Development and application of deep eutectic solvents in carbon dioxide capture

doi:10.16085/j.issn.1000-6613.2024-2118

Chemical Industry and Engineering Progress ›› 2025, Vol. 44 ›› Issue (9): 5377-5390.DOI: 10.16085/j.issn.1000-6613.2024-2118

• Resources and environmental engineering • Previous Articles

Development and application of deep eutectic solvents in carbon dioxide capture

CHEN Siming¹^,²^,³(), LIU Jingchao⁴, ZHONG Zhixuan⁵, ZHANG Xinzhu³, ZHU Tianhao⁶, PENG Yiqing⁶, YOU Sai⁶, WANG Yikai⁶, YUAN Jiajun⁶, ZHANG Yongchun⁷()

^1.Institute of Carbon Neutralization, China University of Mining and Technology, Xuzhou 221116, Jiangsu, China
^2.Jiangsu Key Laboratory of Coal-based Greenhouse Gas Control and Utilization, China University of Mining and Technology, Xuzhou 221116, Jiangsu, China
^3.School of Chemical Engineering, China University of Mining and Technology, Xuzhou 221116, Jiangsu, China
^4.School of Environmental Science and Engineering, Qingdao University, Qingdao 266075, Shandong, China
^5.School of Resources and Geosciences, China University of Mining and Technology, Xuzhou 221116, Jiangsu, China
^6.SUNYUEQI Honors College, China University of Mining and Technology, Xuzhou 221116, Jiangsu, China
^7.School of Chemical Engineering, Dalian University of Technology, Dalian 116024, Liaoning, China

Received:2024-12-30 Revised:2025-05-09 Online:2025-09-30 Published:2025-09-25
Contact: CHEN Siming, ZHANG Yongchun

低共熔溶剂在二氧化碳捕集中的发展与应用

陈思铭¹^,²^,³(), 刘景超⁴, 钟志轩⁵, 张新柱³, 祝天浩⁶, 彭毅勍⁶, 游赛⁶, 王一凯⁶, 袁嘉骏⁶, 张永春⁷()

^1.中国矿业大学碳中和研究院，江苏徐州 221116
^2.中国矿业大学江苏省煤基温室气体减排与资源化利用重点实验室，江苏徐州 221116
^3.中国矿业大学化工学院，江苏徐州 221116
^4.青岛大学环境科学与工程学院，山东青岛 2660754
^5.中国矿业大学资源与地球科学学院，江苏徐州 221116
^6.中国矿业大学孙越崎学院，江苏徐州 221116
^7.大连理工大学化工学院，辽宁大连 116024

通讯作者: 陈思铭,张永春
作者简介:陈思铭（1988—），女，博士，副研究员，硕士生导师，研究方向为CO₂捕集与转化。E-mail：chensiming@cumt.edu.cn。
基金资助:
国家自然科学基金青年基金(52006112);徐州市重点研发计划社会发展项目(KC23293);中国博士后科学基金(2023M743768)

Abstract

Abstract:

The development of CO₂ capture, utilization and storage (CCUS) technology represents a critical step toward mitigating the rising global CO₂ concentration. Among various approaches, chemical absorption stands out as a particularly important CO₂ capture technique. However, traditional chemical absorption methods are hindered by limitations such as short operational lifespans, high energy consumption and corrosive effects. Deep eutectic solvents (DESs) have emerged as a promising class of novel CO₂ chemical absorbents thanks to their exceptional physicochemical properties and environmental friendliness. This paper reviewed the current research progress on DESs in the field of CO₂ capture, exploring their definitions, physicochemical properties and application categories. Furthermore, it examined key parameters influencing the CO₂ capture performance of DESs including the selection of hydrogen bond acceptors (HBAs) and hydrogen bond donors (HBDs), molar ratios, moisture content, temperature and pressure. Finally, this paper synthesized findings on various types and performances of DESs, proposing a molecular design strategy for developing DESs with enhanced CO₂ capture efficiency. The goal was to provide a scientific foundation for advancing the development and optimization of DESs technology, facilitating the application of green solvents in CO₂ capture and contributing to sustainable development.

