化工学报 ›› 2025, Vol. 76 ›› Issue (6): 2667-2677.DOI: 10.11949/0438-1157.20241447

• 流体力学与传递现象 • 上一篇    下一篇

微通道内两相吸收剂TETA/DEEA吸收CO2过程的传质研究

米晓天1(), 刘宏臣1(), 王克军2, 唐文娜1, 徐永伟1, 杨梅3   

  1. 1.西安工程大学环境与化学工程学院,陕西 西安 710048
    2.山东阳谷华泰化工股份有限公司,山东 聊城 252300
    3.中国科学院大连化学物理研究所,辽宁 大连 116023
  • 收稿日期:2024-12-13 修回日期:2025-01-07 出版日期:2025-06-25 发布日期:2025-07-09
  • 通讯作者: 刘宏臣
  • 作者简介:米晓天(2000—),女,硕士,2279072974@qq.com
  • 基金资助:
    国家自然科学基金项目(22208256);西安工程大学科研启动基金项目(107020460)

Mass transfer study of CO2 absorption by TETA/DEEA biphasic absorbent in the microchannel

Xiaotian MI1(), Hongchen LIU1(), Kejun WANG2, Wenna TANG1, Yongwei XU1, Mei YANG3   

  1. 1.School of Environmental and Chemical Engineering, Xi’an Polytechnic University, Xi’an 710048, Shaanxi, China
    2.Shandong Yanggu Huatai Chemical Co. , Ltd. ,Liaocheng 252300, Shandong, China
    3.Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, Liaoning, China
  • Received:2024-12-13 Revised:2025-01-07 Online:2025-06-25 Published:2025-07-09
  • Contact: Hongchen LIU

摘要:

利用高速摄像研究了微通道内两相吸收剂三乙烯四胺/二乙氨基乙醇(TETA/DEEA)的CO2吸收传质特性,系统考察了气液两相流量、吸收剂总胺浓度及总胺中TETA占比对初始气泡长度LB0、气泡体积减小量ΔVB、CO2吸收率φ和液侧体积传质系数kLa的影响。结果表明,LB0与ΔVB密切相关,均随液体流量、总胺浓度和总胺中TETA占比的增加,以及气体流量的降低而降低。CO2吸收率随气体流量的增加而降低,随总胺中TETA占比的增加呈现先增加后降低的趋势。实验测得的kLa值在0.88~13.65 s-1之间,比传统反应器高1~2个数量级,表明微通道反应器可显著强化TETA/DEEA两相吸收剂捕集CO2过程。此外,基于实验数据提出了kLa预测关联式,预测效果较好。

关键词: 微通道, 两相吸收剂, 吸收, 气液两相流, 传质

Abstract:

The CO2 absorption and mass transfer characteristics of the TETA/DEEA (triethylenetetramine/diethylaminoethanol) biphasic absorbent solution in the microchannel were investigated by high-speed video, and the effects of two-phase flow rates, absorbent concentration, and TETA proportion in the total amine on the initial bubble length LB0, bubble volume reduction ΔVB, CO2 absorption percent φ and liquid-side volumetric mass transfer coefficient kLa were systematically examined. The results show that LB0 is closely related to ΔVB, and both decrease with the increase of liquid flow rate, total amine concentration and the proportion of TETA in total amines, as well as the decrease of gas flow rate. For CO2 absorption percent, it decreased with the increase of gas flow rate, and showed a tendency of increasing and then decreasing with the increase of TETA proportion. The experimentally measured kLa values ranged from 0.88 s-1 to 13.65 s-1, which were 1—2 orders of magnitude higher than those of the conventional reactor, indicating that the microchannel reactor can significantly enhance the CO2 capture process by the TETA/DEEA biphasic absorbent. In addition, based on the experimental data, an empirical correlation was proposed to predict the kLa with good prediction performance.

Key words: microchannels, biphasic absorbent, absorption, gas-liquid flow, mass transfer

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