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Optimum design and characteristics of potassium-based sorbents using SiO2 for post-combustion CO2 capture

Author

Listed:
  • Cho, Min Sun
  • Lee, Soo Chool
  • Chae, Ho Jin
  • Kwon, Yong Mok
  • Kim, Hyun Ji
  • Ryu, Min Young
  • Lee, Joong Beom
  • Kim, Jae Chang

Abstract

SiO2 is a common material and is used in various industrial fields. However, the potassium-based sorbents using SiO2 as a support have the low CO2 capture capacities. In this study, the CO2 sorption and regeneration properties of potassium-based sorbents using SiO2 as a support were investigated to determine the cause of the low CO2 capture capacities. In addition, an optimum design method of the potassium-based sorbents using SiO2 as a support having excellent performance was proposed. The CO2 capture capacities of the sorbents decreased as the calcination temperature increased from 500 °C to 700 °C owing to the disappearance of the active material (K2CO3) through the formation of inactive components, such as K2Si2O5 and K2Si4O9. On the other hand, the potassium-based sorbent using SiO2 calcined at 500 °C had a high CO2 capture capacity of 152.3 mg CO2/g sorbent and excellent regeneration properties under the process simulation conditions. Control of the calcination temperature and the mole ratio of K2CO3 to SiO2 was important for obtaining the sorbents with a high CO2 capture capacity. Consequently, SiO2 can be used as a support or additive material in the design of potassium-based sorbents with a high CO2 capture capacity and excellent regeneration properties for post-combustion CO2 capture by controlling the amount of inactive component formed in the calcination process.

Suggested Citation

  • Cho, Min Sun & Lee, Soo Chool & Chae, Ho Jin & Kwon, Yong Mok & Kim, Hyun Ji & Ryu, Min Young & Lee, Joong Beom & Kim, Jae Chang, 2019. "Optimum design and characteristics of potassium-based sorbents using SiO2 for post-combustion CO2 capture," Renewable Energy, Elsevier, vol. 144(C), pages 107-115.
  • Handle: RePEc:eee:renene:v:144:y:2019:i:c:p:107-115
    DOI: 10.1016/j.renene.2018.10.057
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    Cited by:

    1. Nam, Hyungseok & Won, Yooseob & Kim, Jae-Young & Yi, Chang-Keun & Park, Young Cheol & Woo, Jae Min & Jung, Su-Yeong & Jin, Gyoung-Tae & Jo, Sung-Ho & Lee, Seung-Yong & Kim, Hyunuk & Park, Jaehyeon, 2020. "Hydrodynamics and heat transfer coefficients during CO2 carbonation reaction in a circulated fluidized bed reactor using 200 kg potassium-based dry sorbent," Energy, Elsevier, vol. 193(C).

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