockholm, Sweden. | ||
Table 4.4 Gas Phase SO2, NH3, CO2*
|
|
|||
| Background | |||
| SO2 | Northern Hemisphere | ||
| Boundary Layer | 89 ± 69 ppt | ||
| Free Troposphere | 122 ± 85 | ||
| Southern Hemisphere | |||
| Boundary Layer | 57 ± 18 | ||
| Free Troposphere | 90 ± 21 | ||
| NH3 | Very uncertain | ||
| 100 |
|||
| 1-100 ppt (equilibrium with acidic, wet sulphate aerosols) | |||
| CO2 | 340 ppm | ||
| Industrial Region, Boundary Layer (estimates) | |||
| Away from | SO2 | 0.1 |
|
| sources | NH3 | 10-3 |
|
| CO2 | 340 |
||
| Close to | SO2 | up to 1 or a few ppm | |
| sources | NH3 | 10-3 |
|
| CO2 | 340 |
||
|
|
|||
| *Adapted from Maroulis et al. (1980) and Lau and Charlson (1977)., | |||
Collectively, these interactions play significant roles in controlling the molecular form of the aerosol particles as well as the ionic species present in rain and snow water.
The sub-µm sulphate aerosol often exhibits the chemical features of a single compound. For example, some particle samples show deliquescence and X-ray diffraction of pure (NH4)2SO4 (Charlson et al., 1978) or the volatility of H2SO4 at ca. 125°C (Coburn et al., 1980) Since there are no known direct sources of fine-particle (NH4)2SO4, its existence also demonstrates the simplest interactions of the S and N cycles in the atmosphere. This also indicates the sub-µm aerosol particles containing deliquescent salts (e.g. NH4NO3, NH4HSO4, (NH4)2SO4) or hygroscopic liquid (e.g. H2SO4) understandably also contain liquid water. At 80% R.H., taking Raoult's law as a means of approximating the composition, such particles would be 80 mole percent water and 20 mole percent dissolved species. Hence at R.H. < 90 or 95%, the aqueous phase of such particles is sufficiently concentrated that non-ideal behaviour will occur.
The calculations presented in this paper are for water solutions that behave ideally. Extension to non-ideal solutions is not included, but the general tendency will be for the concentration of dissolved gaseous species to decrease (salting-out effect) and for ionic forms to increase since their activity coefficients will be substantially less than unity.
Figure 4.3 Matrix of potential interactions of C, N and S in air defined by oxidation state. Elemental sulphur is omitted because it is not known to occur in air. The shaded corner (SO42-, SO2, CO2, NH3, and RNH2) will be treated in section 4.4
In order to explore objectively the range of interactions, we consider the various C, N and S compounds that exist in tropospheric air. Figure 4.3 depicts a three-dimensional matrix of the oxidation states and species that are involved. Because COS reacts on time scales of years (Johnson, 1981) and because H2S and RSH (mercaptans) are expected to react fairly rapidly to SO2, oxidation states IV and VI of sulphur are of primary interest. Neither N2 nor N2O react on or in particles, nor does CO.
Thus, we can focus on interactions of S(IV) and S(VI) with organic C,
CO2, NH3, NO, NO2, HNO2, HNO3 and H2O(1). These are represented qualitatively in
Figures 4.4 and 4.5 for
S(IV) and S(VI) respectively. Here we assume that NO oxidizes to
NO2 before any interactions with C or S in particles, and we further assume that
NO2 produces HNO3 and HNO2 upon incorporation in hydrated particles. For convenience we list all organic compounds as
C(
IV).
The most common interactions are acid equilibria, gas
liquid exchanges and the influence of NH3 or amines as bases neutralizing weak or strong acids. A potential source of gas phase HNO3 is its volatilization that may be caused if sufficient H2SO4 is added to a particle, e. g. by photochemical production. Since
S(IV) and S(VI) coexist in the same particles, acid
base equilibria are clearly sensitive to the proportions of the weak and strong acids that are present. Because the rate of oxidation of
S(IV) to S(VI) depends on which dissolved species are present, it is necessary to consider the equilibria that are involved.
