Limestone hydrogenation combined with reverse water-gas shift reaction under fluidized and iso-thermal conditions using MFB-TGA-MS

被引:25
|
作者
Wang, Iwei [1 ]
Li, Dan [1 ]
Wang, Shihui [1 ]
Wang, Yang [1 ]
Lin, Gang [2 ]
Yan, Binhang [2 ]
Li, Zhenshan [1 ]
机构
[1] Tsinghua Univ, Dept Energy & Power Engn, Key Lab Thermal Sci & Power Engn, Minist Educ, Beijing 100084, Peoples R China
[2] Tsinghua Univ, Dept Chem Engn, Beijing 100084, Peoples R China
关键词
Hydrogenation decomposition; Fluidization; MFB-TGA-MS; Morphology evolution; Model; CO2; CAPTURE; CACO3; DECOMPOSITION; CALCIUM-CARBONATE; KINETICS; CALCINATION; METHANATION; CONVERSION; PARTICLES; SORBENTS; DIOXIDE;
D O I
10.1016/j.cej.2023.144822
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The integrated CO2 capture and utilization (ICCU) in conjunction with the reverse water-gas shift (RWGS) reaction has emerged as a promising approach to achieve carbon neutrality. However, the scalability of CaCO3 hydrogenation in the context of large volumes of industrial flue gas is impeded by the limited understanding of its performance under fluidized and iso-thermal conditions. This study utilized micro-fluidized bed thermogravimetric analysis coupled with mass spectrometry (MFB-TGA-MS) and in-situ measurements to investigate limestone decomposition under H-2 and Ar atmospheres. Results showed that H-2 atmosphere increased the limestone decomposition rate by 5-fold (79.1% CO2 conversion and similar to 100% CO selectivity at 710 degrees C) compared to Ar, with RWGS as the dominant route and self-catalytic activity of calcined CaO. Morphology evolution revealed finer pores and textures under H-2 conditions. Meanwhile, apparent kinetic models analyzed experimental data and showed a reduction in activation energy from 178.5 kJ/mol (Ar) to 161.3 kJ/mol (H-2). These findings support the effectiveness of ICCU-RWGS approaches for further commercialization.
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页数:11
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