ZHENG Chuanjie, SHENG Changdong. Modeling and reaction kinetics study on K capture by adsorbents in high temperature flue gas[J]. CIESC Journal, 2019, 70(6): 2259-2268
ZHENG Chuanjie, SHENG Changdong. Modeling and reaction kinetics study on K capture by adsorbents in high temperature flue gas[J]. CIESC Journal, 2019, 70(6): 2259-2268DOI: 10.11949/j.issn.0438-1157.20181497.
Modeling and reaction kinetics study on K capture by adsorbents in high temperature flue gas
Aiming at the performance description of using adsorbent to control the behavior of K-containing gas in flue gas during biomass combustion
the performance and influencing factors of kaolin and coal fly ash trapping KOH (K
2
CO
3
)
KCl and K
2
SO
4
were investigated by one-dimensional plug flow reactor model. After comparing the model calculations with the experimental measurements in the literature to verify the rationality of the model and to determine the kinetic parameters
the differences in the performance of kaolin and coal fly ash adsorbing various K-containing gases were compared. The results showed that employing the global kinetic model and a single set of kinetic parameters was capable of predicting the amount of K captured by kaolin and coal fly ash under a wide range of reaction conditions and the kinetic parameters determined were reasonable. Within the given ranges of K concentration and flue gas temperature
the patterns of K capture by kaolin and coal fly ash were similar
both increasing with the increase of flue gas temperature and K concentration
but the effect of K concentration on kaolin adsorption was more obvious.
The capabilities of K adsorption by both kaolin and coal fly ash were: KOH
>
KCl
>
K
2
SO
4
but the adsorption capability of kaolin was much stronger than coal fly ash.
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