Figure 4.4 Interactions of S(IV) with C and N in wet particles. Note: (1) Acid equilibria occur in all nine cases. (2) Catalytic oxidation of S(IV) by C(O) may occur independently of the presence of any N species
Figure 4.5 Interactions of S(VI) with C and N in wet particles. Note: (1) Volatilization of HNO3 probably occurs under acidic conditions independent of the presence of some C species (Tang, 1980). (2) Neutralization of H2SO4 by NH3 is probably independent of C
In order to approach a complete list of factors controlling the equilibrium, we might include the components used by Liljestrand and Morgan (1981): SO2, NO, NO2, HNO2, HNO3 NH3, HCl, H2SO4, CO2, kaolinite, Al(OH)3 and H2O(1). However, it is instructive at this stage to limit this discussion to the simpler system SO2, CO2, NH3, H2SO4 and H2O(1) (Figure 4.3, shaded corner). This may be justified for understanding the chemistry of these components alone, and may be further justified to the extent that there are atmospheric situations in which the other components are present in concentrations that are low enough to be neglected.
Chemical equilibrium of gaseous SO2, CO2 and NH3 with wet particles of less than 5 µm diameter occurs in less than a few seconds (Freiberg and Schwartz, 1981). Thus, multiple equilibrium expressions can be used to approximate the overall composition that results from the weak acid/weak base interactions that occur along with the existence of strong acids such as H2SO4 (Liljestrand and Morgan, 1981). This step is a necessary prelude to examining the oxidation of S(IV) in solution, a discussion of which follows in section 4.5. The equilibrium concentrations can be calculated numerically; however, they also may be presented graphically, a form which reveals more clearly the interrelations of the many constituents.
Table 4.5 lists the relevant expressions and constants that were used to construct the log concentration versus pH diagrams
(Sillén, 1967) in Figures 4.6
4.8 and further used for the oxidation computations in
section 4.5. In addition, Table 4.6 gives the partitioning of SO2, and NH3 between liquid and gas phases in clouds and fog.
Figures 4.6
4.8 are the simplest representation of a master variable diagram
(Sillén, 1967) in which the concentration of each species is given as a function of a master variable, in this case, pH. The nine equilibrium expressions of
Table 4.5 first can be put into logarithmic form, resulting in nine linear equations. The three Henry's law expressions (Equations (2), (5), and (7)) yield aqueous concentrations of SO2
• H2O, NH3•H2O and CO2•H2O that are independent of pH and are governed by the gas phase equilibrium pressure of each gaseous species. These result in values represented by three lines parallel to the pH axis.
The remaining six equations can be solved to yield linear expressions for the concentration of each dissociated species as a function of pH, giving six more lines. A seventh line is
log[H+] = pH, and [SO42-] is included as a pH-independent quantity. The equilibrium condition is depicted by the pH at which the sum of the positive ions is equal to the sum of the negative ions. At this pH, the equilibrium concentrations of the other species are also graphically depicted. We caution that these plots do not include equations of mass balance and hence apply only at the equilibrium condition. Each plot expresses one solution to the equations for a particular set of data and therefore must not be interpreted literally as dynamic diagrams in which processes can be studied.
The three example conditions depicted in Figures 4.6
4.8 were selected to represent a range of concentrations of SO2, NH3, [SO42-] and liquid H2O as might be found in actual cases;
CO2 is constant at 340 ppmv. The equilibrium conditions in Figure 4.6 are intended to represent an industrial region and have been selected as the initial condition for some of the oxidation calculations of
section 4.5. The initial (SO42-) level of 3 ppbv and
SO42- of 5 µg m-3
represents a polluted industrial location that is well removed from the immediate influence of sources. The bulk of the
(NH4+) was initially contained in nuclei of condensation
((NH4)2SO4) and the liquid water content reached in this activated cloud is 0.5 g m-3.
The resulting equilibrium partial pressure of NH3 is only 7
pptv, due to the acidity of the solution.
