An experimental, theoretical, and kinetic modeling study of gas-phase sulfation of KCl

被引:0
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作者
Chanpirak, Arphaphon [1 ]
Wu, Hao [1 ]
Marshall, Paul [2 ,3 ,4 ]
Glarborg, Peter [1 ]
机构
[1] Tech Univ Denmark, DTU Chem Engn, DK-2800 Lyngby, Denmark
[2] Naresuan Univ, Fac Engn, Dept Ind Engn, Phitsanulok 65000, Thailand
[3] Univ North Texas, Dept Chem, Denton, TX USA
[4] Univ North Texas, Ctr Adv Sci Comp & Modeling, Denton, TX USA
关键词
KCl sulfation; Kinetic modeling; Flow reactor; POTASSIUM-CHLORIDE; THERMAL-CONVERSION; INORGANIC ELEMENTS; WOOD COMBUSTION; ALKALI; BIOMASS; AEROSOLS; RELEASE; SULFUR; NUCLEATION;
D O I
10.1016/j.fuel.2024.130974
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The effect of a radical pool on KCl sulfation by SO2 is investigated through flow reactor experiments on KCl sulfation with and without the presence of CO. These experiments, together with results reported in literature, are interpreted in terms of an updated chemical kinetic model for sulfation. In the absence of combustibles, the rate limiting step in the sulfation of KCl is the oxidation of potassium sulfite to potassium sulfate through the reaction KHSO3 + O2 -> KHSO4 + O (R17b). Based on chemical kinetic modeling of a range of sulfation experiments, the rate constant for the reverse, exothermic step KHSO4 + O is estimated to be k17 similar to 2 & sdot; 1012 cm3 mol-1 s-1. Oxidation of combustibles such as CO facilitates establishment of a radical pool that strongly promotes sulfation. In this case, the sulfation rate is controlled by the oxidation of SO2 to SO3, mostly through SO2 + O (+M) -> SO3 (+M). An alternative sulfation pathway involving KSO4 as an intermediate is discarded, because the formation through either KO2 + SO2 or KSO2 + O2 involves significant barriers to reaction.
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页数:10
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