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Appendix
Atmospheric Deposition
Processes
1. INTRODUCTION
In this appendix we present an overview of current
scientific understanding about deposition phenomena, with
the objectives of identifying key literature sources on
this subject and providing the reader with the technical
basis necessary for effective evaluation of the available
literature. There are several important features of this
subject, which should be noted at the outset. First, the
ultimate deposition processes of interest are the end
products of a complex sequence of atmospheric phenomena
(cf. Figure 2.1). Deposition processes tend to reflect
these preceding events strongly. Much of the material
presented in this appendix therefore necessarily deals
with the predeposition processes, which may act as
important rate-influencing steps in the overall
source-deposition sequence.
A second important feature of initial interest is the
relative difference in states of our current understanding
of wet- and dry-deposition phenomena. Wet deposition is
comparatively simple to measure. As a consequence there
exists a substantial and growing base of data on wet
deposition from a variety of networks and field studies.
Precipitation processes tend to be rather complicated,
however, and currently a high level of uncertainty exists
regarding their mathematical characterization.
Dry deposition, on the other hand, tends to be
extremely difficult to measure, and the corresponding
data set is relatively meager. Partly because of this
fact most mathematical characterizations of dry-
deposition processes have been quite simple in form. The
tendency toward simplicity in most mathematical char-
acterizations of dry deposition should not be taken to
213
OCR for page 214
214
imply that the physical processes themelves are simple.
As a consequence of these differences the following sec-
tions on dry and wet deposition have somewhat different
formats, with emphasis in each placed on areas of current
major activity.
Finally, it should be noted that very little of the
material presented in this appendix is new. A number of
reviews of both wet and dry deposition have been presented
during recent years, and the current treatment is merely
an attempt to consolidate these efforts.* In view of this
tendency toward redundancy, it is strongly recommended
that the reader proceed directly to the indicated journal
literature if more detailed pursuit of this subject is
desired.
2. DRY-DEPOSITION PROCESSES
2.1 MECHANISMS OF DRY DEPOSITION
2.1.1 Introduction
The rate of transfer of pollutants between the air and
exposed surfaces is controlled by a wide range of
chemical, physical, and biological factors, which vary in
their relative importance according to the nature and
state of the surface, the characteristics of the pol-
lutant, and the state of the atmosphere. The complexity
of the individual processes involved and the variety of
possible interactions among them combine to prohibit easy
generalization; nevertheless, a Deposition velocity,"
Vd, analogous to a gravitational falling speed, is of
considerable use. In practice, knowledge of vd enables
fluxes, F. to be estimated from airborne concentrations,
C, as the simple product, vd. C.
*Much of the material presented in this appendix was
prepared by Drs. B.B. Hicks and J.M. Hales as a
contribution to the Critical Assessment Document on
Acidic Deposition being prepared by North Carolina State
University under a cooperative agreement with the U.S.
Environmental Protection Agency. These contributions are
published here with permission of the authors and the
concurrence of the editors of the Critical Assessment
Document, Drs. A.P. Altschuller and R.A. Linthurst.
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215
Particles larger than about 20-pm diameter will be
deposited at a rate that is controlled by Stokes law,
although with some enhancement due to inertial impaction
of particles transported to near the surface in turbulent
eddies. The settling of submicrometer-sized particles in
air is sufficiently slow that turbulent transfer tends to
dominate, but the net flux is often limited by the
presence of a quasi-laminar layer adjacent to the
surface, which presents a considerable barrier to all
mass fluxes and especially to gases with very low
molecular diff.,civi~=
~ a. The concept of a gravitational
settling velocity is inappropriate in the case of gases,
but transfer is still often limited by diffusive
properties very near the receptor surface.
Sehmel (1980b) presents a tabulation of factors known
to influence the rate of pollutant deposition upon
exposed surfaces.
Figure C.2-1 has been constructed on
the basis of Sehmel's list and has been organized to
emphasize the greatly dissimilar processes affecting the
fluxes of gases and large particles. Small, submicro-
meter-diameter particles are affected by all the factors
indicated in the diagram; thus, simplification is
especially difficult for deposition of such particles.
In reality, Figure C.2-1 already represents a consider-
able simplification, since many potentially important
factors are omitted. In particular, the emphasis of the
diagram is on properties of the medium containing the
pollutants in question; a similarly complicated diagram
could be constructed to illustrate the effects of pol-
lutant characteristics. For particles, critical factors
include size, shape, mass, and Nettability; for gases,
concern is with molecular weight and polarization,
solubility, and chemical reactivity. In this context,
the acidity of a pollutant that is being transferred to
some receptor surface by dry processes is a quality of
special importance that may have strong impact on the
efficiency of the deposition process itself.
