Encyclopedia of Environmental Science and Engineering, Volume I and II

(Ben Green) #1

928 PCBs AND ASSOCIATED AROMATICS


TABLE 49
PCB concentrations derived from different correlation
curves can produce drastically different result

Concn. of PCB as ppm Aroclor 1016

Early peaks Late peaks Total area

55.7 19.0 8.6
57.3 31.5 6.9
46.8 6.3 40.1
48.9 4.8 33.4
53.4, 62.6‡ 6.9 32.6, 19.5
63.5 26.5 46.7
62.2 27.0 51.4
82.9 58.2 85.8

TABLE 50
A high bias is obtained when residue peaks are
inappropriately calculated
PCB concentration (ppm Aroclor 1016)

Conventional Total area Peak height
30.7 18.7 12.5
59.6 13.7 0.9
51.6 56.8 19.7
60.6 22.0 N.D.
55.0 4.4 N.D.
147 37.7 33.0
73.0 44.1 11.6
65.5 23.2 N.D.
53.9 27.9 7.6
54.6 27.6 7.6
50.7 44.4 13.1
60.4 23.0 4.5
58.4 30.3 6.3
48.8 24.3 6.9
48.0 25.2 7.2

N.D.—not determinable.

TABLE 51
The apparent concentration of aroclor 1016 in the samples can vary by
several hundreds of percent depending upon
the peak chosen for quantitation

Retention time (min)/concentration

4.39 min 6.47 min 8.71 min
21.5 25.0 12.5
58.8 22.6 0.9
37.8 37.0 19.7
73.0† 21.0 N.D.
9.2 N.D. N.D.
38.3 91.7 33.0
65.0 46.7 11.6
51.8 34.6 N.D.
53.1 33.0 7.6
50.7 36.1 7.6
50.0 34.0 13.1
66.3 28.0 4.5
60.2 30.3 6.3
55.5 33.7 6.9
46.3 30.2 7.2

TABLE 52
Peak height ratios for standard aroclors remain constant but vary for the
sample under investigation

Peak height ratios relative to Rt  7.75 min

Sample 4.27 min 6.28 min 7.52 min 8.04 min 11.4 min
EPA 0.64 0.76 1 0.57 0.53
Standard 0.54 0.59 1 0.54 0.43
Oil (1) 0.48 0.54 1 0.45 0.45
Oil (2) 7.60 3.30 1 N.D. N.D.
Oil (3) 0.50 0.52 1 0.44 0.46
Oil (4) 9.8 3.36 1 N.D. N.D.

in a precisely controlled thermal environment. Temperature
and residence time relationships were established for the
conditions necessary to produce a specified destruction effi-
ciency. It was concluded that with a 1 sec. residence time,
most of the pyrolysis occurred within a narrow temperature
range between 640°C and 740°C (Mescher et al.^56 ). The
results were based on the disappearance of PCBs rather than
the accumulation of degradation products. The lower molec-
ular weight PCBs are less thermally stable than the higher
molecular weight congeners. The residence time of the mol-
ecules in the high temperature zone is therefore a critical

parameter in determining the overall efficiency of the deg-
radation. However, the destruction and removal efficiency
(DRE) of an incineration process for a given compound does
not consider the toxicity of any pyrolysis products. The DRE
is defined as

DRE

WW
W

=


×

()feed out

feed

100

where,
W feed  mass feed rate of a compound to the incinerator,

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