1016
B.K. Gullett, E. Wikstrom / Chemosphere 40 (2000) 1015±1019
current instrumentation development shows promise for
measuring these lower chlorinated congeners in an on-
line, real-time mode (Oser et al., 1998). Sampling results
from two facilities and a wide range of operating con-
ditions are used to establish the robustness of the pre-
dictions for application to other facilities and fuels.
Strong relationships between lower chlorinated cong-
eners and PCDD/F measures (such as TEQ) coupled
with further development of methods to monitor the
concentrations of these congeners in ¯ue gas should
provide a valuable tool for understanding the mecha-
nism of PCDD/F formation and ®nding process control
methods to reduce or prevent their formation.
dominance of PCDFs over PCDDs. As is commonly
found, the intra-group PCDD/F TOTAL and TEQ
values appear linearly correlated (Fig. 1). Variation in
the slopes is consistent with dierences found in inter-
source comparisons (Cleverly et al., 1997). Each groupÕs
ꢀ
homologue pro®les (Norfolk ± Fig. 2, Umea-1 ± Fig. 3,
and Umea-2, Fig. 4) exhibit consistent, intra-group
ꢀ
pro®les, although the magnitude and peak homologue
group vary considerably between the three test groups.
The stability of the homologue pattern is not surprising,
ꢀ
although Umea-1, with planned operation beyond the
limits of desirable combustion conditions, might have
been expected to exhibit a larger pro®le variation based
on work by Gullett et al. (1999). Their work showed
shifts or magnitude changes in the homologue pro®le
that were associated with changes in operational pa-
rameters of sulfur dioxide (SO2) and hydrogen chloride
(HCl) concentrations, residence time, and quench rate.
SASâ procedure REG (SAS/STAT User's Guide,
1990) was used to obtain the best group-speci®c one-,
two-, and three-predictor models (Table 1) of run-
2. Experimental
A municipal waste combustor near Norfolk, Virgin-
ia, burning processed ¯u refuse derived fuel (RDF),
was the site for 13 pre-spray-dryer sampling tests
(``Norfolk''). This facility ®red RDF-only or co-®red
RDF with two types of coal during this testing. One coal
was low sulfur (S, 0.7 wt%) and one coal from Illinois
was high S (3.5 wt%). Co-®ring up to 5 wt% high S coal
with RDF reduced the pre-spray-dryer PCDD/F con-
centration by up to 70% from the initial baseline. Sam-
pling and analytical methods were expanded to quantify
mono-, di-, and tri-CDD/CDF congener totals as well as
select isomers using the isotope dilution method. La-
belled di- and tri-CDF and di- and tri-CDD surrogates
were also added to XAD-2 prior to sampling to assess
overall measurement performance.
ꢀ
The pilot scale Umea reactor is a solid fuel comb-
ustor that burns arti®cial pellets on an under®re/over®re
air supplied grate. The nominal burn rate is 18 MJ/h
(1 kg/h). A triple looped convection section, 5 m per
section, allows for simulating quench rates in ®eld units.
Further details can be found in Wikstrom et al. (1998),
Wikstrom and Marklund (1998).
Fig. 1. Comparison of Total PCDD + PCDF [mono- to octa-
PCDD/F (pmol/dscm)] and TEQ (ng/dscm) for Norfolk (n),
ꢀ
Two test groups were run in this reactor. ``Umea-1''
run parameters varied total air ¯ow from 90 to 150
L/min, ¯ow in the secondary air varied from 20 to 70%,
and the temperature of the secondary air varied from 50
ꢀ
Umea-1 (r), and Umea-2 (m) tests.
ꢀ
to 350°C (the test matrix is shown in Wikstrom and
ꢀ
Marklund, 1997). The ``Umea-2'' tests were run under
non-varied combustion conditions. The purpose of these
tests was to simulate full scale combustion with an ar-
ti®cial municipal solid waste to study formation of
PCDD/Fs.
3. Results, analyses, and discussion
Thirteen tests at the Norfolk site and 16 tests at the
ꢀ
Umea pilot plant resulted in a fairly wide range of
PCDD/F TOTAL and TEQ values, with the common
Fig. 2. Run-speci®c homologue pro®les from Norfolk tests.