FINAL TECHNICAL REPORT
September 1, 1995, through August 31, 1996
Project Title: WASHABILITY OF AIR TOXICS IN ILLINOIS COALS AS APPLIED
TO GRAVITY-BASED CLEANING
ICCI Project Number: 95-1/1.2C-1
Principal Investigator: Ilham Demir, Illinois State Geological Survey (ISGS)
Other Investigators: Rodney R. Ruch, John M. Lytle, John D. Steele, Chris C. Rohl, each at the ISGS
Project Manager: Ken K. Ho, ICCI
ABSTRACT
Advanced gravity-based cleaning can potentially reduce the contents of ash
and air toxics, including sulfur (S) and trace and minor elements, in finely
ground coals to levels predicted by laboratory float-sink (F-S) tests. Therefore,
the goal of this project was to generate F-S washability data on ash, S,
and 16 trace and minor elements (As, Be, Cd, Cl, Co, Cr, F, Hg, Mn, Ni, P,
Pb, Sb, Se, Th, U - all identified as hazardous air pollutants (HAPs) by
the Clean Air Act Amendments of 1990) in marketed Illinois coals. The data
will assist in developing strategies to prevent or reduce the adverse effects
of pending environmental regulations on the use of Illinois coals in power
generation.
Samples of 29 marketed coal products from Illinois mines that were in operation
during 1995 were ground to -100 mesh and separated into their specific gravity
fractions (<1.3, 1.3-1.4, 1.4-1.6, >1.6) using a centrifugal F-S method.
Also, representative splits of 10 samples selected among the 29 samples were
ground to -200 mesh and subjected to similar F-S separation tests. Using
the moisture and ash data on the F-S fractions, a composite sample of
80%-combustibles recovery was prepared for each F-S test.
For the twenty-nine -100 mesh samples, the ash content in the composite samples
decreased (relative to parent coals) by 37% to 75%. Average decreases for
As(63%), Cd(73%), Hg(70%), Mn(70%), and P(58%) exceeded the average decrease
for ash (53%). Average decreases for other elements were: Co(33%), Cr(19%),
F(35%), Ni(30%), Pb(45%), S(27%), Sb(18%), Th(28%), and U(12%). Only Be was
enriched (on average, 118%) in composite samples relative to the original
coals. However, the additional environmental risk from Be enrichment during
fine-coal cleaning could be insignificant because this element has small
initial concentration in the coals and relatively low atmospheric mobility
during coal combustion. Grinding the samples to -200 mesh generally did not
result in significant improvement in the F-S separation of ash, S, and HAPs,
beyond the separations obtained at -100 mesh. Thus, grinding marketed Illinois
coals to -100 mesh would be sufficient for significantly improving the quality
of these coals through the use of advanced gravity-based cleaning techniques.
The F-S data of this study showed that the ultimate cleanability of Illinois coals is substantially greater than that indicated by release analysis data of a previous study.
EXECUTIVE SUMMARY
The Clean Air Act Amendments (CAAA) of 1990 require that emissions of 189
hazardous air pollutants (HAPs) and sulfur dioxide into the atmosphere from
various human sources be reduced. Among the 189 HAPs, there are 16 elements
(As, Be, Cd, Cl, Co, Cr, F, Hg, Mn, Ni, P, Pb, Sb, Se, Th, U ) that occur
in coal and that can potentially be emitted into the atmosphere as a result
of coal combustion. Electrical utilities are presently exempt from having
to comply with the CAAA requirements on HAPs. However, this may change after
the U.S. EPA completes its risk analyses and promulgates emission standards.
We previously determined contents of ash, sulfur (S), and HAPs in marketed coal samples from operating mines in Illinois and compiled existing data on channel samples1. In another project, we investigated froth flotation cleanabilities of ash and HAPs in the same coals using a froth flotation / release analysis (FF/RA) procedure2. The FF/RA data can be used to estimate the performance of the coals in standard column or froth flotation circuits. However, FF/RA data generally do not indicate maximum, theoretical cleanability of finely ground coal3,4. Float-sink (F-S) washability tests appear to be more suitable than the FF/RA for determining the maximum cleanability of a coal sample at a given particle size. The purpose of this project, therefore, was to generate F-S washability data on ash, S, and HAPs in marketed coal products from all operating Illinois mines and to compare the results with the FF/RA data obtained previously.
New gravity-based cleaning technologies or technologies that combine gravity
separation and column flotation potentially can achieve the same levels of
washability efficiency predicted by results from F-S separation of finely
ground coal in the laboratory. The F-S washability data produced by this
project can then be used to evaluate the efficiency of physical fine-coal
cleaning, especially advanced gravity-based cleaning, for reducing ash, S,
and HAPs contents in marketed coal products from operating Illinois mines.
