United States
                     Environmental Protection
                     Agency
Air and Energy Engineering
Research Laboratory
Research Triangle Park, NC 27711
                     Research and Development
EPA/600/SR-93/170   December 1993
&EPA      Project Summary

                     Biomass Gasification
                     Pilot  Plant  Study
                     A.M. Furman, S.G. Kimura, R.E. Ayala, and J. F. Joyce
                       A gasification pilot program carried
                     out at  General  Electric's (GE's)  Re-
                     search and Development Center, using
                     two biomass feedstocks:  bagasse  pel-
                     lets and wood chips. The object of the
                     testing was to determine the properties
                     of biomass  product gas  and its suit-
                     ability as a  fuel for gas-turbine-based
                     power  generation cycles.  The feed-
                     stocks were gasified at a feed  rate of
                     about 1 ton/hr*, using GE's pressur-
                     ized, fixed-bed gasifier  and a  single
                     stage of cyclone paniculate removal,
                     operating at 538°C. The biomass prod-
                     uct gas was  analyzed for chemical com-
                     position, paniculate loading, fuel-bound
                     nitrogen (FBN) levels, and sulfur  and
                     alkali metal content.
                       Both  feedstocks gasified easily.  The
                     composition and heating value  of the
                     biomass product gas were compatible
                     with  gas  turbine combustion  require-
                     ments. However, the paniculate removal
                     performance of the pilot facility single-
                     stage cyclone did  not  meet turbine
                     specifications. In addition, alkali metal
                     compounds  in the paniculate matter (at
                     538°C)  carried  over from the gasifier
                     exceeded turbine limits. Improved par-
                     ticulate removal technology, designed
                     specifically for biomass feedstock char-
                     acteristics, could meet turbine require-
                     ments for both  paniculate and alkali
                     loading. FBN compounds were also
                     measured since they can be convened
                     to nitrogen  oxides (NOx) during com-
                     *Readers more familiar with metric units may use the
                      following factors to convert to that system: 1 ton = 907
                      kg, and 1 atm = 98 kPa.
bustion in  a gas turbine.  Since  this
conversion is highly dependent on gas
turbine combustor design, no firm con-
clusions regarding NOx production can
be reached without actual combustion
testing.
  This Project Summary was developed
by the U.S. EPA's Air and Energy Engi-
neering Research Laboratory, Research
Triangle Park, NC, to announce key find-
ings of the research project that is fully
documented in a separate report of the
same title (see Project Report ordering
information at back).

