United States
                    Environmental Protection
                    Agency
Air and Energy Engineering
Research Laboratory
Research Triangle Park, NC 27711
                    Research and Development
 EPA/600/S8-89/060  May 1990
x>EPA          Project Summary
                    Municipal Waste  Combustion
                    Assessment: Waste Co-Firing
                    V.J. Landrum and P.J. Schindler
                     This report provides an overview of
                   waste co-firing  and  auxiliary fuel
                   fired technology and identifies the
                   extent to which co-firing and auxiliary
                   fuel firing are  practiced. Waste co-
                   firing is defined as the combustion of
                   wastes (e.g., sewage sludge,  medical
                   waste, wood waste, and agricultural
                   waste)  In  a unit designed to burn
                   municipal  solid waste (MSW)  or
                   refuse derived fuel  (RDF) as  a major
                   fraction  of  total fuel Input Auxiliary
                   fuel firing  is defined as the practice
                   whereby coal, fuel oil, or natural gas
                   is fired  in  a municipal   waste
                   combustor  under condititions when
                   waste feed quantities are interrupted.
                   This is a fairly common practice for
                   dedicated RDF boilers, and there may
                   be additional mass burn MWCs that
                   meet the definition of auxiliary fuel
                   firing.  This  report  includes
                   descriptions of technologies used  by
                   facilities that meet  these definitions,
                   characterizes the  population, and
                   discusses design and operating
                   practices  and available emissions
                   data from  each facility. THe report
                   concludes  with  a  discussion   of
                   recommended  good  combustion
                   practices for  waste co-firing
                   combustors and  auxiliary fuel fired
                   MWCs.
                     This  Project   Summary was
                   developed  by EPA's Air and  Energy
                   Engineering Research Laboratory,
                   Research  Triangle Park,  NC,  to
                   announce key findings of the research
                   project that is fully  documented In a
                   separate report of the same title (see
                   Project Report ordering Information at
                   back).

                   Introduction
                     Waste  co-firing is defined   as the
                   combustion of  wastes (e.g..sewage
                   sludge, medical waste, wood waste, and
agricultural waste) in a unit designed to
burn MSW or RDF as a major fraction of
total fuel  input.  All  MWC designs have
the potential to be waste co-firing units:
however, some facility operating permits
specify the extent to which waste can be
co-fired. Auxiliary fuel firing is defined as
the practice whereby coal,  fuel oil or
natural gas is fired in a municipal waste
combustor under conditions when waste
feed quantities are interrupted. This is a
fairly common  practice for  dedicated
RDF boilers, and there may be additional
mass burn MWCs that meet the definition
of auxiliary fuel firing.

Refuse Derived Fuel Firing
  RDF combustion technology includes
suspension firing, semi-suspension firing,
and fluidized  bed  combustion.
Suspension firing is restricted largely to
fossil  fuel co-fired  units.  Nearly  all
dedicated RDF combustors are spreader
stokers,  which  burn RDF in a semi-
suspension mode. The RDF is normally
injected  into the  combustor through
airswept  distributors on the front wall of
the furnace. A portion of the fuel burns in
suspension and the  remainder falls to a
traveling grate where burnout  is
completed. All RDF spreader stokers use
waterwall  boilers to produce  steam and,
in some  cases, generate electricity, and
most of these units are equiped with oil
or natural gas burners that can provide
up to 100% of design heat input.
  A Fluidized Bed Combustor (FBC) is a
reaction vessel containing a bed of inert
solid particles (typically sand, limestone,
or alumina), which  is fluidized by the
upward flow of gas  (air). Combustion in
the FBC  occurs primarily within the bed,
which is  interspersed with the fluidizing
air and particles of  fuel and ash. FBCs
are characterized by extremely  efficient
mass and heat transfer, i.e. very uniform
temperatures and mass compositions are

