An inherent water-soluble
sodium-loaded coal sample was prepared
using crown ether for this study. The pyrolysis process of an inherent
water-soluble sodium-loaded coal sample and a water-soluble sodium
compound-loaded coal sample was researched by thermogravimetric analysis
(TGA). Also, the pyrolysis kinetics of the coal samples were analyzed
and researched by the distributed activation energy model (DAEM).
The results show that the inherent water-soluble sodium is mainly
concentrated on coal particles, which further aggravates the degree
of the pyrolysis reaction. The presence of sodium can promote the
weight loss of coal samples in the preliminary stage of pyrolysis
and the thermal condensation stage, block the escape of volatile matter
during the main pyrolysis period, and inhibit the process of graphitization
of char. The activation energy of pyrolysis increases with the carbon
conversion rate, and the presence of sodium can reduce the activation
energy under the same carbon conversion rate.
A comprehensive study
was conducted to assess the co-gasification
characteristics of sewage sludge and high-sodium coal. As the gasification
temperature increased, the CO2 concentration was decreased,
and the concentrations of CO and H2 were increased, while
the change of CH4 concentration was not obvious. As the
coal blending ratio increased, the H2 and CO concentrations
initially increased and then decreased, while the CO2 concentration
initially decreased and then increased. The mixture of sewage sludge
and high-sodium coal shows the synergistic effect of co-gasification,
and the synergistic effect was to promote the gasification reaction
positively. The average activation energies of co-gasification reactions
were calculated by the OFW method, and the average activation energy
initially decreases and then increases as the coal blending ratio
increases. Both fluidized-bed gasification and thermogravimetric analyzer
gasification show that the optimum coal blending ratio is 0.6. Overall,
these results provide a theoretical basis for the industrial application
of sewage sludge and high-sodium coal co-gasification.
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