The marketed coal products are currently ground to 70% -200 mesh size for
utilization in PC boilers which comprise over 90% of the combustion boilers
used in Illinois5. Therefore, because of no extra cost for grinding,
an advanced cleaning strategy to produce compliance coal from Illinois coals
could be economical.
For this project, samples of 29 marketed Illinois coals were ground to -100
mesh and then separated into their specific gravity fractions (<1.3, 1.3-1.4,
1.4-1.6, >1.6) using a centrifugal F-S method. In addition, representative
splits of 10 samples selected among the 29 samples were subjected to similar
F-S separation at -200 mesh size. For a given test, the first two and sometimes
three lightest F-S fractions were combined in proportion to their moisture
and ash contents to obtain a clean composite sample with the lowest possible
ash content at an 80%-combustibles recovery.
The result of the F-S tests indicated that ash and S contents of marketed
Illinois coals can potentially be reduced significantly, beyond conventional
cleaning, through the use of advanced physical fine-coal cleaning. For the
29 samples ground to -100 mesh, the decrease in the ash content of the clean
composite samples relative to the parent coals ranged from 37% to 75% with
an average decrease of 53%. As a result, clean composite samples having ash
contents of 2.8 to 3.9% were produced from 10 of the 29 samples. For the
remaining composite samples, the ash content ranged from 4.0 to 5.3 % for
12 samples and 5.6% to 7.9% for 7 samples. The S content of the 29 composite
samples varied between 0.6 and 3.5%, representing a decrease of a 8% to 47%
with an average of 27%. The S remaining in the clean composite samples was
overwhelmingly organic S.
Among the decrease values for HAPs, the average decreases for As(63%), Cd(73%),
Hg(70%), Mn(70%), and P(58%) exceeded the average decrease for ash, indicating
that these five elements were somewhat enriched in relatively coarse mineral
grains that were effectively removed. Precombustion removal of As, Cd, and
Hg from coal is important because of the relatively high atmospheric mobility
of these elements during coal combustion. The average decreases for Pb(45%),
Se(38%), and F(35%), three other elements with relatively significant atmospheric
mobility, were smaller than the decrease for ash but still significant. The
average decreases for other HAPs were: Co(33%), Cr(19%), Ni(30%), Sb(18%),
Th (28%), and U(12%). Although Sb can be mobilized to a relatively significant
degree by attachment to air-borne fly ash particles, small Sb concentrations
(generally <1.5 mg/kg) in marketed Illinois coals could limit any
environmental risk associated with Sb emission from combustion of these coals.
Only Be was generally enriched in the -100 mesh washability products (on
average, by 118%) when compared with the parent coals, suggesting that Be
was associated with the coal macerals. Because some of the Be stays with
bottom ash and slag during coal combustion, and because the Be content of
marketed Illinois coals is usually <1.5 mg/kg, additional environmental
risk due to the enrichment of this element could be very small or insignificant.
Because a Cl-containing heavy medium was used in the F-S tests, the Cl analysis
was compromised for this study. Further improvement in the F-S separation
of ash, S, and HAPs made by grinding 10 of the samples to -200 mesh was generally
insignificant. Thus, grinding the coals to -100 mesh would be sufficient
for significantly improving their quality through the use of advanced
gravity-based cleaning techniques.
The F-S process used in this study generally removed significantly more ash
and HAPs than the previously used2 FF/RA process. Therefore, the
F-S tests can estimate the ultimate cleanabilities of marketed Illinois coals
better than the FF/RA tests.
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1Demir, I., Harvey R.D., Ruch, R.R., Damberger, H.H., Chaven, C., Steele, J.D., and Frankie, W.T., 1994, Characterization of Available (Marketed) Coals From Illinois Mines. Illinois State Geological Survey, Open File Series 1994-2, 26 p.
2Demir, I., Ruch, R.R., Harvey, R.D., Steele, J.D., and Khan, S., 1995, Washability of Trace Elements in Product Coals from Illinois Mines. Illinois State Geological Survey, Open File Series 1995-8, 22 p.
3Straszheim, W.E. and Markuszewski, R., 1989, Association of mineral matter with the organic coal matrix, Preprints ACS Div. Fuel Chem., v. 34(3), p. 648-655.
4Forrest, W.R., Adel, G.T., and Yoon, R.H., 1994, Characterizing coal flotation performance using release analysis. Coal Prep., v. 14(1-2), p. 13-27.
5Honaker, R.Q., Paul, B.C., and Wang, D., 1994, Advanced physical coal cleaning to comply with potential air toxic regulations. Quarterly Technical Report (9/1-11/30/1994) to the Illinois Clean Coal Institute.