Figure C.2-2 summarizes particle size distributions on
a number, surface area, and volume basis. In this way,
the three major modes are brought clearly to attention.
The number distribution emphasizes the transient (or
Aitken) nuclei range, 0.005-0.05-pm diameter, for which
diffusion plays a role in controlling deposition. The
area distribution draws attention to the so-called
accumulation size range formed largely from gaseous
precursors (0.05-2-pm diameter, affected by both
diffusion and gravity). The remaining mode (2-50-~m
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216
| AIRBORNE SOURCE |
LARGE PARTICLES
AERODYNAMIC | SETTLING l
FACTO RS
GASES
I>
TO R8U LENCE ~-~ TO R8U LENCE
TH E RMOPH O R ESIS
NEAR-SU RfACE
PRORETIC ELECTROPHORESIS
EFFECTS
Dlf FUSI OPHO RESIS
&
STEFAN FLOW
| I MPACTI ON
QUASI-LAMINAR ~
LAYER I INTERCEPTION l
f ACTO RS it=
| 3ROWNIAN DlfFUSION
SU R FACE
PROPE RTI ES
~:r
~ STEFAN FLOW I
l
~ MOLECULAR DlffUSION 1
| ORIENTATION| ~ STOMATA | | WETNESS |
1 .
.
| FLEXIBILITY | | WAXINESS | I CHEMISTRY I
(SMOOTHNESS | | VESTITURE | | EMISSIONS |
| MOTION 1 | EXUDATES 1
.
1
RECEPTOR
l
FIGURE C.2-1 A schematic representation of processes likely to influence the rate of
dry deposition of airborne gases and particles. Note that some factors affect both
gaseous and particulate transfer, whereas others do not. However, submicrometer
particles are affected by all the factors that influence gases and large particles, and
hence it is these "accumulation-size-range" aerosols that present the greatest chal-
lenge for deposition research.
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217
-- ' ' 1 ' 1 1 ' ' 1 ' ' 1 '-- ' 1
FINE PARTICLES
~ COARSE PARTICLES
| ACCUMULATION I MECHANICALLY
I SIZE I GENERATED
RANGE I PARTICLES
A
V
, , 1 , , 1 , , 1 1 1
0.001 O.Ot
0.' 1.0
PARTICLE DIAMETER {pm)
10 100
FIGURE C.2-2 A hypothetical particle-size spectrum, such as might be found down-
wind of an industrial complex. The smaller aerosols have gaseous precursors and are
formed by condensation of exhaust gases and by atmospheric chemical reactions
(typically oxidation), followed by growth due to particle coagulation. The larger
particles are partly soil-derived, suspended by natural erosion and agricultural practices,
and partly the direct result of the combustion of fossil fuels. Acidic aerosols are pn-
marily in the smaller mode of the particle-size spectrum, whereas the larger mode
contains material that might tend to neutralize the acidic deposition of the smaller
particles. In evaluating the net input of acidity to a surface, it is critical that both
size fractions and gaseous contributions be included.
diameter, most evident in the volume distribution) is the
mechanically generated particle range for which gravity
causes most of the deposition. In most literature,
2-pm diameter is used as a convenient boundary between
~fine" and "coarse" particles.
Atmospheric sulfates, nitrates, and ammonium compounds
are primarily associated with the accumulation size
range. Figure C.2-2 demonstrates that very little acidic
or acidifying material is likely to be associated with
the coarse particle fraction in background conditions.
However, the larger particles include soil-derived
minerals, some of which can react chemically with
airborne and deposited acids. Moreover, it has been
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218
suggested that some of these larger particles may provide
sites for the catalytic oxidation of sulfur dioxide (for
example when the particles are carbon; Chang et al. 1981,
Cofer et al. 1981). Little is known about the detailed
chemical composition of large particle agglomerates.
However it is accepted that their residence time is quite
short (i.e., they are deposited relatively rapidly), that
there are substantial spatial and temporal variations in
both their concentrations and their composition, and that
their contribution to acid dry deposition should not be
ignored.