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observed in  both  the  bed  and  the
freeboard.  Efficient  mass and heat
transfer allows both conventional and
waste fueled FBCs  to operate at lower
excess air and temperature levels than
conventional  combustion  systems. Waste
fired FBCs typically operate  at excess air
levels between 30 and 100% (5-10% 02
in the  dry  flue  gas)  and  at  bed
temperatures around 815°C.
  There are  many  types of mass burn
MWCs in the  existing   population  of
facilities,  including  large field-erected
units with individual capacities of 100-
1000 tpd (91-907 tonnes/day),  and
modular shop-fabricated  units  of  5-120
tpd (4.5-109  tonnes/day).  The large mass
burn systems include conventional mass
burn  waterwall combustors,  rotary
waterwall combustors, and refractory wall
incinerators.  All of the large mass burn
units operate in an excess air mode, with
typical  excess air  levels of  30-150%.
Most modular  mass burn units include
multiple combustion chambers, with  the
waste burning  in the  primary  chamber
and  burnout of  combustible  products
being  completed  in  a  secondary
chamber.
  Several MWC  facilities meet the
definition of  waste  co-firing combustors
by  burning  sewage  sludge,  medical
waste, or wood waste, in  a unit designed
to burn MSW or RDF as  a major fraction
of total fuel input. Six plants that routinely
burn sewage sludge with municipal solid
waste have been identified in the existing
MWC population. The plants  include units
using conventional  mass  burn  waterwall
combustors,  mass  burn  refractory wall
combustors,  modular  excess air com-
bustors, and  FBCs. The average sewage
sludge  mass input ranges from 1-10% for
five facilities and  is 74% for  the FBC
facility which was primarily designed as a
sewage sludge incinerator. An additional
facility has  sewage  sludge  handling
equipment, although it has never been
used, and plant personnel report that
there are no  future  plans to  co-fire
sludge. At least nine facilities in planning,
permitting, and construction  phases may
burn a mixture of  MSW and  sewage
sludge.
  At least  15 MWC  facilities  have
previously accepted  or are currently
accepting  medical waste, including three
mass burnwaterwall, three mass burn
refractory, three modular starved air,  five
modular  excess air,  and one  FBC.
Medical waste ranges  from  less than 1-
50% by  weight of  the  total feed. The
design and  operating  characteristics of
these  facilities are described  in  the
"Municipal  Waste   Combustion
Assessment, Medical Waste Combustion
Practices at MWC Facilities, July  1989,
EPA-600/8-89-062."  Many new MWC
projects are planned for construction  in
the next few years. All of these facilities
have the  potential  to  accept medical
waste along with MSW.  Existing facilities
also have the potential to begin accepting
medical waste with their MSW. There are
strong  economic incentives  for other
MWCs to accept medical  waste; much
higher  tipping fees can  be charged for
medical waste than for MSW. As a result
of these incentives, there  is  a  high
potential for additional MWCs to accept
medical waste routinely.
  Wood waste is  routinely  fired in  three
MWC facilities. The annual average  mass
input of wood waste is  10-40%. At least
13 facilities in planning, permitting, and
construction phases  may burn a mixture
of wood and MSW.

Auxiliary  Fuel Firing
  Auxiliary fuel firing  is  limited to MWCs
that produce steam, and is  generally
practiced only as necessary to maintain
steam  load when waste  supplies are
curtailed  or interrupted.  Although some
mass burn facilities may fire auxiliary fuel
when waste is not available, auxiliary fuel
firing is more commonly  practiced by
RDF spreader  stokers  than  by other
designs. Because of the manner in which
feeding  takes  place  (air  swept
distributors),  plugging   of  feed
mechanisms  is a  more persistent
problem  in  RDF spreader stokers.
Therefore,  it is necessary to have the
ability to fire an auxiliary fuel in order  to
maintain  steam  load  when these
problems  occur. These facilities are
described  briefly  below. Most  RDF
spreader  stoker  facilities are  equipped
with natural gas as the auxiliary fuel with
rated  capacities  of  14-100%. Coal can
provide 100%  of the rated capacity for
these facilities.At least one  additional
RDF-fired facility  was designed  to  burn
RDF and/or coal. However,  the units have
not burned coal for  several  years, and
there  are  no  plans to  resume  this
practice.  Two  additional facilities  have
been identified that  plan to co-fire  RDF
and coal in FBC boilers.  Currently,  no
chlorinated  dibenzo-p-dioxin/chlorinated
dibenzofuran  (CDD/CDF  data  are
available  from RDF spreader stokers co-
firing coal.  Testing at Mid-Connecticut in
1988-89 should provide these data.
  Emissions were tested at the Albany,
NY facility in 1984 while firing 100% RDF
and also while  firing  RDF with   15%
natural gas. CDD/CDF  emissions  were
measured in the stack during both tests.
The  tetra-  through  hepta-CDD/CDF
homolog groups were quantified (no octa-
CDD/CDF) for both test conditions. Total
CDD/CDF  emissions  were 440 ng/dscm
while firing 100% RDF, and 840 ng/dscm
while firing 85% RDF with  15%  natural
gas. The natural gas burners are on the
rear wall of the boiler about half  way
between the traveling grate and the over
fire air  ports. It is suspected that, when
the gas burners are operating,  mixing
patterns may be disrupted in the boiler,
increasing vertical gas  velocities in  the
lower portion of the combustion chamber.
This  may allow pockets of  unburned
material (gaseous and  solid) to escape
from  the boiler without  being  properly
mixed,  resulting  in  higher CDD/CDF
emissions in the stack.
  The  existing  population of waste  co-
fired MWCs includes  all combustor
designs, and each  of these combustors
can potentially  burn  a wide variety ol
waste  and  fossil fuel  mixtures.  The
currently  available emissions data base
does not support any conclusion that, foi
a  given combustor  design,  CDD/CDF
emissions  from waste co-firing facilities
will differ substantially from 100% MSV\
or RDF combustion.  CDD/CDF emission;
have   been  measured  from  man}
combustion sources,  including units  tha
burn  sewage sludge, wood, coal,   ant
medical waste. However, for these fuels
CDD/CDF emission  levels  appear t(
depend more on combustion  condition:
than on waste feed characteristics.

