Page 17 - 《精细化工》2023年第1期

第 1 期 赵然磊，等: 二氧化碳捕集化学吸收剂的研究进展 ·9·

using ionic liquids and CO 2 [J]. Nature, 1999, 399(6731): 28-29. capture from flue gas[J]. Chemical Industry and Engineering
[56] CUI G K (崔国凯), LYU S Z (吕书贞), WANG J J (王键吉). Progress (化工进展), 2022, 41(4): 2090-2101.
Functional ionic liquids for carbon dioxide capture and separation[J]. [70] PERRY R J, WOOD B R, GENOVESE S, et al. CO 2 capture using
CIESC Journal (化工学报), 2020, 71(1): 16-25, 429. phase-changing sorbents[J]. Energy & Fuels, 2012, 26(4): 2528-
[57] LI M Y (李孟盈), LYU C J (吕春捷), XU L H (徐立华), et al. 2538.
Research progress in CO 2 capture by ionic liquids-alkanolamine [71] ZHENG S D, TAO M N, QING L, et al. Capturing CO 2 into the
aqueous solutions[J]. Modern Chemical Industry (现代化工), 2021, precipitate of a phase-changing solvent after absorption[J]. Environmental
41(2): 70-74. Science & Technology, 2014, 48(15): 8905-8910.
[58] XIA P W (夏裴文), DING B H (丁保宏), ZHANG P J (张鹏军), [72] WANG X，AKHMEDOV N Q, HOPKINSON D, et a1. Phase change
et al. Preparation of amino acid ionic liquid and its absorption of amino acid salt separates into CO 2-rich and CO 2-lean phases upon
carbon dioxide[J]. Speciality Petrochemicals (精细石油化工), 2019, interacting with CO 2[J]. Applied Energy, 2016, 161: 41-47．
36(4): 74-78. [73] XU M M (许咪咪), WANG S J (王淑娟). Research progress in CO 2
[59] ZHANG D. Synthesis, characterization and properties of ether amino capture technology using liquid-liquid biphasic solvents[J]. CIESC
acid functionalized ionic liquids[D]. Shenyang: Liaoning University, Journal (化工学报), 2018, 69(5): 1809-1818.
2020. [74] ZHANG J, QIAO Y, WANG W, et al. Development of an energy-
[60] BATES E D, MAYTON R D, NTAI I, et al. CO 2 capture by a efficient CO 2 capture process using thermomorphic biphasic solvents[J].
task-specific ionic liquid[J]. Journal of the American Chemical Energy Procedia, 2013, 37: 1254-1261.
Society, 2002, 124(6): 926-927. [75] WANG L D, ZHANG Y F, WANG R J, et al. Advanced
[61] YU G R，FAN S S, CHEN X C, et al. CO 2 absorption by binary monoethanolamine absorption using sulfolane as a phasesplitter for
mixture of ionic liquids-monoethanol amine at lower pressure[J]. CO 2 capture[J]. Environmental Science & Technology, 2018, 52(24):
International Journal of Greenhouse Gas Control, 2016, 44: 52-58． 14556-14563.
[62] YANG J, YU X H, AN L, et al. CO 2 capture with the absorbent of a [76] KIERZKOWSKA-PAWLAK H, KATARZYNA S. Heat of absorption
mixed ionic liquid and amine solution considering the effects of SO 2 of CO 2 in aqueous solutions of DEEA and DEEA+MAPA blends—A
and O 2[J]. Applied Energy, 2017, 194: 9-18. new approach to measurement methodology[J]. International Journal
[63] LI J (李京), ZHAN Z G (湛志钢), DING C F (丁常富), et al. of Greenhouse Gas Control, 2020, 100: 103102.
Experimental study on decarbonization absorption enthalpy of [77] ZHANG W D, JIN X, TU W, et al. A novel CO 2 phase change absorbent:
N-methylcyclohexylamine (MCA)-ionic liquid aqueous solution and MEA/1-propanol/H 2O[J]. Energy & Fuels, 2017, 31(4): 4273-4279.
calculation of regenerative energy consumption[J]. Journal of North [78] ZHANG S, YAO S, SHAO P, et al. Kinetics, thermodynamics, and
China Electric Power University (华北电力大学学报), 2018, 45(5): mechanism of a novel biphasic solvent for CO 2 capture from flue
101-110. gas[J]. Environmental Science & Technology, 2018, 52(6): 3660-
[64] LIU Z H (刘忠海). Performance of carbon dioxide absorption/ 3668.
desorption in tetramethylammonium glycin complex solution[D]. [79] XU Z C, WANG S J, CHEN C H. CO 2 absorption by biphasic
Chongqing: Chongqing University, 2014. solvents: Mixtures of 1,4-butanediamine and 2-(diethylamino)- ethanol[J].
[65] GAO K X (高凯璇). Absorption of [N 1111][Gly] and DMEE mixed International Journal of Greenhouse Gas Control, 2013, 16(10):
anhydrous absorbent to CO 2[D]. Nanjing: Nanjing University (南京 107-115.
大学), 2016. [80] ZHANG J, QIAO Y, AGAR D W. Intensification of low temperature
[66] ZHANG F, FANG C G, WU Y T, et al. Absorption of CO 2 in the thermomorphic biphasic amine solvent regeneration for CO 2 capture
aqueous solutions of functionalized ionic liquids and MDEA[J]. [J]. Chemical Engineering Research and Design, 2012, 90(6):
Chemical Industry & Engineering Progress, 2013, 160(2): 691-697. 743-749．
[67] LYU B H (吕碧洪). Mechanism of mass transfer with chemical [81] KIM Y E, PARK J H, YUN S H, et a1. Carbon dioxide absorption
reaction of CO 2 absorption into the mixed aqueous solution of MEA using a phase transitional alkanolamine-alcohol mixture[J]. Journal
and ionic liquid[D]. Hangzhou: Zhejiang University (浙江大学), of Industrial and Engineering Chemistry, 2014, 20(4): 1486-1492.
2014. [82] ALEIXO M, PRIGENT M, GIBERT A, et al. Physical and chemical
[68] TU W W (涂巍巍), FANG J W (方佳伟), LI Z S (李竹石), et al. properties of DMXTM solvents[J]. Energy Procedia, 2011, 4: 148-
Development of CO 2 phase change absorbent based on MEA[J]. 155.
Scientia Sinica Chimica (中国科学:化学), 2018, 48(6): 641-647. [83] RAYNAL L, ALIX P, BOUILLON P, et al. The DMX™ process: An
[69] ZHANG W F (张卫风), ZHOU W (周武), WANG Q H (王秋华). original solution for lowering the cost of post-combustion carbon
Recent developments of phase-change absorption technology for CO 2 capture[J]. Energy Procedia, 2011, 4: 779-786.