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Question 7.1: USING GROUNDWATER CONCENTRATIONS TO ESTIMATE THE PROXIMITY O......

USING GROUNDWATER CONCENTRATIONS TO ESTIMATE THE PROXIMITY OF RESIDUAL SINGLE-COMPONENT DNAPL

Analysis of a water sample from a monitoring well indicated 6.4 mg/L of tetrachloroethene (PERC). Tetrachloroethene was a target contaminant because a dry cleaning establishment had once been on the site near the well. Is residual tetrachloroethene DNAPL likely to be in the subsurface upgradient near the well? Use data from Table 7.3.

TABLE 7.3 Values for Important Properties of DNAPL Contaminants Commonly Found at U.S. Superfund Sites
Chemical Compound Density (g/cm^{3}) Water Solubility (mg/L) Vapor Pressure (torr) Henry’s Law Constant (atm  m^{3}/mol) Dynamic  Viscosity^{a} (centipoise) Kinematic  Viscosity^{a} (centistokes)
water 0.9991 (15°C) _ 12.8 (15°C) _ 1.145 (15°C) 1.146 (15°C)
(for comparison) 0.9982 (20°C) 17.5 (20°C) 1.009 (20°C) 1.011 (20°C)
Halogenated semivolatiles
Aroclor^{b}  1242 1.3850 0.45 4.06\times 10^{-4} 3.4\times 10^{-4}
Aroclor^{b}  1254 1.5380 0.012 7.71\times 10^{-5} 2.8\times 10^{-4}
Aroclor^{b} 1260 1.4400 0.0027 4.05\times 10^{-5} 3.4\times 10^{-4}
Chlordane 1.6 0.056 1\times 10^{-5} 2.2\times 10^{-4} 1.104 0.69
1,4-Dichlorobenzene 1.2475 80 0.6 1.58\times 10^{-3} 1.258 1.008
1,2-Dichlorobenzene 1.3060 100 0.96 1.88\times 10^{-3} 1.302 0.997
Dieldrin 1.7500 0.186 1.78\times 10^{-7} 9.7\times 10^{-6}
Pentachlorophenol 1.9780 14 1.1\times 10^{-4} 2.8\times 10^{-6}
2,3,4,6-Tetrachlorophenol 1.8390 1,000
Halogenated volatiles
Carbon tetrachloride 1.5947 790 91.3 0.020 0.965 0.605
Chlorobenzene 1.1060 490 8.8 3.46\times 10^{-3} 0.756 0.683
Chloroform (trichloromethane) 1.4850 7,920 160 3.75\times 10^{-3} 0.563 0.379
1,1-Dichloroethane 1.1750 5,500 182 5.45\times 10^{-4} 0.377 0.321
1,2-Dichloroethane 1.2530 8,690 63.7 1.1\times 10^{-3} 0.840 0.67
cis-1,2-Dichloroethylene 1.2480 3,500 200 7.5\times 10^{-3} 0.467 0.364
trans-1,2-Dichloroethylene 1.2570 6,300 265 5.32\times 10^{-3} 0.404 0.321
1,1-Dichloroethylene 1.2140 400 500 1.49\times 10^{-3} 0.330 0.27
