Hydrothermal
oxidation (HTO) provides an efficient technique to completely destroy
wet organic wastes. In this study, HTO was applied to treat fecal
sludge at well-defined experimental conditions. Four different kinetic
models were adjusted to the obtained data. Among others, a distributed
activation energy model (DAEM) was applied. A total of 33 experiments
were carried out in an unstirred batch reactor with pressurized air
as the oxidant at temperatures of <470 °C, oxygen-to-fuel
equivalence ratios between 0 and 1.9, feed concentrations between
3.9 and 9.8 molTOC L–1 (TOC = total organic
carbon), and reaction times between 86 and 1572 s. Decomposition of
the fecal sludge was monitored by means of the conversion of TOC to
CO2 and CO. In the presence of oxygen, ignition of the
reaction was observed around 300 °C, followed by further rapid
decomposition of the organic material. The TOC was completely decomposed
to CO2 within 25 min at 470 °C and an oxygen-to-fuel
equivalence ratio of 1.2. CO was formed as an intermediate product,
and no other combustible products were found in the gas. At certain
reaction conditions, the formation of unwanted coke and tarlike products
occurred. The reaction temperature and oxygen-to-fuel equivalence
ratio showed a significant influence on TOC conversion, while the
initial TOC concentration did not. Conversion of TOC to CO2 could be well described with a first-order rate law and an activation
energy of 39 kJ mol–1.