A key step in the production of clean
energy from biomass gasification
is the cleaning of the product gas to remove impurities, such as tars,
H2S, HCl, particulates, and alkali compounds. Some gas
cleaning systems employ activated carbon (AC), with Brunauer–Emmett–Teller
(BET) surface areas in the range of 800–1300 m2/g.
Because the operational conditions for the production of AC are similar
to those applied in the gasification chamber of a dual fluidized bed
gasifier, the possibility to produce AC within the dual fluidized
bed gasification (DFBG) process was investigated in the present work.
Wood pellets were gasified with steam in a fluidized bed reactor at
800 and 840 °C. Part of the unconverted char from this process
was further activated with steam in a fixed bed reactor at 850 °C.
The results obtained indicate that if ≥44% of the char that
results from the devolatilization of the wood pellets is gasified
(the extent of char conversion), the unconverted char acquires a BET
surface area >900 m2/g, which makes it suitable for
use
in gas cleaning processes. Achieving this extent of char conversion
in the gasification chamber of industrial dual fluidized gasification
plants would remove the need and cost for a second reactor for further
activation of the unconverted char. The cost of the produced activated
carbon (AC) has been estimated as being 15-fold lower than that of
commercially available AC. This suggests that the production of AC
as part of the dual fluidized bed gasification process would be cost-effective.