To evaluate deposition rates, several different
approaches are possible. Field experiments can be
conducted to monitor changes in some system of receptors
from which average deposition rates can be deduced. More
intensive experiments can measure the deposition of
particular pollutants in some circumstances. Neither
approach is capable of monitoring the long-term, spatial-
average dry deposition of pollutants. To understand why,
we must first consider in some detail the processes that
influence pollutant fluxes and then relate these consid-
erations to measurement and modeling techniques that are
currently being advocated. The logical sequence illus-
trated in Figure C.2-1 will be used to guide this
discussion.
2.1.2 Aerodynamic Factors
Except for the obvious difference that particles will
settle slowly under the influence of gravity, small
particles and trace gases behave similarly in the air.
Trace gases are an integral part of the gas mixture that
constitutes air and thus will be moved with all the
turbulent motions that normally transport heat, momentum,
and water vapor. However, particles have finite inertia
and can fail to respond to rapid turbulent fluctuations.
Table C.2-1 lists some relevant characteristics of
spherical particles in air (based on data tabulated by
Davies 1966, Friedlander 1977, and Fuchs 1964). The time
scales of most turbulent motions in the air are con-
siderably greater than the inertial relaxation (or
stopping) times listed in the table. These time scales
vary with height, but even as close as 1 cm from a smooth,
flat surface, most turbulence energy will be associated
with time scales longer that 0.01 see, so that even
100-pmrdiameter particles would follow most turbulent
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219
TABLE C.2-1 Dynamic Characteristics of Unit Density Aerosol
Particles at STP, Corrected for Stokes-Cunningham Effectsa
Particle Stopping Settling
Radius Dif fusivity Time Speed
(~m) (cm2/s) (s) (cays)
0.001 1.28 x 10-2 1.33 x 10-9 1.30 x 10-6
0.007 3.23 x 10-3 2.67 x 10-9 2.62 x 10-6
0.005 5.24 x 10-4 6.76 x 10-9 6.62 x 1-6
0.01 1.35 x 10-4 1.40 x 10-8 1.37 x 10-5
0.02 3.59 x 10 5 2.97 x 10-8 2.91 x 10-5
0.05 6.82 x 10-6 8.81 x 1o~8 8.63 x 10-5
0.1 2.21 x 10-6 2.28 x 10-7 2.23 x 10-4
0.2 8.32 x 10-7 6.87 x 10-7 6.73 x 10-4
0.5 2.74 x 10-7 3.54 x 10-6 3.47 x 10-3
1.0 1.27 x 10-7 1.31 x 10-5 1.28 x ~o~2
2.0 6.10 x 10-8 5.03 x 10-5 4.93 x 10-2
5.0 2.38 x 10-8 3.08 x 10-4 3.02 x 10~
10.0 1.38 x 10-8 1.23 x 10-3 1.2 x 10°
_ ... .
aData are from Fuchs tl964), Davies (1966), and Friedlander (1977)
fluctuations. However, natural surfaces
neither smooth nor flat, and it is clear that In many
circumstances the flux of particles will be limited by
their inability to respond to rapid air motions.
Naturally occurring aerosol particles are not always
spherical, although it seems reasonable to assume so in
the case of hydroscopic Particles in the submicromet. r
size range.
are normally
~ _ ~ - ~ ~ lo.. ~ _ ~ ~ _ ~ _
Chamberlain (1975) documents the ratio of
the terminal velocity of nonspherical particles to that
of spherical particles with the same volume. In all
cases, the nonspherical particles have a lower terminal
settling speed than equivalent spheres. The settling
speed differential is indicated by a dynamical shape
factor," a, as listed in Table C.2-2.
Thus, trace gases and small particles are carried by
atmospheric turbulence as if they were integral come
portents of the air itself, whereas large particles are
also affected by gravitational settling, which causes
them to fall through the turbulent eddies. In general,
however, the distribution of pollutants in the lower
atmosphere is governed by the dynamic structure of the
atmosphere as much as by pollutant properties.
.
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220
TABLE C.2-2 Dynamic Shape Factors as by which Nonspherical
Particles Fall More Slowly than Spherical (from
Chamberlain, 1975)
Ratio
Shape of axes ~
Ellipsoid 4 1.28
Cylinder 1 1.06
Cylinder 2 1.14
Cylinder 3 1.24
Cylinder 4 1.32
Two spheres touching, vertically 2 1.10
Two spheres touching, horizontally 2 1.17
Three spheres touching, as triangle - 1.20
Three spheres touching, in line 3 1.34-1.40
Four spheres touching, in line 4 1.56-1.58
In daytime, the lower atmosphere is usually well mixed
up to a height typically in the range 1 to 2 km, as a
consequence of convection associated with surface heating
by insolation. Pollutants residing anywhere within this
mixed layer are effectively available for deposition
through the many possible mechanisms. However, at night,
the lower atmosphere becomes stably stratified and
vertical transfer of nonsedimenting material is so slow
that, at times, pollutants at heights as low as 50 to 100
m are isolated from surface deposition processes. Thus,
in daytime, atmospheric transfer does not usually limit
the rate of delivery of pollutants to the surface bound-
ary layer in which direct deposition processes are active.
