United States
Environmental Protection
Agency
Industrial Environmental Research
Laboratory
Research Triangle Park NC 27711
Research and Development
EPA-600/S7-84-026 Mar. 1984
SERA Project Summary
Pollutant Formation During
Fixed-Bed and Suspension
Coal Combustion
S. C. Manis, J. M. Munro, S. P. Purcell, G. P. Starley, D. M. Slaughter, and
D. W. Pershing
This summarizes a 3-year laboratory
study of factors controlling the forma-
tion of nitrogen and sulfur oxides (NO>
and SOX) in industrial coal-fired boilers,
with emphasis on stoker-fired units.
The study identified the combustion
phenomena governing conversion of
coal constituents to NOK and SO*, and
investigated approaches to controlling
these emissions. The study also consid-
ered possible detrimental effects of
control technology on boiler operation.
Study results indicate that two types
of NO, controls appear to be viable: (1)
the coal feed could be screened to
remove the fines (particles less than 0.1
in.), essentially eliminating the high conver-
sion of nitrogen evolved in the suspen-
sion zone and resulting in an overall
emissions reduction of about 10-40%,
depending on the amount of fines
normally present in the raw coal; or (2)
the primary overfire-air injection port
could be moved to above the spreader
and the suspension zone and bed region
could both be operated substoichi-
ometric, reducing emissions by as much
as 50%. Unfortunately, controlling SO2
formation in either a spreader or mass-
burning stoker unit appears to be diffi-
cult. Coal/limestone pellets can signif-
icantly reduce SOz emissions, and the
effectiveness of the sorbent appears to
increase when the bed-region stoichi-
ometry is reduced below 1.0.
This Project Summary was developed
by EPA's Industrial Environmental Re-
search Laboratory, Research Triangle
Park, NC, to announce key findings of
the research project that is fully docu-
mented in a separate report of the same
title (see Project Report ordering infor-
mation at back).
Purpose and Scope
This report summarizes the results of a
3-year research program to study the
formation and control of nitrogen and
sulfur oxides (NOX and SOX) in industrial
coal-fired boilers with emphasis on
stoker-fired units. In particular, this pro-
gram considered the following major
research areas:
1. the evolution and oxidation of fuel
nitrogen and sulfur;
2. the retention of SOX by ash and/or
solid-chemical sorbents; and
3. the effectiveness of distributed air
addition for NO« control.
In addition, the study attempted to quanti-
fy the combustion process in a stoker
environment and considered possible
detrimental effects of control technology
on boiler operation. The work considered
conditions typical of both spreader-stoker
and mass-burning systems.
The approach was primarily experi-
mental; three types of laboratory furnaces
were utilized to investigate the various
combustion regimes of major importance
in stoker-fired systems:
1. A 200,000 Btu/hr tower furnace
was used to characterize the sus-
pension phase oxidation of fuel
nitrogen and sulfur as a function of
local oxygen concentration, temper-
ature, and particle size.
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2. A 300,000 Btu/hr//xe-6et/furnace
was used to study NO, and SO,
formation in mass-burning units as
a function of stoichiometry distribu-
tion, burning rate, and overfire-air
height. The effectiveness of coal-
limestone pellets for SO, control
was also considered in this system.
3. A 750,000 Btu/hr model spreader-
stoker furnace was used to investi-
gate NO,formation and control in a
system where both suspension-
phase and bed combustion are
significant.
All of the experimental studies were
conducted with high volatile bituminous
coals from Utah (low sulfur) and Indiana
(high sulfur).
Complete details of all of the experi-
mental systems (including fabrication
drawings), analytical methods, and experi-
mental data are available.
Discussion
Study results indicate that NO emis-
sions from spreader-stoker fired coal
furnaces are the result of relatively high
conversions (25-45%) of the fuel nitrogen
evolved from particles less than 0.11 in.
in the suspension phase and low conver-
sions (5 to 15%) of fuel nitrogen from the
bed combustion. Mass-burning stokers
(e.g..traveling grate units) almost certain-
ly yield lower NO, emissions because of
the absence of significant overthrow
combustion. In the suspension phase, the
nitrogen is evolved at approximately the
same rate as the carbon is oxidized, and
the percentage conversion is relatively
insensitive to reaction zone temperature.
Decreasing particle size dramatically in-
creases the amount of fuel nitrogen
evolved; however, it had little effect on
the percentage conversion of that nitro-
gen to NOx.
Local oxygen availability is the primary
control parameter for both phases of the
combustion. Substantial NO, emission
reductions were achieved when the fuel
bed was operated under substoichio-
metric conditions (fuel rich). NO, emis-
sions decreased further when the stoi-
chiometry of the suspension zone was
reduced below 1.0 by, moving the overf ire
air injection to above the spreader. Under
these conditions, a minimum overall fuel
nitrogen conversion of approximately 6%
was achieved, suggesting that under
staged combustion conditions, positive
synergism can be achieved between the
suspension phase and the bed combus-
tion. The suspension zone almost certain-
ly provides both the sites for heterogen-
eous reduction of NO formed in the bed
and the free radical concentrations neces-
sary to accelerate the decay of total fixed
nitrogen formed in the bed. In addition,
the low oxygen partial pressure decreases
the conversion of nitrogen evolved in the
suspension zone.
Thus, two types of NO, control technol-
ogy appear to be viable. First, the coal
feed could be screened to remove the
fines (particles less than 0.1 in.). This
would essentially eliminate the high
conversion of nitrogen evolved in the
suspension zone and would result in an
overall emissions reduction of approxi-
mately 10 to 40%, depending on the
amount of fines normally present in the
raw coal. Alternatively, the primary
overfire-air injection port could be moved
to above the spreader and the suspension
zone and bed region could both be
operated substoichiometric. This could
result in an emission reduction as large
as 50%; however, before this concept can
be applied commercially, the influence on
other important combustion parameters
(e.g., bed thickness, grate temperature,
and ash characteristics) should be eval-
uated.
Unfortunately, control of SOzformation
in either a spreader or mass-burning
stoker unit appears to be difficult. The
rate of sulfur evolution and oxidation in
both the suspension and fixed-bed phases
can be influenced by local temperature;
however, if the coal is completely burned,
the sulfur is ultimately oxidized to S02.
Utilization of coal/limestone pellets can
result in significantly reduced SOz emis-
sions, and the effectiveness of the sorbent
appears to increase when the bed-region
stoichiometry is reduced be'low 1.0.
S. C. Mam's, J. M. Munro. S. P. Purcell, G. P. Starley, D. M. Slaughter, and D. W.
Pershing are with the University of Utah, Salt Lake City. UT84112.
G. Blair Martin is the EPA Project Officer (see below).
The complete report, entitled "Pollutant Formation During Fixed-Bed and
Suspension Coal Combustion," (Order No. PB 84-163 286; Cost: $11.50,
subject to change) will be available only from:
National Technical Information Service
5285 Port Royal Road
Springfield, VA 22161
Telephone: 703-487-4650
The EPA Project Officer can be contacted at:
Industrial Environmental Research Laboratory
U.S. Environmental Protection Agency
Research Triangle Park, NC 27711
-t( U.S GOVERNMENT PRINTING OFFICE; 1984 —759-015/7634
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United States
Environmental Protection
Agency
Center for Environmental Research
Information
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Official Business
Penalty for Private Use $300
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