C. Roy et al., CHARACTERIZATION AND CATALYTIC GASIFICATION OF THE AQUEOUS BY-PRODUCTFROM VACUUM PYROLYSIS OF BIOMASS, Canadian journal of chemical engineering, 72(1), 1994, pp. 98-105
Spruce wood residues were treated in a vacuum pyrolysis Process Develo
pment Unit with a throughput capacity of 28 kg/h. Two aqueous phase co
ndensate samples with COD concentration varying between 190 and 255 g/
L were produced and sequentially extracted with dichloromethane and et
hylacetate solvents. The soluble organic matter was composed of acidic
, phenolic, alcoholic and ketonic compounds. The insoluble fraction wa
s sequentially distilled at 100 and 110-degrees-C under atmospheric pr
essure. Mainly water was recovered in the first distillate, while the
second distillate contained 30.4% formic and acetic acids, 69.4% water
and 0.2% residual organic compounds. The distillation residue was ric
h in oxygen and was essentially insoluble in any organic solvent. The
two aqueous phase pyroligneous samples were treated in Battelle's Ther
mochemical Envirornmental Energy System (TEES(R)), a registered servic
e mark of OnsiteOfsite, Inc. of Duarte, California, U.S.A. The result
s of the tests showed that similar results were obtained with either f
eedstock. In batch tests a COD reduction of 99% was achieved. The prod
uct gas composition was typically about 49 % methane, 5 % hydrogen, 1%
ethane and 45% carbon dioxide. Tests in a continuous stirred-tank rea
ctor produced reproducible data which can be used for process scale-up
. Catalyst lifetime was identified as needing further improvement. The
preliminary results demonstrated the technical feasibility of the cat
alytic gasification process as a useful step in the recovery of energy
from the secondary condensate stream and the cleanup of the by-produc
t water from vacuum pyrolysis of wood.