The fine details of turbulent transport of pollutants
remain somewhat contentious. Notable among the areas of
disagreement is the question of flux-gradient relation-
ships in the surface boundary layer. It is now well
accepted that the eddy diffusivity of sensible heat and
water vapor exceeds that for momentum in unstable (i.e.,
daytime) but not in stable conditions over fairly smooth
surfaces (see Dyer 1974, for example). However, it is
not clear that the well-accepted relations governing
either heat or momentum transfer are fully applicable to
the case of particles or trace gases; some disagreement
exists even in the case of water vapor. The situation is
OCR for page 221
221
even more uncertain in circumstances other than over
large expanses of horizontally uniform pasture. When
vegetation is tall, pollutant sinks are distributed
throughout the canopy so that close similarity with the
transfer of more familiar quantities such as heat or
momentum is effectively lost. There is even considerable
uncertainty about how to interpret profiles of tempera-
ture, humidity, and velocity above forests (see Garratt
1978, Hicks et al. 1979, Raupach et al. 1979).
2.1.3 The Quasi-laminar Layer
In the immediate vicinity of any receptor surface, a
number of factors associated with the molecular dif-
fusivity and the inertia of pollutants become important.
Large particles carried by turbulence can be impacted on
the surface as they fail to respond to rapid velocity
changes. The physics of this process is similar to the
physics of sampling by inertial collection.
Inertial impaction is a process that augments gravi-
tational settling for particles that fall into a size
range typically between 2- and 20-pm diameter (q.v.
Slinn 1976b). Larger-sized particles tend to bounce, and
capture is therefore less efficient, while smaller-sized
particles experience difficulty in penetrating the quasi-
laminar layer that envelops receptor surfaces. From the
viewpoint of acidic particles, inertial impaction is a
process of questionable relevance since most acidic
species are associated with smaller particles (see Figure
C.2-2), which are not strongly affected by this process.
However, Figures C.2-2 and C.2-3 show that many airborne
materials exist in the size range likely to be affected
by inertial impaction. Since many of the chemical
constituents of soil-derived particles are capable of
neutralizing deposited acids, inertial impaction may have
important indirect effects on acidic deposition.
To illustrate the role of molecular or Brownian
diffusivity, it is informative to consider the simple
case of a knife-edged thin plate, mounted horizontally
and with edge normal to the wind sector. As air passes
over (and under) the ~late, a laminar layer develops, of
thickness ~ = c(vx/u) /2, where v is kinematic vis-
cocity, x is the downwind distance from the edge of the
plate, and u is wind speed. According to Batchelor
(1967), the value of the numerical constant c is 1.72.
Thus, for a plate of dimensions 5 cm in a wind speed of
OCR for page 222
222
~.~.` 1 1 1 1 1 1
111 1 1 1 1 111]
CD 10-4
10-5
I.
· - o
to
to
to
\ 1
i
\
1 1 1 1 1 1 1 111 1 1 1 1 1 1 111 1 1 1 1 i 111
-
2 ~03 104 105
SO
FIGURE C.2-3 Laboratory verification of Schmidt-number scaling for particle trans-
fer to a smooth surface. The quantity plotted is B _ vd/u*, evaluated for transfer
across a quasi-laminar layer of molecular control immediately adjacent to a smooth
surface. Data are from Harnott and Hamilton (1965; open circles), Hubbard and Light-
food (1966 ; triangles), and Muzushinz et al. (1 971; solid circles), as reported by
Lewellen and Sheng (1980~. The line drawn through the data is Equation (C.2-1), with
exponent al = -2/3 and constant of proportionality A_ 0.06.
1 m/s, we should imagine a boundary-layer thickness
reaching about 1.5-mm thick at the trailing edge.
Over nonideal surfaces, the internal viscous boundary
layer is frequently neither laminar nor constant with
time. The layer generates slowly as a consequence of
viscosity and surface drag as air moves across a
surface. The Reynolds number Re (_ ux/v, where u is
the wind speed, x is the downwind dimension of the
obstacle, and v is kinematic viscosity) is an index of
the likelihood that a truly laminar layer will occur.