Table 4.5 Values of constants used
|
|
|||||
| Equilibrium | Equilibrium constant | Value at 5°C | Reference | ||
|
|
|||||
| (1) | H2O H+ + OH |
Kw = [H+][OH |
1.82 x 10-15 mol2 litre-2 | Yui (1940) | |
| Robinson and Stokes (1959) | |||||
| (2) | SO2(g) + H2O SO2 . H2O | KHS = | PCO2 [SO2 . H2O] |
0.379 atm litre mol-1 | Johnstone and Leppla (1934) Lowell et al. (1970) |
| (3) | SO2 . H2O
H+ +
HSO3 |
K1S= | [H+][HSO3 [SO2 . H2O] |
0.0206 mol litre-1 | Lowell
et al. (1970) Yui (1940) |
| (4) | HSO3 |
K2S = | [H+][SO32 [HSO3 |
8.88 x 10-8 mol litre-1 | Lowell et al. (1970) Yui (1940) |
| (5) | NH3(g) + H2O NH3 . H2O | KHN = | PNH3 [NH3 . H2O] |
7.11 x 10-3 atm litre mole-1 | Morgan and Maass (1931) Freiberg (1974) |
| (6) | NH3 + H2O
NH4+ + OH |
Kb = | [NH4 [NH3 . H2O] |
1.5 x 10-5 mol litre-1 | Yui (1940) Freiberg (1974) |
| (7) | CO2(g) + H2OCO2 . H2O | KHC = | PCO2 [CO2 . H2O] |
16.6 atm litre mol-1 | Robinson and Stokes (1959) Morgan and Maass (1931) |
| (8) | CO2 . H2O
H+ + HCO3 |
K1C | [H+][CO3 [CO2 . H2O] |
2.94 x 10-7 mol litre-1 | Yui (1940) Robinson and Stokes (1959) |
| (9) | HCO3 |
K2C = | [H+][CO32 [HCO3 |
2.74 x 10-11 mol litre-1 | Yui (1940) Robinson and Stokes (1959) |
|
|
|||||
Figure 4.6 Industrial region. The equilibrium pH of the system is determined at the point of charge balance (O). At that pH, the concentrations of other species are also given for the equilibrium conditions. We caution that these plots do not include equations of mass conservation and thus strictly apply only at the equilibrium pH. Assumptions:
aerosol (SO24 ) |
= 5.0 µg m-3 | ||
| liquid water | = 0.5 g m-3 | ||
| aerosol (NH4+) | = 1.7 µg m-3 | ||
| PSO2 | = 3 ppbv; 7.86 µg m-3 | ||
| Calculated: PNH3 | = 7.1 x 10-12 atm = 5 x 10-3 µg m-3 | ||
| pH | = 4.6 |
For comparison to the hypothetical case of Figure 4.6, we can consider the composition of rain-water from an actual site downwind of an industrial region. Here we assume that rain-water has a composition similar to and governed by the composition of the clouds from which it fell. Figure 4.7 is based on 5 years of precipitation chemistry data from Forshult, Sweden (Table 4.3) with the assumption of an SO2 concentration of 1 ppbv. This case might be termed a cloud in well-aged industrial or continental air.
Figure
4.7 Forshult (Sweden) precipitation 1975
1979. Assumptions:
| PCO2 = 330 ppmv | ||
| PSO2 = 1 ppbv | ||
| 2[SO2-] + [Cl-] + [NO3-] = 108 µeq litre-1 | ||
| 2[Ca2+] + 2[Mg2+] + [K+] + [Na+] = 47 µeq litre-1 | ||
| pH = 4.3 | ||
| calculated: | ||
| PNH3 = 0.23 pptv | ||
| Note: [SO32-] and [CO32-] are omitted for simplicity | ||
Finally, Figure 4.8 represents a clean background case, either in the boundary layer or free troposphere. The total SO2 concentrations, i.e. SO2 (gas) plus SO2 (dissolved), are representative of remote locations in the northern hemisphere (Maroulis et al., 1980). Recent data for sulphate aerosol in remote locations indicate sulphate concentrations of 0.1 to 1 µg per standard cubic meter with molar ratios of (NH4+) to SO42- between 1 and 2. The [NH4+]/[H+] of 2 was picked arbitrarily for this example.
Several general features are evident in these figures, the equilibrium expressions in Table 4.5, and the partition expressions in Table 4.6:
in a cloud
decreases as hydrogen ion in the cloud water increases, regardless of oxidation mechanism. (This presumes reaction rates for
HSO3
or SO32
comparable to or greater than for
SO2.H2O).
) as in
Figure 4.8. Even then it is not dominant.
, even in the presence of realistic amounts of (SO42-) (Hales and Dana,
1979).Figure 4.8 Background cloud. Assumptions: Liquid water content = 0.5 g m-3
|
T = 5C |
|
| [NH4+]/[H+] =2 | |
Mass concentration (SO42 )
= 0.1 to 1.0 µg m-3 |
|
| PNH3 = 1.6 X 10-12 atm (10-3 µg m-3) | |
| PSO2= 0.1 ppbv (0.26 µg m-3) | |
At (SO42 ) = 0.1 µg m-3 pH =
5.6 NH4+ (aq) = 0.05 µg m-3 |
|
| S (IV) (aq) = 0.06 µg m-3 | |
At (SO42 ) = 1 µg
m-3 pH = 4.95 NH4+ (aq) = 0.2 µg m-3 |
|
| S(IV) (aq) = 0.013 µg m-3 | |
Note: [SO32 ] and [CO32 ] are omitted for simplicity |
|
Given this set of equilibrium conditions, it is now possible to consider chemical reactions that occur within the liquid phase. In doing so, we want to emphasize the ways in which ammonia and pH influence the reaction rates. A major goal in doing this is to study the overall response of the amounts of reaction products (e.g. (SO42-) to changes in the inputs of reactants (SO2).
