Spruce wood charcoal, macadamia shell charcoal, coal activated carbon,
and coconut shell activated carbon catalyze the gasification of organ
ic compounds in supercritical water. Feedstocks studied in this paper
include glycerol, glucose, cellobiose, whole biomass feedstocks (depit
hed bagasse liquid extract and sewage sludge), and representative Depa
rtment of Defense (DoD) wastes (methanol, methyl ethyl ketone, ethylen
e glycol, acetic acid, and phenol). The effects of temperature, pressu
re, reactant concentration, weight hourly space velocity, and the type
of catalyst on the gasification of glucose are reported. Complete con
version of glucose (22% by weight in water) to a hydrogen-rich synthes
is gas was realized at a weight hourly space velocity (WHSV) of 22.2 h
(-1) in supercritical water at 600 degrees C, 34.5 MPa. Complete conve
rsions of the whole biomass feeds were also achieved at the same tempe
rature and pressure. The destruction efficiencies for the representati
ve DoD wastes were also high. Deactivation of the carbon catalyst was
observed after 4 h of operation without swirl in the entrance region o
f the reactor, but the carbon gasification efficiency remained near 10
0% for more than 6 h when a swirl generator was employed in the entran
ce of the reactor.