YU Zhiyuan, ZHAO Bingtao, HE Shushen. Mass transfer performance of enhanced CO2 absorption in swirling flow field[J]. CIESC Journal, 2015, (3): 1012-1018. DOI: 10.11949/j.issn.0438-1157.20141353.
DOI:
YU Zhiyuan, ZHAO Bingtao, HE Shushen. Mass transfer performance of enhanced CO2 absorption in swirling flow field[J]. CIESC Journal, 2015, (3): 1012-1018. DOI: 10.11949/j.issn.0438-1157.20141353.DOI:
Mass transfer performance of enhanced CO2 absorption in swirling flow field
a reactor based on swirling and multi-staged liquid-gas contact was used to examine the mass transfer performance of long-concentration span CO2 (2.5%—15%) capture with NaOH solution. The effects of absorbent concentration
absorbent flow rate
CO2 concentration
gas flow rate and reaction temperature on volumetric overall mass transfer coefficient (Kga) were experimentally investigated. The mass transfer coefficient varied from 4.53×10-5 to 9.22×10-5 kmol·m-3·s-1·kPa-1 under the experimental conditions. Compared with axial spray with double stages and swirling spray with single stage
swirling-based multi-staged spray reactor was able to effectively enhance the performance of absorption of long-concentration span CO2. A high concentration and a high flow rate of the absorbent
and a high reaction temperature helped to increase Kga. Kga increased with the increase of CO2 concentration
but decreased while CO2 concentration was more than 5%. Kga increased and then stabilized with increase of gas flow rate.
Mass transfer study of CO2 absorption by TETA/DEEA biphasic absorbent in the microchannel
Mass transfer performance of CO2 absorption into ionic liquid/ethanol mixture in microchannel
Mass transfer and hydraulic performance of CO2 absorption by ionic liquids over structured packings
Mass transfer characteristics in gas-liquid swirling quench box with gas injection
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