Key words: CO₂ capture, deep eutectic solvents, hydrogen bond donors, hydrogen bond acceptors, molecular design

摘要：

CO₂捕集、利用和封存（CCUS）技术的开发是遏制全球CO₂浓度增高的关键措施。其中以化学吸收为代表的CO₂捕集技术尤为关键，然而传统化学吸收方法存在着低寿命、高能耗与腐蚀性等问题。低共熔溶剂（DESs）以其优异的物理化学性质及环境友好性，已成为开发新型CO₂化学吸收剂的热点。本文总结了DESs在CO₂捕集领域的研究现状，并深入探讨了其定义、物理化学特性及应用分类。随后进一步分析了影响DESs捕集CO₂性能的因素，包括氢键受体（HBAs）和氢键供体（HBDs）的选择、摩尔比、水分含量、温度和压力等。最后，综合现有DESs种类及性能，提出了高效捕集CO₂的DESs分子设计策略，旨在为未来DESs的开发和技术优化提供科学依据，以推进绿色溶剂在捕集CO₂和促进可持续发展中的应用。

关键词: CO₂捕集, 低共熔溶剂, 氢键供体, 氢键受体, 分子设计

CLC Number:

CHEN Siming, LIU Jingchao, ZHONG Zhixuan, ZHANG Xinzhu, ZHU Tianhao, PENG Yiqing, YOU Sai, WANG Yikai, YUAN Jiajun, ZHANG Yongchun. Development and application of deep eutectic solvents in carbon dioxide capture[J]. Chemical Industry and Engineering Progress, 2025, 44(9): 5377-5390.

陈思铭, 刘景超, 钟志轩, 张新柱, 祝天浩, 彭毅勍, 游赛, 王一凯, 袁嘉骏, 张永春. 低共熔溶剂在二氧化碳捕集中的发展与应用[J]. 化工进展, 2025, 44(9): 5377-5390.

Figures/Tables 5

类型	通式	组成
Ⅰ	Cat⁺X^-zMCl _x	M=Zn, Sn, Fe, Al, Ga, In等
Ⅱ	Cat⁺X^-zMCl _x ·yH₂O	M=Cr, Co, Cu, Ni, Fe等
Ⅲ	Cat⁺X^-zR^*Z	Z=CONH₂, COOH, OH
Ⅳ	MCl _x +R^Z $̿$ MCl $x - 1 +$ ·R^Z+MCl _x₊	M=Al, Zn等; Z=CONH₂, OH

类型	通式	组成
Ⅰ	Cat⁺X^-zMCl _x	M=Zn, Sn, Fe, Al, Ga, In等
Ⅱ	Cat⁺X^-zMCl _x ·yH₂O	M=Cr, Co, Cu, Ni, Fe等
Ⅲ	Cat⁺X^-zR^*Z	Z=CONH₂, COOH, OH
Ⅳ	MCl _x +R^Z $̿$ MCl $x - 1 +$ ·R^Z+MCl _x₊	M=Al, Zn等; Z=CONH₂, OH

