TY - JOUR
T1 - Enhancing CO2 capture efficiency
T2 - CFD investigation of gas–liquid self-suction reactor configurations
AU - Li, Xingyan
AU - Xie, Suwen
AU - Liu, Huazong
AU - Gan, Jian
AU - Jiang, Zhou
AU - Wang, Luyao
AU - Zhu, Hongyu
AU - Li, Ganlu
AU - Li, Hui
AU - Chen, Kequan
N1 - Publisher Copyright:
© 2024 Elsevier B.V.
PY - 2025/7/8
Y1 - 2025/7/8
N2 - The separation and removal of industrial waste gases (such as CO2) has broad prospects. Efficient gas separation and removal equipment is the key to the purification of industrial waste gases. In this study, a new type of gas separation and purification reaction equipment was designed that can effectively improve the capture of CO2. The Propeller self-suction impeller coupled with the dynamic membrane–aeration impeller (Propeller + DMAI, also SDMSR) is the best impeller combination, achieving a gas holdup (εG) of up to 11.4 % and a volume mass transfer coefficient (kLa) of up to 0.061 s−1. Compared with other combinations, εG and kLa are significantly improved. Additionally, compared with the dynamic membrane–stirred reactor (DMSR) and self-suction stirred reactor (SSR), SDMSR enhances CO2 mass transfer and gas recovery, with a CaCO3 nucleation rate constant of 1.37 s−1, which is 11.38 % and 52.22 % higher than DMSR and SSR, respectively. In summary, this study provides a reference for the separation and purification of special gases.
AB - The separation and removal of industrial waste gases (such as CO2) has broad prospects. Efficient gas separation and removal equipment is the key to the purification of industrial waste gases. In this study, a new type of gas separation and purification reaction equipment was designed that can effectively improve the capture of CO2. The Propeller self-suction impeller coupled with the dynamic membrane–aeration impeller (Propeller + DMAI, also SDMSR) is the best impeller combination, achieving a gas holdup (εG) of up to 11.4 % and a volume mass transfer coefficient (kLa) of up to 0.061 s−1. Compared with other combinations, εG and kLa are significantly improved. Additionally, compared with the dynamic membrane–stirred reactor (DMSR) and self-suction stirred reactor (SSR), SDMSR enhances CO2 mass transfer and gas recovery, with a CaCO3 nucleation rate constant of 1.37 s−1, which is 11.38 % and 52.22 % higher than DMSR and SSR, respectively. In summary, this study provides a reference for the separation and purification of special gases.
KW - Dynamic membrane
KW - Fine bubble
KW - Gas recovery
KW - Gas–liquid mass transfer
KW - Self-suction reactor
UR - http://www.scopus.com/inward/record.url?scp=85211438767&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2024.130979
DO - 10.1016/j.seppur.2024.130979
M3 - 文章
AN - SCOPUS:85211438767
SN - 1383-5866
VL - 360
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 130979
ER -