Good Combustion Practices
  The  good  combustion  practice
developed  for   MSW  and  RDI
combustors are based  on two mai
concepts:
  1) Sufficient mixing must be  achieve
   at  a  temperature  adequate  t
    maximize  the destruction  of trac
    organics.
  2)Conditions  that  promote   lo
    temperature formation  of trac
    organics must be minimized.
These  basic concepts apply to all MW
systems, and hence, to all waste co-firir
MWCs. They  are necessary  conditior
for minimization of CDD/CDF emissions.
  The  requirements  that will minimu
CDD/CDF  emissions  do not change  wi
waste  feed.  However,  when firing
mixture of wastes  and/or  fossil fuel
conditions  may  arise  that  will  lirr
operation.  For example, the high moistu
content of sewage sludge may impose
maximum  sludge firing rate  to mainte
the required temperature  at  the  fu
mixed  location. A typical  sewage sludi
with 20% solids and  a dry heating val

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of 7000 Btu/lb (1.63 x 10? J/kg) will have
  net as-fired  heat  input  near zero.
.'herefore, the heat required to maintain
temperatures in  the combustor must be
contributed from an additional source. It
may be   necessary  for  mass  burn
systems to have air preheat or to fire an
auxiliary fuel when burning MSW/sludge
mixtures. These considerations  are
important  when  designing new systems
or retrofitting existing  MWCs  to  fire
sludge along with MSW. Sometimes,
excess air levels and combustion  air
distributions will  also  change  slightly
when co-firing waste.
  Combustion of wood waste, particularly
in RDF spreader stokers, may contribute
to high carryover of entrained particulate
matter, which  may  contribute  to low-
temperature downstream  formation
mechanisms  that  lead  to   higher
CDD/CDF  emissions.  As a  result, it  is
important to  design  all  systems  to
minimize the  potential  for  these
conditions.
  Auxiliary fuel firing in MWCs should be
designed so  that  adequate mixing  at
necessary temperatures occurs for all
firing   conditions.   This    can
beaccomplished  by  conducting  flow
modeling studies  on new and existing
boilers to determine the optimum location
and firing rate for auxiliary  fuel burners
that will  be  used in combination  with
MSW or RDF combustion.  By applying
appropriate  design  and   operating
practices to ensure good mixing, auxiliary
fuel  firing  MWCs  can maintain  low
emissions of air pollutants.

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  V. Landrum and P. Schindler are with Energy and Environmental Research Corp.,
        Durham, NC 27707.
  James D. Kilgroe is the EPA Project Officer (see below).
  The complete report, entitled "Municipal Waste Combustion Assessment: Waste
        Co-Firing," (Order No. PB90-161 001/AS; Cost: $15.00, 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:
           Air and Energy Engineering Research Laboratory
           U.S. Environmental Protection Agency
           Research Triangle Park, NC 27711
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