HBA	HBD	HBA∶HBD	T/K	P/kPa	CO₂溶解度/mol·kg^-1	文献
BHDE	AC	1∶2	298.15	210~2026	0.064~0.84	[24]
BHDE	LA	1∶2	298.15	283~2086	0.016~0.50	[24]
BTEA	AC	1∶2	298.15	325~2054	0.13~0.97	[24]
BTMA	AC	1∶2	298.15	219~2037	0.078~1.45	[24]
BTMA	Gly	1∶2	298.15	394~2026	0.037~0.26	[24]
[BTPP]Br	EG	1∶12	298.15	1000	0.6	[23]
[BTPP]Cl	Gly	1∶12	298.15	1000	0.47	[23]
ChCl	MEA	1∶7	298.15	182~2035	0.78~3.58	[24]
Gua	MEA	1∶2	298.15	226~2025	0.31~1.66	[24]
MTPP	PG	1∶4	298.15	220~2026	0.022~0.55	[24]
MTPP	AC	1∶4	298.15	173~2014	0.073~3.02	[24]
MTPP	EG	1∶3	298.15	192~2018	0.045~0.35	[24]
MTPP	Gly	1∶4	298.15	161~2026	0.009~0.29	[24]
MTPP	LV	1∶3	298.15	301~2068	0.024~0.69	[24]
MTPP	MEA	1∶6	298.15	1000	1.63	[23]
MTPP	MEA	1∶7	298.15	1000	1.46	[23]
MTPP	MEA	1∶8	298.15	1000	1.44	[23]
TBAC	DecA	1∶2	298.15~323.15	90~1990	0.042~1.52	[25]
[N₈₈₈₁]Br	DecA	1∶2	298.15~323.15	90~1990	0.041~1.31	[25]
[N₈₈₈₁]Cl	DecA	1∶2	298.15~308.15	90~1990	0.045~1.35	[25]
[N₈₈₈₈]Br	DecA	1∶2	298.15~323.15	90~1990	0.039~1.33	[25]
[N₈₈₈₈]Cl	DecA	1∶1.5	298.15~323.15	90~1990	0.041~1.41	[25]
[N₈₈₈₈]Cl	DecA	1∶2	298.15~323.15	90~1990	0.042~1.41	[25]
TBAB	AC	1∶2	298.15	388~2011	0.14~1.13	[24]
TBAB	DEA	1∶6	298.15	1000	0.85	[23]
TBAB	MEA	1∶6	298.15	1000	1.34	[23]
TBAB	MEA	1∶6	298.15	351~2021	0.44~2.78	[24]
TBAB	MEA	1∶7	298.15	381~2040	0.53~3.01	[24]
TBAB	TEA	1∶3	298.15	1000	0.47	[23]
TBAC	AC	1∶2	298.15	348~2002	0.18~1.41	[24]
TEAC	AC	1∶2	298.15	281~2018	0.14~1.18	[24]
TEAC	AC	1∶3	298.15	397~2016	0.13~1.23	[24]
TEAC	OCT	1∶3	298.15	353~2018	0.16~1.39	[24]
TEMA	AC	1∶2	298.15	198~1837	0.081~1.18	[24]
TEMA	EG	1∶2	298.15	138~1345	0.062~0.63	[24]
TEMA	Gly	1∶2	298.15	150~1648	0.017~0.43	[24]
TEMA	LA	1∶2	298.15	143~1863	0.047~0.53	[24]
TEMA	LV	1∶2	298.15	136~1617	0.057~0.61	[24]
TMAC	AC	1∶4	298.15	294~2096	0.12~1.56	[24]
TPAC	AC	1∶6	298.15	350~2030	0.25~1.72	[24]
TPAC	MEA	1∶4	298.15	481~2009	0.34~1.43	[24]
TPAC	MEA	1∶7	298.15	357~2019	1.71~3.53	[24]

HBA	HBD	HBA∶HBD	T/K	P/kPa	CO₂溶解度(摩尔分数)	文献
ChCl	EG	1∶2	303.15	10000	0.046	[32]
ChCl	DEG	1∶3	303.15	8200	0.028	[32]
ChCl	DEG	1∶4	303.15	8300	0.028	[32]
TBAB	EG	1∶2	303.15	7800	0.031	[32]
TBAB	EG	1∶3	303.15	8800	0.039	[32]
TBAB	EG	1∶4	303.15	8300	0.032	[32]
TBAB	DEG	1∶2	303.15	7200	0.034	[32]
TBAB	DEG	1∶3	303.15	6900	0.040	[32]
TBAB	DEG	1∶4	303.15	9000	0.084	[32]
ChCl	MDEA	1∶6	303.15	7100	0.160	[32]
ChCl	MDEA	1∶7	303.15	5900	0.120	[32]
ChCl	DEA	1∶6	303.15	8000	0.078	[32]
TBTA	DEA	1∶6	303.15	6000	0.050	[32]
TBAB	MDEA	1∶3	303.15	8100	0.020	[32]
TBAB	MDEA	1∶4	303.15	7000	0.020	[32]
ChCl	PG	1∶2	303.15	9000	0.025	[34]
ChCl	GLY	1∶2	303.15	11000	0.030	[34]
ChCl	MA	1∶1	303.15	10000	0.025	[34]
TMG	PhAc	1∶2	313.15	400	(38.1±1.2)mg/g	[37]
TMG	GA	1∶2	313.15	400	(2.84±0.19)mg/g	[37]
TMG	EA	1∶2	313.15	400	(0.52±0.04)mg/g	[37]