Table 4.6 Partitioning* of SO2 and NH3 between liquid and gas phases as functions of liquid water content, L, and [H+]
| (SO2) | ||||||
|
|
||||||
|
L (gm-3) = 0.5 |
0.1 | 0.01 | ||||
|
|
||||||
| [H+] | SO2† | SO2 | SO2 | |||
|
|
||||||
| 10-6 | 0.6 | 0.1 | 0.01 | |||
| 10-5 | 0.06 | 0.01 | 10-3 | |||
| 10-4 | 6 X 10-3 | 10-3 | 10-4 | |||
|
|
||||||
| NH3 | L (gm-3) = 0.5 | 0.1 | 0.01 | |||
|
|
||||||
| [H+] | NH3‡ | NH3 | NH3 | |||
|
|
||||||
| 10-6 | 10 | 3 | 0.3 | |||
| 10-5 | 102 | 30 | 3 | |||
| 10-4 | 103 | 300 | 30 | |||
|
|
||||||
| *x is the ratio of moles of a soluble gas in the liquid phase to the moles in the gas phase for a given cloud volume. In general it is given as: | ||||||
|
x= |
L[x]RT Px |
| †SO2
|
LK1SRT [H+]KHS |
for pH <6 |
| ‡NH3= | LKb[H+]RT KHNKw |
|
One of the outstanding practical problems of atmospheric chemistry is to be able to understand and to predict the response of chemical processes in the atmosphere to increases or decreases of input materials. In the case of the system in section 4.4, we would like to know what happens to the composition of cloud and rain-water when SO2. sources are increased (e.g. due to industrial development) or decreased (e.g. when controls are instigated). Not only must we consider the changes in equilibria, we also must include the effects of chemical reaction.
We have already seen in Chapter 3 (Crutzen, this volume) the possibility of delays in the oxidation of SO2. These may be due to effective competition by NO2 for OH radicals in the gas phase (reaction R10) or by decreases in H2O2 and subsequent decrease in oxidation of SO2 in cloud-water caused by competition for HO2 radicals by NO (reaction R5 followed by R36). Such interactions of NOx with the oxidation of SO2 would cause some SO2 to be transported farther before being oxidized and deposited in rain-water, possibly leading to increases in the area of regions influenced by acid precipitation. Besides such gas phase interactions, shifts of equilibria in the liquid phase can lead to similar effects.
It is well established that S(IV) is easily oxidized in aqueous solutions. Models of the oxidation of SO2 in clouds have been developed that include oxidation by O2 (Scott and Hobbs, 1967; Easter and Hobbs, 1974; Hegg and Hobbs, 1979). Other models simply treat the oxidation rate as an input parameter, typically in the range of a few to several percent per hour (see e.g. Scott, 1981). Considerable effort has been expended on studies of various liquid-phase reaction mechanisms, including oxidation by O2, O3, and H2O2 and catalysis by metal ions as well as the role of mass transport of gases within clouds (Freiberg and Schwartz, 1981). Table 4.7 lists the reaction mechanisms we include in our calculations.
As noted numerous times in the literature, the oxidation rates show dependences on pH and on NH3. The sense of this dependence is that the rate of conversion of S(IV) to S(VI) decreases as the aqueous phase becomes acidic. Thus a reaction product, H2SO4, tends to decrease the rate of reaction indicated earlier for the case of the effect of gas phase reactions of NOx, acidification of cloud water by the production of H2SO4 should also delay the oxidation of SO2. To explore the role of this pH dependence, we will calculate the rate of production of SO42- in a cloud as a function of the SO42- source strength. Although they are clearly important, we neglect entirely any gas phase reactions. The purpose of this section is not to study liquid-phase oxidation mechanisms, but rather to use the mechanisms that have been proposed to address the question of the relationship of SO42- production rates in cloud-water to SO42- source strengths. We are particularly interested in determining the response of SO42- production to SO42- source strengths, the nature of the responses (e.g., linear versus nonlinear) and to what degree this depends on NH3. We herein include a brief description of our model and qualitative results; the model will be presented in detail elsewhere (Taylor et al., in preparation).
