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CO2 capture at ambient temperature in a fixed bed with CaO-based sorbents

Author

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  • Ridha, Firas N.
  • Manovic, Vasilije
  • Macchi, Arturo
  • Anthony, Edward J.

Abstract

This work investigates post-combustion CO2 capture at ambient temperature in a fixed bed by means of CaO-based sorbents. Two sorbents were used: limestone and pellets prepared from powdered limestone using calcium aluminate cement as a binder. The results showed that pre-hydration had a significant effect on CO2 capture performance of the two sorbents. For instance, after 8h pre-hydration, the breakthrough time increased from 21min to 660min for lime, and from 19min to 750min for pellets. The performance of pellets was more sensitive to hydration conditions than for the lime. At breakthrough, full carbonation conversion over half of the reactor was achieved in a pre-hydrated bed of pellets exposed to a feed with 0.5% CO2, resulting in an average specific capture of 0.51gCO2/gbed material. This was considered a sufficient capture performance, with a distinct mass transfer zone (MTZ) located in the upper half of the reactor. However, increasing CO2 inlet concentration to 2% shortened the breakthrough time and shifted the MTZ toward the entrance zone of the reactor. It was concluded that capturing CO2 from low-CO2 flue gases at ambient temperature using a fixed bed of pre-hydrated CaO-based pellets is a promising approach that has the potential to achieve reasonable capture performance at relatively low cost. The proposed process can be used for CO2 capture from CO2-depleted flue gases (residual CO2) from processes such as amine scrubbing and calcium looping. And it would allow for the possibility that capture could be increased to any given level required by new legislation for plant with carbon capture.

Suggested Citation

  • Ridha, Firas N. & Manovic, Vasilije & Macchi, Arturo & Anthony, Edward J., 2015. "CO2 capture at ambient temperature in a fixed bed with CaO-based sorbents," Applied Energy, Elsevier, vol. 140(C), pages 297-303.
  • Handle: RePEc:eee:appene:v:140:y:2015:i:c:p:297-303
    DOI: 10.1016/j.apenergy.2014.11.030
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    3. Chen, S.J. & Zhu, M. & Fu, Y. & Huang, Y.X. & Tao, Z.C. & Li, W.L., 2017. "Using 13X, LiX, and LiPdAgX zeolites for CO2 capture from post-combustion flue gas," Applied Energy, Elsevier, vol. 191(C), pages 87-98.
    4. Erans, María & Jeremias, Michal & Zheng, Liya & Yao, Joseph G. & Blamey, John & Manovic, Vasilije & Fennell, Paul S. & Anthony, Edward J., 2018. "Pilot testing of enhanced sorbents for calcium looping with cement production," Applied Energy, Elsevier, vol. 225(C), pages 392-401.
    5. Ma, Xiaotong & Li, Yingjie & Shi, Lei & He, Zirui & Wang, Zeyan, 2016. "Fabrication and CO2 capture performance of magnesia-stabilized carbide slag by by-product of biodiesel during calcium looping process," Applied Energy, Elsevier, vol. 168(C), pages 85-95.
    6. Yu, Cheng-Hsiu & Chen, Ming-Tsz & Chen, Hao & Tan, Chung-Sung, 2016. "Effects of process configurations for combination of rotating packed bed and packed bed on CO2 capture," Applied Energy, Elsevier, vol. 175(C), pages 269-276.
    7. Abanades, Stéphane & André, Laurie, 2018. "Design and demonstration of a high temperature solar-heated rotary tube reactor for continuous particles calcination," Applied Energy, Elsevier, vol. 212(C), pages 1310-1320.
    8. Qi, Guojie & Wang, Shujuan, 2017. "Thermodynamic modeling of NH3-CO2-SO2-K2SO4-H2O system for combined CO2 and SO2 capture using aqueous NH3," Applied Energy, Elsevier, vol. 191(C), pages 549-558.
    9. Mutch, Greg A. & Anderson, James A. & Vega-Maza, David, 2017. "Surface and bulk carbonate formation in calcium oxide during CO2 capture," Applied Energy, Elsevier, vol. 202(C), pages 365-376.
    10. Yan, J. & Zhao, C.Y., 2016. "Experimental study of CaO/Ca(OH)2 in a fixed-bed reactor for thermochemical heat storage," Applied Energy, Elsevier, vol. 175(C), pages 277-284.

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