Environmental Engineering Reference
In-Depth Information
Stabilizers of Perchloroethylene
Butoxymethyl oxirane
0.023
0.00029
20,000
5.87
25.549
<100
Cyclohexene oxide
0.0009
0.000015
<1
Perchloroethylene
99.98
0.9997
150
150
Stabilizers of Dichloromethane
Nitromethane
1.0
0.0137
11,100
152
103
<100
1,4-Dioxane
1.9
0.0178
10,000,000
178,312
0.087
>10,000
Cyclohexane
0.21
0.0021
55
0.12
132,346
<1
1,3-Dioxolane
4.3
0.0488
10,000,000
487,945
0.032
>100,000
Dichloromethane
92.6
0.9175
17,000
15,598
Notes: The values given here are rough approximations; the calculations that yielded these estimates do not account for the ~25% of oily wastes that accumulate in vapor degreaser still
bottoms.
a
Operating parameters for perchloroethylene and methyl chloroform vapor degreasers are from Tarrer et al. (1993); parameters for trichloroethylene and dichloromethane vapor degreasers
are inferred from data in USEPA (1977).
b
Enthalpy data are from Chickos and Acree (2003). Enthalpies of vaporization were not located for butoxymethyl oxirane or cyclohexene oxide. Where enthalpy data are not available,
enthalpy of vaporization can be calculated by using Antoine coefi cients with the method presented in the Handbook of Chemical Property Estimation Methods (Lyman et al., 1990);
however, Antoine coefi cients were also not located for these two compounds.
c
CF = Concentration factor from Table 1.26.
d
Where solvent concentration is 10 mg/L. Final stabilizer concentration in groundwater resulting from a spill of still bottoms is estimated to an order of magnitude without considering i ne-
grained storage or other fates of stabilizers in the subsurface.
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