The presence of ambient ammonia or other basic gases or particles increases the liquid-phase oxidation rate (Junge and Ryan, 1958; Scott and Hobbs, 1967) by neutralizing the pH as acid sulphates are formed. The concentration of ammonia in the gas phase has such a large effect on the rate and total amount of oxidation (Easter and Hobbs, 1974; Adamowicz, 1979; Overton et al., 1979) that ammonia concentrations and source rates must be studied along with SO42- concentrations and source rates in any attempt to understand the effect of varying these parameters on SO42- production.
Table 4.7 Oxidation mechanisms
|
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|
Rate Equation |
Constants at 5°C |
Reference |
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||||
| (1) |
d[SO4= ] |
(O2)= k1 + k2 [H+]0.5[SO32-] | kl = 2.2 x 10-2 min-1 k2 =4.3 x 102 litre0.5 mol-0.5 min-1 |
Larson et al. |
| (2) |
d[SO4= ] |
(O3) = kO3KHO3PO3[HSO3-][H+]-0.38 | kO3 = 1.2 x 106 litre0.62 min-1 kHO3=2.00 x 10-2 mol litre-1 atm-1 |
Penkett et al. |
| (3) |
d[SO4= ] |
(H2O2) = kH2O2 [H2O2][S(IV)] | kH2O2= 4.0 x 104 litre mol-1 min-1(pH = 4.3) |
Penkett et al. |
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There is no general acceptance as to the ambient air concentration of NH3 (Lau and Charlson, 1977; Hales and Drewes, 1979), and there are also major questions as to source strengths of NH3. Söderlund and Svensson (1976) could only account for approximately one-quarter of the NH3 sources that are needed to balance the global NH3 cycle. We therefore include a source of ammonia as a variable parameter in our model and make no attempt to analyse or justify the relationship between NH3 and SO2 emission rates.
Our calculations were done using a simple box model of uniform wet haze at 5°C. The box is a closed system except for sources of SO2 and NH3 which are assumed to be instantaneously and uniformly mixed. The box has dimensions 1 km x 1 km x 1 km and there are no advection or sink terms. The liquid water content of the haze is determined by the choices of initial sulphate aerosol concentration, size and sulphate composition of the condensation nuclei (CN), the fraction of total sulphate used as CN, and the supersaturation. To simplify the calculation only one form of sulphate ((NH4)2SO4) and one composition and size of CN are used, resulting in only one size droplets. All droplets have the same concentration of SO42- and associated cations. Also for simplicity all SO42- in the initial calculations is assumed to be in the CN.
The droplet equilibrium size is determined by the standard Köhler curve equation. We chose to use the equilibrium size before activation and to keep the droplet the same size throughout the oxidation process (this is an approximation that is true only if the increase in mass of the droplet remains small). The chemical composition of the CN is impure (NH4)2SO4; however, its effect on the equilibrium droplet size is approximated as if it were pure (NH4)2SO4. The impurities are assumed to be chemically inert. The parameters remaining that must be defined are the supersaturation and the mass of the CN, and they in turn determine the resulting liquid water content, L, and the initial concentration of NH4+ and SO42- in the liquid water.
Our values of 3.0 µm for the droplet radii and 0.01 g m-3 for the liquid water content seem reasonable when compared to measurements made by Garland et al. (1973). In choosing one size droplet to comprise the entire liquid water content of the system, 3.0 µm gives a reasonable number of droplets and liquid water content for a high humidity haze. The liquid water content measured by Garland et al. (1973) was 0.05 g m-3 40 minutes after the onset of the fog, so 0.01 g m-3 would seem reasonable for earlier in a developing fog or haze. Clearly, our assumption that the droplets do not grow must be considered only a first approximation, taken to avoid the complexity of the cloud droplet growth equations. We also consider higher liquid water content later in order to assess the sensitivity of the model to this parameter.
The pressures of gas that initially come into contact with the above droplets
are 3 ppb SO2, 330 ppm
CO2 and a variable amount of ammonia (0.1
10 ppb). For any given condition the total amount of NH3 and
NH4+ is
constant. The resulting equilibrium concentrations are found by simultaneously solving the equations for
PSO2,PNH3 and [H+] from Table
4.5,
and taking into account that total nitrogen will include the [NH4+] from
the CN as well as from NH3(g).
