Kinetics of carbon dioxide absorption from air in a flow reactor with a fixed bed of K2CO3-based sorbent
- 作者: Sivtsova O.1,2, Eremenko S.2, Derevschikov V.1,3, Veselovskaya J.1,3
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隶属关系:
- Novosibirsk State University
- TION
- Boreskov Institute of Catalysis
- 期: 卷 91, 编号 5 (2017)
- 页面: 850-855
- 栏目: Chemical Kinetics and Catalysis
- URL: https://journals.rcsi.science/0036-0244/article/view/169462
- DOI: https://doi.org/10.1134/S0036024417050223
- ID: 169462
如何引用文章
详细
Sorption of carbon dioxide from air in a flow reactor with a bulky fixed bed of the K2CO3/Al2O3 composite sorbent was studied. The dynamic sorption capacity of the material was shown to depend on the relative humidity of the inlet air. A numerical model was constructed for evaluating the profile of СО2 concentration in the layer and kinetic curves of CO2 breakthrough at the outlet of the reactor. The results of simulation allowed us to adequately describe the experimental kinetic curves at 20–40% humidity.
作者简介
O. Sivtsova
Novosibirsk State University; TION
编辑信件的主要联系方式.
Email: KOlgaN-01@yandex.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090
S. Eremenko
TION
Email: KOlgaN-01@yandex.ru
俄罗斯联邦, Novosibirsk, 630090
V. Derevschikov
Novosibirsk State University; Boreskov Institute of Catalysis
Email: KOlgaN-01@yandex.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090
J. Veselovskaya
Novosibirsk State University; Boreskov Institute of Catalysis
Email: KOlgaN-01@yandex.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090