Ikelic - Alliance Digital Repository
Ikelic - Alliance Digital Repository
Ikelic - Alliance Digital Repository
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GENERAL<br />
VERMONT BIOMASS GASIFIER WILL USE<br />
BATTELLE DESIGN<br />
A 200-ton per day biomass gasification plant is<br />
under construction at the McNeil generating sta<br />
tion in Burlington, Vermont. Potential feedstocks<br />
for the gasifier include wood waste, crop<br />
residues, yard wastes and energy crops. The<br />
project will be carried out in two phases. In the<br />
first phase, a 200-ton per day gasifier based on<br />
Battelle technology will be constructed and<br />
operated at the McNeil site. The product gas will<br />
be used in the existing McNeil power boilers. In<br />
the second phase, a gas combustion turbine will<br />
be installed to accept the product gas from the<br />
gasifier and form an integrated combined cycle<br />
system.<br />
The design and development of the Battelle<br />
biomass gasifier was described by M. Paisley of<br />
Battelle and R. Overend of the National Renew<br />
able Energy Laboratory at the 13th EPRI Con<br />
ference on Gasification Power Plants, held in San<br />
Francisco, California in October.<br />
The development of the indirectly-heated Battelle<br />
High Throughput Gasification Process was in<br />
itiated in 1977. Detailed process development<br />
activities began in 1980 with the construction and<br />
startup of a Process Research Unit (PRU) at<br />
Battelle's West Jefferson, Ohio Laboratory.<br />
Process Description<br />
The Battelle biomass gasification process<br />
produces a medium-BTU product gas without the<br />
need for an oxygen plant. The process<br />
schematic in Figure 1 shows the two reactors<br />
and their integration into the overall gasification<br />
process. This process uses two physically<br />
separate reactors: 1) a gasification reactor in<br />
which the biomass is converted into a medium-<br />
BTU gas and residual char and 2) a combustion<br />
reactor that burns the residual char to provide<br />
heat for gasification. Heat transfer between reac<br />
tors is accomplished by circulating sand between<br />
the gasifier and the combustor.<br />
1-12<br />
The gasification process utilizes circulating<br />
fluidized-bed reactors to take advantage of the<br />
inherently high reactivity of biomass feedstocks.<br />
The reactivity of biomass is such that through<br />
puts in excess of 3,000 pounds per hour per<br />
square foot can be achieved. In other gasifica<br />
tion systems throughput is generally limited to<br />
less than 200 pounds per hour per square foot.<br />
As an added benefit, the high heatup rates pos<br />
sible through indirect heating with a circulating<br />
sand phase along with the short residence times<br />
in the gasification reactor effectively reduce the<br />
tendency to form condensable tar-like materials<br />
which results in an environmentally simpler<br />
process.<br />
According to Paisley and Overend, the basic<br />
uniqueness of the Battelle process compared to<br />
other biomass gasification processes is that it<br />
was designed to exploit the unique properties of<br />
biomass while the other processes were either<br />
developed for coal gasification or were heavily in<br />
fluenced by coal gasification technology.<br />
Several characteristics of the process and the<br />
resulting benefits are:<br />
- Constant<br />
High Throughput-ln excess of<br />
3,000 Ib/hr-ft2. A 200-dry-ton per day<br />
facility<br />
will have a "footprint,"<br />
excluding<br />
biomass storage, of approximately<br />
20 feet by 30 feet and will utilize a gasifier<br />
less than 3 feet in diameter.<br />
Fuel Flexibility-The process has been<br />
demonstrated with a wide range of<br />
biomass fuels including sawdust, wood<br />
chips, shredded bark, hog fuel, refusederived<br />
fuel, and energy plantation crops<br />
such as hybrid poplar and switch grass.<br />
Gas Heating Value-By cir<br />
culating<br />
hot solids between the gasifier<br />
and combustion reactors, it is possible to<br />
produce a medium-BTU gas without re<br />
quiring<br />
oxygen in the gasifier. The cir-<br />
THE SYNTHETIC FUELS REPORT, JANUARY 1995