Oxidation rate calculations were carried out using the mechanisms listed in Table 4.7 and starting with the above initial conditions (time = 0). The oxidation proceeded for 30 minutes, a typical lifetime for a cloud droplet, after which the composition changes were assessed. The oxidation of S(IV) to S(VI) is assumed to be the rate determining step and considered to be irreversible.
The concentration of ozone was held constant at 50 ppb during the oxidation. The concentration of hydrogen peroxide was 0.3 ppb, all of which dissolved in the water to give a concentration of 1.3 x 10-3 mole litre-1. H2O2 was depleted during oxidation and was solved simultaneously with the other differential equations.
|
d[H2O2 ] |
= kH2O2[H2O2][S(IV)] |
where [H2O2] = |
PH2O2 LRT |
The amount of sulphate produced per cubic meter of fog or cloud by these
oxidation mechanisms was evaluated for nine different SO2 source rates
(QSO2). Initial levels of NH3 (0.1, 1.0 and 10 ppb) and a source strength of 4.5
10-4 kg km-2 min-1 were used for three separate cases. An
ammonia source strength of 4.5
10-5
kg km-2 min-1 and a source strength of NH3 proportional to that of SO2 provide two more cases.
These first five cases had liquid water contents of 0.01 g m-3, while the
sixth case had 0.5 g m-3.
Figure 4.9 shows the influence of the initial amounts of NH3, with increasing
amounts of sulphate produced with increasing initial NH3. As expected, the
amount of sulphate produced is a nonlinear function of QSO2.
Figure 4.10
compares the cases of fixed QNH3 with one where NH3 sources are proportional
to sources of SO2. This might be the case, for instance, where NH3 is used as a
fertilizer in the same region where SO2 is produced. Here, the amount of
SO42- produced is a nonlinear function of QSO2
in the opposite sense
that is positive as opposed to negative feedback occurs.
Figure 4.11
compares production rates of SO42- for liquid water contents of 0.01 and
0.5 g m-3 with the initial values and source strength of NH3 as used
previously (Case 1). Here, more SO42- is produced at the higher liquid water content while the nonlinear behaviour is preserved.
| Figure 4.9 Amount of sulphate produced (µg m-3) in model fog of 0.01 g m-3 liquid water in 30 minutes versus source strength of SO2 (QSO2) kg km-2 min-1. Other parameters: | ||
| Case 1: | PNH3 (t=0) = 0.1 ppb | |
| QNH3 = 4.5 |
||
| PSO2 (t=0) = 3 ppb | ||
| Case 2: | PNH3 (t=0) = 1.0 ppb | |
| QNH3 = 4.5 |
||
| Case 3: | PNH3 (t=0) = 10 ppb | |
| QNH3 = 4.5 |
||
The major goals of this approach are to quantify the relationships between fluxes and reaction rates and to explore departures from linearity. However, before this can be done, it is clearly necessary to identify key pathways and to establish the sensitivities of the cycles to key variables. The use of simple, diagnostic models make it possible to ascertain at least some of the controlling factors. However, we caution that this kind of model is only diagnostic and not well suited for predictive applications. Perhaps the most important outcome at this stage is that the results from the model will guide further modelling exercises and will suggest the important variables that need to be measured. Among the conclusions at this stage are:
| Figure 4.10 The same as Figure 4.9, except: | ||
| Case 4: | PNH3 (t=0) = 0.1 ppb | |
| QNH3 = 4.5 x 10-5 kg km-2 min-1 | ||
| Case 5: | PNH3 (t=0) = 0.1 ppb | |
| QNH3 = 0.27 QSO2 | ||
| Figure 4.11 The same as Figure 4.9, except: | ||
| Case 6: | L (liquid water content) = 0.5g m-3 | |
| PNH3 (t=0) = 0.1 ppb | ||
| QNH3 = 4.5 |
||
These results are consistent with the observations of Altshuller (1976, 1980) that reductions in local SO2 emissions in the Eastern and Midwestern U.S.A. between 1963 and 1972 caused only modest reductions in sulphate aerosol concentration. Data collected in 1974 in Europe (LRTAP) similarly showed a possible nonlinear relationship of sulphate in rain-water as a function of total sulphur (SO2 and SO42-) (OECD, 1977). In their cloud model, Easter and Hobbs (1974) found, using several oxidation mechanisms, that sulphate production decreased as initial SO2 rose above 10 ppb. This is also consistent with the lack of a clear-cut trend of decreasing pH in rain in recent years in Scandinavia (Granat, 1978).
