Micro-interface enhanced mass transfer sodium carbonate absorption carbon dioxide reaction
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Micro-interface enhanced mass transfer sodium carbonate absorption carbon dioxide reaction
Micro-interface enhanced mass transfer sodium carbonate absorption carbon dioxide reaction
中国化学工程学报(英文版)2023年64卷第12期 页码:208-223
Affiliations:
Key Laboratory of Mesoscopic Chemistry of Ministry of Education (MOE), School of Chemistry and Chemical Engineering, Nanjing University,Nanjing,China,210023
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纸质出版:2023
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Hu Shen, Yingyu Xu, Jigang An, 等. Micro-interface enhanced mass transfer sodium carbonate absorption carbon dioxide reaction[J]. 中国化学工程学报(英文版), 2023,64(12):208-223.
Hu Shen, Yingyu Xu, Jigang An, Bowen Jiang, Jinnan Sun, Guoqiang Yang, Zhibing Zhang. Micro-interface enhanced mass transfer sodium carbonate absorption carbon dioxide reaction[J]. Chinese Journal of Chemical Engineering, 2023, 64(12): 208-223.
Hu Shen, Yingyu Xu, Jigang An, 等. Micro-interface enhanced mass transfer sodium carbonate absorption carbon dioxide reaction[J]. 中国化学工程学报(英文版), 2023,64(12):208-223.DOI:
Hu Shen, Yingyu Xu, Jigang An, Bowen Jiang, Jinnan Sun, Guoqiang Yang, Zhibing Zhang. Micro-interface enhanced mass transfer sodium carbonate absorption carbon dioxide reaction[J]. Chinese Journal of Chemical Engineering, 2023, 64(12): 208-223.DOI:
Micro-interface enhanced mass transfer sodium carbonate absorption carbon dioxide reaction
Micro-interface intensified reactor (MIR) can be applied in series/parallel in the absorption of CO
2
in industrial gases by Na
2
CO
3
due to the ability to produce large numbers of stable microbubbles. This work focuses on the variation pattern of mass transfer characteristics parameters of the reaction gas in Na
2
CO
3
solution under the influence of different solution properties and operating parameters in the reaction of CO
2
absorption by Na
2
CO
3
. The mass transfer characteristics parameters include bubble Sauter mean diameter
gas holdup
interfacial area
liquid side mass transfer coefficient
and liquid side volume mass transfer coefficient
k
L
a
. The solution properties and operating parameters include Na
2
CO
3
concentration (0.05–2.0 mol·L
-1
)
superficial gas velocity (0.00221–0.01989 m·s
-1
)
superficial liquid velocity (0.00332–0.02984 m·s
-1
)
and ionic strength (1.42456–1.59588 mol·kg
-1
). And volumetric mass transfer coefficients
k
L
a
and superficial reaction rates
r
of the MIR and the bubble column reactor are compared in
the reaction of sodium carbonate absorption of carbon dioxide
and the former shows a greater improvement under different solution properties and operating parameters. The enhanced role of MIR in mass transfer in non-homogeneous reactions is verified and the feasibility of industrial practical applications of MIR is demonstrated.
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