CO2 capture by a novel CaO/MgO sorbent fabricated from industrial waste and dolomite under calcium looping conditions

2019 ◽  
Vol 43 (13) ◽  
pp. 5116-5125 ◽  
Author(s):  
Xianyao Yan ◽  
Yingjie Li ◽  
Xiaotong Ma ◽  
Jianli Zhao ◽  
Zeyan Wang ◽  
...  

A synthetic sorbent prepared from carbide slag and dolomite by combustion exhibits high CO2 capture capacity, good cyclic stability and a porous microstructure.

2021 ◽  
Vol 218 ◽  
pp. 106845
Author(s):  
Yuping Hu ◽  
Shuimu Wu ◽  
Yingjie Li ◽  
Jianli Zhao ◽  
Shijian Lu

2013 ◽  
Vol 38 (31) ◽  
pp. 13655-13663 ◽  
Author(s):  
Rongyue Sun ◽  
Yingjie Li ◽  
Jianli Zhao ◽  
Changtian Liu ◽  
Chunmei Lu

RSC Advances ◽  
2016 ◽  
Vol 6 (106) ◽  
pp. 104303-104310 ◽  
Author(s):  
Changyun Chi ◽  
Yingjie Li ◽  
Rongyue Sun ◽  
Xiaotong Ma ◽  
Lunbo Duan ◽  
...  

Synthetic MgO/CaO sorbent prepared by industrial waste (carbide slag) experiencing various CO2 capture cycles can effectively capture HCl.


Author(s):  
Senthoorselvan Sivalingam ◽  
Stephan Gleis ◽  
Hartmut Spliethoff ◽  
Craig Hawthorne ◽  
Alexander Charitos ◽  
...  

Naturally occurring limestone and samples from a lab scale dual fluidized bed (DFB) calcium looping (CaL) test facility were analysed in a thermo gravimetric analyser (TGA). The reactivity of the samples evaluated at typical carbonation conditions prevailed in the carbonator was compared with raw samples. Carbonations were carried out at 600, 650 &700°C and 5, 10 &15 vol-% CO2 atmosphere using a custom designed sample holder that provided ideal conditions for solid gas contact in a TGA. The rate of carbonation and carbonation capacity of the samples were compared with respect to the following three categories: number of calcination-carbonation cycles, carbonation temperature and CO2 concentration. Notable differences in total conversion (XCaO) and the rates of conversions were observed between the raw and DFB samples in all three cases. It is suspected the much lower activity of the DFB sample is attributed to the differences in experimental conditions: ie., partial carbonation of the DFB particles, fast heating rate in the calciner and thus a rapid calcination reaction, and particle attrition in the CFB calciner riser. These harsh conditions lead sintering and thus a loss of surface area and reactivity. Sintered DFB samples showed low (nearly 1/3 of the raw samples) but stable conversions with increasing number of cycles. The sorbent taken from the DFB facility did not decrease with respect to carbonation rate or maximum conversion over 4 cycles whereas the fresh limestone changed significantly over 4 cycles. Hydration was used as an attempt to regenerate the lost capture capacity of partially carbonated DFB sample. Hydration of the sintered DFB sample was successful in increasing the maximum capture capacity in the fast reaction regime to values almost as high as that of a fresh sample in its first carbonation cycle. Although more investigation is required to investigate the effect of hydration on the CaO particle morphology, a process modification to enhance the CO2 capture efficiency of the carbonator via particle hydration was proposed.


Author(s):  
Senthoorselvan Sivalingam ◽  
Stephan Gleis ◽  
Hartmut Spliethoff ◽  
Craig Hawthorne ◽  
Alexander Charitos ◽  
...  

Naturally occurring limestone and samples from a lab-scale dual fluidized bed (DFB) calcium looping test facility were analyzed in a thermogravimetric analyzer. The reactivity of the samples evaluated at typical carbonation conditions prevailed in the carbonator was compared with raw samples. The rate of carbonation and carbonation capacity of the samples were compared with respect to the following three categories: number of calcination-carbonation cycles, carbonation temperature, and CO2 concentration. It is suspected that the much lower activity of the DFB sample is attributed to the differences in experimental conditions, i.e., partial carbonation of the DFB particles, fast heating rate in the calciner and thus a rapid calcination reaction, and particle attrition in the circulating fluidized bed calciner riser. These harsh conditions lead to sintering and thus a loss of surface area and reactivity. Sintered DFB samples showed low (nearly one-third of the raw samples) but stable conversions with increasing number of cycles. Hydration was used as an attempt to regenerate the lost capture capacity of partially carbonated and sintered DFB sample. Hydration of the DFB sample was successful in increasing the maximum capture capacity in the fast reaction regime to values almost as high as that of a fresh sample in its first carbonation cycle. Although more investigation is required to investigate the effect of hydration on the CaO particle morphology, a process modification to enhance the CO2 capture efficiency of the carbonator via particle hydration was proposed.


2021 ◽  
Vol 6 (1) ◽  
pp. 100-111
Author(s):  
Chunxiao Zhang ◽  
Yingjie Li ◽  
Yi Yuan ◽  
Zeyan Wang ◽  
Tao Wang ◽  
...  

The Ca/Mg-based composite prepared from carbide slag and dolomite is efficient for simultaneous CO2 capture and heat storage.


Fuel ◽  
2014 ◽  
Vol 127 ◽  
pp. 109-115 ◽  
Author(s):  
Antonio Coppola ◽  
Piero Salatino ◽  
Fabio Montagnaro ◽  
Fabrizio Scala

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