Since oxidation of sulphur dioxide is considered to be the major source of sulphate aerosols (Gartrell and Friedlander,1975; Yuen et al., 1979) as well as the major source of acid precipitation and since reaction in aerosol and cloud particles seems to be possible or probable (Hegg and Hobbs, 1978, 1979) it is worthwhile to develop a more complete and quantitative understanding of these interactions. We fully can expect these interactions to be nonlinear due to both homogeneous gas-phase reactions and heterogeneous cloud and aerosol reactions. The expected nonlinearity in both cases is a slowing-down or delay of the oxidation of SO2 as SO2 and NO sources increase. However, the degree of nonlinearity is not known at this time, resulting in uncertainties in the effectiveness of various control strategies.
Financial support was provided by the International Meteorological Institute in Stockholm and also by the National Science Foundation, under Grant ATM 7808163. Special thanks are due to Professor Bert Bolin for suggesting the topic, and Professors Henning Rodhe, Peter Liss, Robert Duce, Dr. Rolf Söderlund and Dr. Robert Cook for helpful discussions.
Altshuller, A. P. (1976) Regional transport and transformation of sulphur dioxide to sulphates in the U.S., J. Air Pollut. Cont. Ass., 26, 318-324.
Altshuller, A. P. (1980) Seasonal and episodic trends in sulphate concentrations (1963Charlson, R. J., Covert, D. S., Larson, T. V., and Waggoner, A. P. (1978) Chemical properties of tropospheric sulphur aerosols, Atmos. Environ.,12, 39-53.
Coborn, W. G., Djukic-Husar, J., and Husar, R. B. (1980) Monitoring of sulphuric acid episodes in St. Louis, Missouri, J. Geophys. Res., 85(C8), 4487-4494.
Crutzen, P., Atmospheric interactions
homogeneous gas phase reactions, Chapter
3, this volume.
Easter, R. C., and Hobbs, P. V. (1974) The formation of sulphates and the enhancement of clouds condensation nuclei in clouds, J. Atmos. Sci., 31,1586-1594.
Freiberg, J. E. (1974) Effects of relative humidity and temperature on iron catalyzed oxidation of SO2 in atmospheric aerosols, Environ. Sci. Technol, 8, 731-734.
Freiberg, J. E., and Schwartz, S. E. (1981) Oxidation of SO2 in aqueous droplets: mass-transport limitation in laboratory studies and the ambient atmosphere, Atmos. Environ., 15, 1145-1154.Garland, J. A., Branson, J. R., and Cox, L. C. (1973) A study of the contribution of pollution to visibility in a radiative fog, Atmos. Environ., 7, 1079-1092.
Gartrell, G. Jr, and Friedlander, S. K. (1975) Relating particulate pollution sources: the 1972 California Aerosol Characterization Study, Atmos. Environ., 9, 279-299.Granat, L. (1978) Sulphate in precipitation as observed by the European Atmospheric Chemistry Network, Atmos. Environ., 12, 413-424.
Hales, J. M., and Dana, M. T. (1979) Regional-scale deposition of sulphur dioxide by precipitation scavenging, Atmos. Environ., 13, 1121-1132.Hales, J. M., and Drewes, D. R. (1979) Solubility of ammonia in water at low concentrations, Atmos Environ., 13, 1133-1147.
Hegg, D. A., and Hobbs, P. V. (1978) Oxidation of sulphur dioxide in aqueous systems with particular reference to the atmosphere, Atmos. Environ., 12, 241-253.Hegg, D. A., and Hobbs, P. V. (1979) The homogeneous oxidation of sulphur dioxide in cloud droplets, Atmos. Environ., 13, 981-988.
Huebert, B. J., and Lazrus, A. L. (1980) Bulk composition of aerosols in the remote troposphere, J. Geophys. Res., 85, 7337-7344.Johnson, J. E. (1981) The lifetime of carbonyl sulphide in the troposphere, Geophys. Res. Lett., 8, 938-940.
Johnstone, H. F., and Leppla, P. W. (1934) The solubility of sulphur dioxide at low pressures, J. Am. Chem. Soc., 56, 2233-2238.Junge, C. E., and Ryan, T. G. (1958) Study of SO2 oxidation in solution and its role in atmospheric chemistry, Q. J. R. Met. Soc., 54, 46-55.
Junge, C. E. (1963) Air Chemistry and Radioactivity, New York, Academic Press.Kok, G. L. (1980) Measurements of hydrogen peroxide in rainwater, Atmos. Environ., 14, 653-656.