1,2-Dichloropropane 1.1580 2,700 39.5 3.6\times 10^{-3} 0.840 0.72
Ethylene dibromide 2.1720 3,400 11 3.18\times 10^{-4} 1.676 0.79
Methylene chloride 1.3250 13,200 350 2.57\times 10^{-3} 0.430 0.324
1,1,2,2-Tetrachloroethane 1.6 2,900 4.9 5.0\times 10^{-4} 1.770 1.10
1,1,2-Trichloroethane 1.4436 4,500 0.188 1.17\times 10^{-3} 0.119 0.824
1,1,1-Trichloroethane 1.3250 950 100 4.08\times 10^{-3} 0.858 0.647
Tetrachloroethylene (PCE) 1.620 200 14 0.0227 0.890 0.54
Trichloroethylene (TCE) 1.460 1,100 58.7 8.92\times 10^{-3} 0.570 0.390
Trichloromethane (chloroform) 1.4850 7,920 160 3.75\times 10^{-3} 0.563 0.379
Nonhalogenated semivolatiles
2-Methyl naphthalene 1.0058 25.4 0.0680 0.0506
o-Cresol 1.0273 31,000 2.45\times 10^{-1} 4.7\times 10^{-5}
p-Cresol 1.0347 24,000 1.08\times 10^{-1} 3.5\times 10^{-4}
2,4-Dimethylphenol 1.0360 6,200 0.098 2.5\times 10^{-6}
m-Cresol 1.0380 23,500 1.53\times 10^{-1} 3.8\times 10^{-5} 21.0 20
Phenol 1.0576 84,000 5.293\times 10^{-1} 7.8\times 10^{-7} 3.87
Naphthalene 1.1620 31 2.336\times 10^{-1} 1.27\times 10^{-3}
Benzo(a)Anthracene 1.1740 0.014 1.16\times 10^{-9} 4.5\times 10^{-6}
Fluorene 1.2030 1.9 6.67\times 10^{-4} 7.65\times 10^{-5}
Acenaphthene 1.2250 3.88 0.0231 1.2\times 10^{-3}
Anthracene 1.2500 0.075 1.08\times 10^{-5} 3.38\times 10^{-5}
Dibenzo(a,h)anthracene 1.2520 2.5\times 10^{-3} 1\times 10^{-10} 7.33\times 10^{-8}
Fluoranthene 1.252 0.27 7.2\times 10^{-5} 11\times 10^{-6}
Pyrene 1.2710 0.148 6.67\times 10^{-6} 1.2\times 10^{-5}
Chrysene 1.2740 6.0\times 10^{-3} 6.3\times 10^{-9} 1.05\times 10^{-6}
2,4-
Dinitrophenol
1.6800 6.0\times 10^{-3} 1.49\times 10^{-5} 6.45\times 10^{-10}
Miscellaneous
Coal tar (45°F) 1.028 18.98
Creosote 1.05 ~1.08 (15°C)
Source: Adapted from USEPA, Dense Nonaqueous Liquids, S.G. Huling and J.W. Weaver, Ground Water Issue, Office of Research and Development, Office of Solid Waste and Emergency Response, Washington, DC, EP A/540/4-91-002, March 1991.
^a Dynamic viscosity measures a liquid’s resistance to flow. Kine matic viscosity is the ratio of dynamic viscosity to density, see Table 7.2.
^b Aroclor is the trade name for polychlorinated biphenyls (PCBs) manufactured by Monsanto. See Section 7.3.4.

