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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

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