Larson, T. V., Horike, N. R., and Harrison, H. (1978) Oxidation of sulphur dioxide by oxygen and ozone in aqueous solution: a kinetic study with significance to atmospheric rate processes, Atmos. Environ., 12, 1597-1611.Lau, N., and Charlson, R. J. (1977) On the discrepancy between background atmospheric ammonia measurements and the existence of acid sulphate as a dominant atmospheric aerosol, Atmos. Environ., 11, 475-478.
Liljestrand, H. M., and Morgan, J. J. (1981) Spatial variations of acid precipitation in Southern California, Environ. Sci. Technol. 15, 333-339.Lowell, D. S. et al. (1970) A theoretical description of the limestone injection-wet scrubbing process. National Technical Information Service Publication, Vol. I, No. Pb 193-029.
Maroulis, P. J., Torres, A. L., Goldberg, A. B., and Bandy, A. R. (1980) Atmospheric SO2 measurements on Project Gametag, J. Geophys. Res., 85, 7345-7349.Morgan, O. M., and Maass, O. (1931) An investigation of the equilibrium existing in
gas
water systems forming electrolytes,
Can. J. Res., 5,162-199.
Overton, J. H. Jr., Viney, P. A., and Durham, J. L. (1979) Production of sulphate in rain and raindrops in polluted atmospheres, Atmos. Environ., 13, 355-367.
Penkett, S. A., Jones, B. M., Brice, K. A., and Eggleton, A. E. (1979) The importance of atmospheric ozone and hydrogen peroxide in oxidizing sulphur dioxide in clouds and rainwater, Atmos. Environ., 13, 132-137.
Petrenchuk, O., and Drozdova, V. M. (1966) On the chemical composition of cloud water, Tellus, 18, 280-286.Robinson, R. A., and Stokes, R. H. (1959) Electrolytic Solutions, Butterworths, London, 559.
Scott, B. C. (1981) Predictions of in-cloud conversion rates of SO2 to SO4 based upon a simple chemical and kinematic storm model. Battelle Pacific Northwest Laboratory, PNL-S 8053
8, Richland, WA.
Scott, B. C., and Laulainen, N. S. (1979) On the concentration of sulphate in precipitation, J. Appl. Meteorol., 18, 138-147.
Scott, W. D., and Hobbs, P. V. (1967) The formation of sulphate in water droplets, J. Atmos. Sci., 24, 54-57.Shaw, R. W., and Stevens, R. K. (1980) Trace element abundances and chemistry of atmospheric aerosols: current techniques and future possibilities. Ann. New York Acad. Sci., 338, 13-25.
Shaw R. W., and Rodhe, H. (1981) Non-photochemical oxidation of SO2 in regionally polluted air during winter. Report CMSillén, L. G. (1967) Master Variables and Activity Scales, in Gould, R. F. (ed.) Equilibrium Concepts in Natural Water Systems, Advances in Chemistry Series No. 67, Washington, American Chemical Society, 45-56.
Söderlund, R., and Svensson, B. H. (1976) The global nitrogen cycle, in Svensson, B. H. and Söderlund, R. (eds) Nitrogen, Phosphorus, and Sulphur
Global Cycles, SCOPE Report No. 7, Ecol. Bull. (Stockholm), 22,
23-73.
Stevens, R. K., Dzubay, T. G., Russworm, G., and Rickel, D. (1978) Sampling and analysis of atmospheric sulphate and related species, Atmos. Environ.,12, 56-68.
Tang, I. M. (1980) On the equilibrium partial pressures of nitric acid and ammonia in the atmosphere, Atmos. Environ., 14, 819-828.
Taylor, G. S., Baker, M. B., and Charlson, R. J. (19XX) Non-linearity of Sulphate Production in Cloud as a Function of SO2 Source Strength. Manuscript in preparation, University of Washington, FC-05, Seattle, WA 98195, USA.Whitby, K. T., and Sverdrup, G. (1980) California Aerosols: Their Physical and Chemical Characteristics, in Hidy, G. M., et al. (eds) The Character and Origins of Smog Aerosols, New York, Wiley Interscience, 499.
Yuen, T. S., Harrison, H., Charlson, R. J., and Baker, M. B. (1979) The global sulphur box model, Atmos. Environ., 13, 1351-1360.Yui, T. (1940) On the electrolytic dissociation constant of sulphurous acid, Tokyo Inst. Phys. Chem. Res. Bull., 19, 1229-1236.
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