For large Re, air adjacent to the surface remains
turbulent: viscosity is then incapable of exerting its
influence. In many cases, it seems that the surface
layer is intermittently turbulent. For these reasons,
and because close similarlity between ideal surfaces
studied in wind tunnels and natural surfaces is rather
difficult to swallow, the term "quasi-laminar layer" is
preferred.
Wind-tunnel studies of the transfer of particles to
the walls of pipes tend to support the concept of a
limiting diffusive layer adjacent to smooth receptor
OCR for page 223
223
surfaces. Transfer across such a laminar layer is
conveniently formulated in terms of the Schmidt number,
Sc = v/D, where v is viscosity and D is the pollutant
diffusivity. The conductance, or transfer velocity vl,
across the quasi-laminar layer is proportional to the
friction velocity u*:
v1 = Au* Sca,
(C.2-1)
where A and ~ are determined experimentally. Most
studies agree that the exponent a is about -2/3, as is
evident in the experimental data represented in Figure
C.2-3. However, a survey by Brutsaert (1975a) indicates
exponents ranging from -0.4 to -0.8. The value of the
constant A is also uncertain. The line drawn through the
data of Figure C.2-3 corresponds to A ~ 0.06, yet the
wind-water tunnel results of Moller and Schumann (1970)
appears to require A ~ 0.6. These values span the
value of A ~ 0.2 recommended for the case of sulfur
dioxide flux to fibrous, vegetated surfaces (Shepherd
1974, Wesely and Hicks 1977).
~ _~: _ ~ _ =_. _ ~. .
~ _ _,= _ _ _
=~'l~a~ w unuary-layer theory Imposes the expectation
that particle deposition to exposed surfaces will be
strongly influenced by the size of the particle, with
smaller particles being more readily deposited hv
diffusion than larger.
It is clear that many artificial
Furnaces or structures made of mineral material will have
characteristics for which the laminar-layer theories
might be quite appropriate. However, the relevance to
vegetation can be questioned. Microscale surface
roughness elements can penetrate the barrier presented by
this quasi-laminar layer and should be suspected as sites
for enhanced deposition of both particles and gases (see
Chamberlain 1980).
2.1.4 Phoretic Effects and Stefan Flow
Particles near a hot surface experience a force that
tends to drive them away from the surface. For very
small particles (<0.03-pm diameter, according to
Davies 1967), this "thermophoresis" can be visualized as
the consequence of hotter, more energetic air molecules
impacting the side of the particle facing the hot sur-
face. For larger particles, radiometric forces become
important (Cadre 1966). In theory, thermal radiation can
OCR for page 363
363
chemical formation of such species in clouds and
precipitation, there is a tendency to lump these effects
with physical removal processes In most modeling efforts,
expressing them in terms of pseudo scavenging coefficients
or collection efficiencies. Such phenomena must be
resolved in finer mechanistic detail than this before a
satisfactory treatment is possible, and this requires a
knowledge of chemical transformation processes that is
much more advanced than existing at present.
~ Much more extensive understanding of the
competitive nucleation capability of aerosols in in-cloud
environments is needed, especially for those substances
that do not compete particularly well in the nucleation
process. The influence of aerosol-particle composition--
especially for "internally mixed aerosols"*--is
particularly important in this regard.
· The identification of specific sources responsible
for chemical deposition at a given receptor location
requires that we possess a much more accomplished
capability to describe long-range pollution transport.
Progress in this area during recent years has been
encouraging, but much more remains to be achieved before
we have a proficiency that is really satisfactory for
reliable source-receptor analysis.
· We still need to enhance our understanding of the
detailed microphysical and dynamical processes that occur
in storm systems. Besides providing required knowledge
of basic physical phenomena, such research is important
in providing valid parameterizations of wet removal for
subsequent use in composite regional models.
As a final note, it is useful to reflect once again on
the fact that scavenging modeling research--as treated in
this section--has been in a rather continuous state of
development over the past 30 years. while progress has
been indeed significant during this period, a number of
important and unsolved problems still exist. Accordingly,
one must use this perspective in assessing our rate of
advancement during future years. Reasonable progress in
resolving the above items can be expected over the next
decade; but the complexity of these problems demands that
a serious and sustained effort be applied for this
purpose.
*Those containing individual particles composed of a
mixture of chemical species.
OCR for page 364
364
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Representative terms from entire chapter:
deposition velocities