Introduction
  The gasification performance of two bio-
mass feedstocks—wood chips and ba-
gasse—was evaluated  in the pilot Inte-
grated  Gasification Combined  Cycle
(IGCC) facility located at GE's Research
and Development Center in Schenectady,
NY. The overall objective of this program
was to evaluate biomass as  a feedstock
for a biomass gasification/gas turbine sys-
tem, which  is a potentially cost-effective
and highly efficient approach for using for-
est and agricultural wastes for power gen-
eration. Specific objectives were to mea-
sure gas composition and to determine
whether the product gas would meet gas
turbine requirements.
  The  pilot IGCC  facility  consists of a
pressurized, fixed-bed gasifier  with a nomi-
nal  operating pressure  of 20 atm and a
hot  gas cleanup system, consisting  of a
high-temperature cyclone, a solid-sorbent
desulfurization system, and  a polishing
cyclone. The gasifier has a  nominal ca-
pacity for  coal gasification of 1  ton/hr.
Since desulfurization is not an issue for
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the biomass  feedstocks  evaluated, only
the gasifier and high-temperature cyclone
were used. The product gas was flared.
  Because the pilot gasifier and its asso-
ciated fuel feeding system were designed
for operation on coal, the issue of feeding
of biomass,  with  its  lower density  and
different  flow properties, was  addressed
before gasification testing. Bagasse, which
was supplied as small cylindrical pellets,
was found to feed  easily with some modi-
fications  to  the  fuel feeding equipment.
However, it was  necessary to  evaluate
several  wood chip samples  before  one
was found that  could  be fed  at the re-
quired feed rate.
  A total of 42.5 tons of bagasse  was
gasified during a 32-hr test, and 83.8  tons
of wood  chips were gasified in an 81-hr
test. These quantities of fuel represented
the total fuel available to the program.
Wood chips  were provided by  the  Ver-
mont Department  of Public Service.  The
bagasse pellets were  obtained from the
Winrock  International  Institute for Agricul-
tural Development.
   Both  biomass  fuels gasified  readily.
Their reactivity was higher than that for
coal. Gasification capacities of both fuels
were limited by feed rate  or system ca-
pacity, and not by  gasification kinetics.
Product  gas compositions  for  both biom-
ass feedstocks indicated that they would
have combustion  characteristics compat-
ible with gas turbine combustor require-
ments. However, particulate removal per-
formance of the single cyclone was inad-
equate to  meet fuel contaminant  specifi-
cations. In particular, alkali  metals, which
are present in the fine particulate material
carried over from the gasifier and which
cause  hot corrosion on gas turbine hot
gas  path  components,  were present at
levels well in excess of turbine specifica-
tion limits. The low density  of particulates
and their poor flow properties, which made
removal from the cyclone difficult, caused
the cyclone  to perform poorly. This result
was not unexpected since the cyclone had
been designed for removing contaminants
from coal gas. In order to achieve con-
taminant levels consistent  with  gas tur-
bine requirements, it will be necessary to
improve particulate removal. This improve-
ment is well within  the state-of-the-art of
particulate cleanup technology.
   A second class  of contaminant mea-
sured was fuel-bound nitrogen (FBN) com-
pounds. Typical  of these  are ammonia,
cyanides,  and nitrogen-containing organic
compounds. A large fraction of  FBN will
be converted to nitrogen oxides (NOx) dur-
ing combustion  in  conventional gaxs tur-
bine combustors. Thus, when stringent NOx
emissions  requirements (< 10 ppm) are in
effect, it may be necessary to  consider
alternative  approaches to  reducing the
level of this pollutant.  One potential ap-
proach is to utilize  advanced combustion
techniques  such  as "rich-quench-lean" to
reduce the conversion of FBN. This tech-
nology is still in an early stage of develop-
ment and will  require significant effort to
bring it to a suitable stage of commercial
readiness. A second approach  is to cool
the fuel gas and "scrub" the gas with wa-
ter to remove  the FBN compounds. This
approach lowers the overall plant  effi-
ciency,  reduces  the heating value of the
fuel, and creates an environmental  dis-
posal problem associated  with the  dis-
posal of  the  "scrub" water.  Other ap-
proaches include the use of commercially
available selective  catalytic  reduction
(SCR) technology to reduce the NO level
in the  exhaust gas.  Note that  FBNJ  pro-
duction is a strong function of both the
feedstock and gasifier,  with higher tem-
perature gasifiers such  as  fluidized  and
entrained gasifiers  producing  less FBN
than fixed-bed gasifiers. A  system trade-
off  study would  help determine the  best
system level approach  to  NOx reduction
by  identifying  the capital equipment  cost
differences and  the associated plant effi-
ciency impact on the overall system de-
sign.
  The tests at  the  GE-CRD  pilot plant
have demonstrated the  successful gasifi-
cation  of biomass and  the general  suit-
ability of biomass fuel gas for use in a gas
turbine. Areas of possible future develop-
ment include improved particulate removal,
improved low  NOx combustion, and pre-
and post-gas cleanup.
   These accomplishments represent a key
step  in the  overall  development of  a
Biomass-IGCC power generation system
                                                                       -&U.S. GOVERNMENT PRINTING OFFICE: I«W4 - 550-067/80140

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A. Furman, S. Kimura, R. Ayala, and J. Joyce are with GE Research and Develop-
  ment Center, Schenectady, NY 12301.
Carol R. Purvis is the EPA Project Officer (see below).
The complete report, entitled "Biomass Gasification Pilot Plant Study," (Order No.
  PB94-114766/AS;  Cost: $27.00; 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
United States
Environmental Protection Agency
Center for Environmental Research Information
Cincinnati, OH 45268

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