the National Natural Science Foundation of China(52476120);the Key international Cooperation of Qingdao City. The author is very grateful for the support of these projects(24-1-6-ghgg-9-hz)
DOI:
中图分类号:
收稿:2025-07-28,
修回:2025-12-30,
录用:2026-01-03,
网络首发:2026-02-06,
纸质出版:2026-06
Accepted:
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Yuan Xiaoying, Wang Xiaoran, Zheng Zhihao, 等. Kinetic characteristics and redox performance of iron-based oxygen carriers blending with iron-rich sludge ash[J]. 中国化学工程学报(英文), 2026,94(6):223-231.
Yuan Xiaoying, Wang Xiaoran, Zheng Zhihao, et al. Kinetic characteristics and redox performance of iron-based oxygen carriers blending with iron-rich sludge ash[J]. Chinese Journal of Chemical Engineering, 2026, 94(6): 223-231.
Yuan Xiaoying, Wang Xiaoran, Zheng Zhihao, 等. Kinetic characteristics and redox performance of iron-based oxygen carriers blending with iron-rich sludge ash[J]. 中国化学工程学报(英文), 2026,94(6):223-231.DOI:
Yuan Xiaoying, Wang Xiaoran, Zheng Zhihao, et al. Kinetic characteristics and redox performance of iron-based oxygen carriers blending with iron-rich sludge ash[J]. Chinese Journal of Chemical Engineering, 2026, 94(6): 223-231.DOI:
Kinetic characteristics and redox performance of iron-based oxygen carriers blending with iron-rich sludge ash
To investigate the redox performance and kinetic characteristics of iron-based oxygen carriers when mixed with iron-rich sludge ash during the sludge chemical looping gasification or combustion
the impregnation method was used to prepare Fe/Al composite oxygen carriers (Fe/Al-OC)
and the iron-rich sludge ash (IRSA) was produced by high-moisture sludge burning in Muffle stove. The two types powder were then mixed in a 1:1 mass ratio to obtain another OC of Fe1Ash1. Using a the
rmogravimetric analyzer
the deep redox processes of the three oxygen carriers were carried out
and their reduction under variable temperature or constant temperature and oxidation processes were analyzed using 13 kinetic models to investigate their kinetic parameters. The results showed that the blending of Fe/Al-OC and IRSA exhibited a synergistic effect
in which the actual oxygen release and oxygen gain amount of Fe1Ash1 both exceed the theoretical values
indicating enhanced oxygen transport capacity. During the reduction process
under non-isothermal conditions
the oxygen release in Fe/Al-OC was controlled by two-dimensional diffusion
while the oxygen release in IRSA and Fe1Ash1 followed a first-order reaction model
with Fe1Ash1 having a slightly lower activation energy (34.81 kJ·mol
- 1
) than the individual OCs. During isothermal reduction
the reaction of Fe/Al-OC transitions to contraction model control as temperature increases
while Fe1Ash1 reaction is more compatible with the F3/2 model
with synergistic effects weakening. During the oxidation process
Fe/Al-OC follows a first-order reaction model
while IRSA and Fe1Ash1 both follow two-dimensional diffusion models
but the activation energy of Fe1Ash1 (34.60 kJ·mol
- 1
) is significantly lower than that of the other two
resulting in superior oxidation performance. Thus the Fe/Al OC might achieve complementary performance and kinetic characteristics in redox with more sludge ash blending. The highest ash blending proportion that can promote oxygen carrying capacity would be studied in next works.
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