微通道反应器内低共熔溶剂/水混合物吸收CO2的传质特性OA北大核心CSTPCD
Mass transfer characteristics of CO2 absorption by deep eutectic solvents/water mixtures in microchannel reactor
为了探索低共熔溶剂在CO2 吸收过程中的应用前景,通过实验对康宁先进流动反应器内低共熔溶剂/水混合物吸收CO2 的传质特性进行了研究,并与目前常用的CO2 吸收剂(N-甲基二乙醇胺的质量分数为 30%的水溶液)进行了比较和分析.结果表明,当低共熔溶剂/水混合物吸收剂体积流量qV,L不变、气相体积流量qV,G增大时,反应器的吸收负荷、体积传质系数均随之增大;而吸收率在 qV,G较低时随 qV,G增大而增大,当 qV,G较大时,吸收率变化趋于平缓;当qV,G不变、qV,L增大时,吸收负荷、体积传质系数随之减小,但压降随之增大,而吸收率在qV,L较小时随qV,L增大而减小,当qV,L较大时变化趋近平缓.采用气、液相Re数、液相Sc数及增强因子等自变量,建立了体积传质系数关联式和压降关联式,平均绝对偏差分别为 4.19%和 1.74%,最大绝对偏差分别为 13.9%和 11.7%.
In order to explore the application of deep eutectic solvents(DESs)in CO2 absorption processes,mass transfer characteristics of CO2 absorption by DESs/water mixtures in the Advanced Flow Reactor of Corning were studied,and the results were compared with those of commonly used CO2 absorbents(30%mass fraction of N-methyldiethanolamine aqueous solution).The results show that when the liquid volume flow rate qV,L of the DESs/water mixture absorbent is kept constant,the absorption load of the reaction and volume mass transfer coefficient increase with the increase of gas volume flow rate qV,G.The absorptivity increased with qV,G at low qV,G,and at high qV,G the change of absorptivity became less obvious.When qV,G was kept constant and qV,L increased,the absorption load and volume mass transfer coefficient decreased,but the pressure drop increased.The absorptivity decreased with the increase of qV,L at low qV,L,and at high qV,L the change of absorptivity was also not obvious.By taking the gas/liquid Re number,Sc number of liquid phase and enhancement factor into account,the correlations for volumetric mass transfer coefficient and pressure drop were established with the average absolute deviations of 4.19%and 1.74%,and the maximum absolute deviations of 13.9%and 11.7%,respectively.
王彦旭;侯晓静;伍辛军;吴可君;何潮洪
浙江大学 化学工程与生物工程学院 浙江省化工高效制造技术重点实验室,浙江 杭州 310058浙江大学 化学工程与生物工程学院 浙江省化工高效制造技术重点实验室,浙江 杭州 310058||浙江大学衢州研究院,浙江 衢州 324000康宁反应器技术有限公司,江苏 常州 213000
化学工程
低共熔溶剂微通道反应器CO2 吸收气、液两相流
deep eutectic solventsmicrochannel reactorCO2 absorptiongas-liquid flow
《高校化学工程学报》 2024 (002)
184-194 / 11
国家自然科学基金(U22A20408,51874256),浙江省重点研发计划(2022C01179).
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