 

 

TABLE 7.2 DNAPL Properties Important for Predicting Mobility in Environment
Properties of DNAPL/Soil Definition/Typical Units Comments
Density (d) d = mass/volume

d = g · cm^{-3}; lb  ·  ft^{-3}

Density distinguishes between LNAPLs  (d_{DNAPL} < d_{water})  and  DNAPLs  (d_{DNAPL} < d_{water}).
It depends on temperature, pressure, molecular weights of components, intermolecular forces,
and bulk liquid structure.
Dynamic viscosity (\mu) \mu = fluid internal resistance to flow or
shear. The CGS unit is poise (P); SI
unit is N·s·m^{-2}.
1 P = 100 centipoise
= 1 g/cm·s = 0.1 Pa·s
Dynamic viscosity is a measure of the force required to move a liquid at a constant velocity.
The common unit of μ is the centipoise (cP) because water at 20.2°C has a convenient
viscosity of 1.000 cP. Viscosity decreases with increasing temperature (note water in
Table 7.2). Intermolecular attractions are the main cause of viscosity. The lower the viscosity,
the more fluid the liquid and the more easily it will flow through soils. The reciprocal of
dynamic viscosity is called fluidity.
Kinematic viscosity (\nu) \nu= dynamic viscosity/density
The CGS unit is stokes (St) or centistokes (cSt); SI units are m^{2}·s^{-1}; stokes = poises/density
1  St = 100  cSt = 10^{-4} m^{2}·s^{-1}
When the force causing a liquid to move is only due to gravity, as in NAPL movement in the
environment, the fluid density, as well as the dynamic viscosity, affects the rate of movement.
Using kinematic viscosity includes density in its definition and eliminates the force term
(N or Pa). Kinematic viscosity is convenient for calculating hydraulic conductivity, which is
inversely proportional to n. Since the density of water at 20.2°C is 0.998 g/cm^{3}, the kinematic
viscosity of water at 20.2°C is, for most practical purposes, equal to 1.0 cSt
Solubility in water (S) S = mass of dissolved substance per
unit volume of water, in equilibrium
with the undissolved substance. For
environmental pollutants in water,
the common units are mg/L or
\mu g/L.
Solubility measures a compound’s tendency to partition from the bulk compound into water.
For a single-component NAPL, the solubility is the concentration of dissolved component in
equilibrium with the NAPL. For NAPLs that are mixtures, each component of the mixture has
its own characteristic solubility, which is generally lower than the solubility of the pure
component (see Section 6.3.8). Thus, the overall solubility of an NAPL mixture is variable,
depending on its composition, and changes with time as the more-soluble components leave
the NAPL by partitioning into the water. Solubility can vary with temperature, pH, TDS, and
the presence of cosolvents (e.g., detergents, EDTA, etc.). In general, the greater the molecular
weight (high polarizability) and symmetry (low polarity) and the fewer hydrogen-bonding
atoms, the lower the solubility, see Section 2.9.
Vapor pressure (P_{v}) P_{v} = pressure exerted by a vapor in
equilibrium with the liquid or solid
phase of the same substance. There
are many different units for pressure.
The more common units are
millimeters of mercury (mm Hg),
torr, and atmosphere (atm). The SI
unit is pascal (Pa).
1  mm  Hg = 1  torr = 760^{-1}  atm
= 1.333  mbar = 133.3  Pa
= 1.934 \times 10^{-2}  psi  1  Pa
= 1 N/m^{2} = 10^{-5}  bar
= 7.50\times 10^{-3}  torr
= 1.450\times10^{-4}  psi
Vapor pressure indicates an NAPL’s volatility, or tendency to vaporize, at a given temperature.
It depends only on the temperature and increases exponentially with increasing temperature.
On a molecular level, vapor pressure is an indication of the strength of intermolecular
attractive forces, see Section 2.8.6. The vapor pressure of DNAPLs ranges from very high to
very low; for example, compare 1,1-dichloroethylene and chrysene in Table 7.2
Henry’s law volatility The Henry’s law volatility of a
compound is a measure of the
transfer of the compound from being
dissolved in the aqueous phase to
being a vapor in the gaseous phase.
The transfer process from water to the gaseous phase in the atmosphere is dependent on the
chemical and physical properties of the compound, the presence of other compounds, and the
physical properties (velocity, turbulence, depth) of the water body and atmosphere above it.
The factors that control volatilization are the solubility, molecular weight, vapor pressure, and the nature of the air–water interface through which it must pass. The Henry’s constant is a
valuable parameter that can be used to help evaluate the propensity of an organic compound to volatilize from the water. The Henry’s law constant is defined as the vapor pressure divided by the aqueous solubility. Therefore, the greater the Henry’s law constant, the greater the tendency to volatilize from the aqueous phase, refer to Table 7.1.
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Since the observed DNAPL is a pure solvent (tetrachloroethene) and not a mixture, its mole fraction, X, equals unity and S_{eff} = S_{pure}. From Table 7.3, the solubility of pure tetrachloroethene is 200 mg/L. By the guideline in Section 7.3.1, if the measured concentration of a single-component DNAPL in a well is 1% or more of its purephase solubility, it is likely that a DNAPL source zone is near the well.
One percent of 200 mg/L is 2.0 mg/L. The measured concentration of tetrachloroethene in the well is 6.4 mg/L. Because this is significantly larger than 2.0 mg/L, it is likely that a source zone of tetrachloroethene DNAPL is quite close to the well.

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