HBA	HBD	助剂	HBA∶HBD∶助剂	T/K	P/kPa	CO₂溶解度(质量分数)/%	文献
ChCl	Gly	DBN	1∶2∶3	RT^③	101	9.6	[38]
ChCl	Gly	DBN	1∶2∶6	RT	101	10.3	[38]
ChCl	Gly	DBN	1∶2∶7	RT	101	10.5	[38]
ChCl	Gly	DBN	1∶2∶8	RT	101	10.3	[38]
ChCl	Gly	DBN	1∶3∶10	RT	101	10.4	[38]
ChCl	Gly	DBU	1∶2∶6	RT	101	3.55	[38]
ChCl	Gly	MTBD	1∶2∶6	RT	101	10	[38]
ChCl	MEA		1∶5	303.15	101	25.23	[38]
BmimCl	Im	DBN	1∶1∶1	298.15	101	(1.02)^①	[39]
BmimCl	Im	DBN	1∶1∶2	298.15	101	(0.97)^①	[39]
BmimCl	Im	DBN	1∶2∶1	298.15	101	(1.07)^①	[39]
DBN	DMLU		2∶1	318.15	101	4.27；2.47^②	[40]
DBN	DMU		2∶1	318.15	101	17.34；16.8^②	[38]
[HDBU][Im]	EG		7∶3	313.15	101	0.141	[40]
[HDBU][Ind]	EG		7∶3	313.15	101	0.117	[41]
[HDBU][Triz]	EG		7∶3	313.15	101	0.108	[41]
HmimCl	AP		1∶1	RT	101	2.0 (0.04)^①	[41]
HmimCl	AP		1∶2	RT	101	9.5 (0.21)^①	[41]
HmimCl	AP		1∶3	RT	101	13.9 (0.30)^①	[41]
HmimCl	AP		1∶4	RT	101	19.4 (0.37)^①	[41]
HmimCl	PEHA		1∶4	RT	101	8.4 (0.4)^①	[41]
HmimCl	DETA		1∶4	RT	101	22.8 (0.55)^①	[41]
HmimCl	EDA		1∶1	RT	101	9.0 (0.19)^①	[41]
HmimCl	EDA		1∶2	RT	101	25.0 (0.45)^①	[41]
HmimCl	EDA		1∶3	RT	101	26.7 (0.45)^①	[41]
HmimCl	EDA		1∶4	RT	101	30.8 (0.50)^①	[41]
HmimCl	TEPA		1∶4	RT	101	9.9 (0.39)^①	[41]
MEAC	AP		1∶1	RT	101	15.8 (0.28)^①	[41]
MEAC	AP		1∶2	RT	101	21 (0.37)^①	[41]
MEAC	AP		1∶3	RT	101	24.3 (0.42)^①	[41]
MEAC	AP		1∶4	RT	101	26.3 (0.46)^①	[41]
MEAC	DETA		1∶4	RT	101	25.5 (0.57)^①	[41]
MEAC	EDA		1∶1	RT	101	23.5 (0.38)^①	[41]
MEAC	EDA		1∶2	RT	101	30.9 (0.47)^①	[41]
MEAC	EDA		1∶3	RT	101	36.5 (0.54)^①	[41]
MEAC	EDA		1∶3	303.15	101	33.7	[41]
MEAC	EDA		1∶4	RT	101	39.0 (0.57)^①	[41]
MEAC	PEHA		1∶4	RT	101	12.7 (0.59)^①	[41]
MEAC	TEPA		1∶4	RT	101	16.6 (0.63)^①	[41]
[N2222][Im]	EG		1∶2	298.15	101	12.9 (0.94)^①	[41]
[N2222][Triz]	EG		1∶2	298.15	101	12.5 (0.92)^①	[42]
[P2222][Im]	EG		1∶2	298.15	101	11.8 (0.91)^①	[42]
[P2222][Triz]	EG		1∶2	298.15	101	11.8 (0.91)^①	[42]
MEACl	EDA		1∶3	303.15	101	31.5	[42]
TBAB	AMP		1∶3	RT	101	10.5 (0.35)^①	[43]
TBAB	AMP		1∶4	RT	101	12.2 (0.38)^①	[41]
TBAB	AP		1∶2	RT	101	11.1 (0.43)^①	[41]
TBAB	AP		1∶3	RT	101	15.6 (0.49)^①	[41]
TBAB	AP		1∶4	RT	101	18.1 (0.51)^①	[41]
TEAC	DA		1∶3	303.15	101	24.2	[41]
[TETA]Cl	DG		1∶2	313.15	101	0.159	[43]
[TEPA]Cl	thymol		1∶3	313.15	101	0.088 (1.355)^①	[44]
[TETA]Cl	EG		1∶3	313.15	101	0.175	[45]
[TETA]Cl	thymol		1∶3	313.15	101	0.09 (1.298)^①	[44]
UEC	EDA		1∶3	303.15	101	17.8	[45]
TPAC	EA		1∶6	298.15	20.0	0.276	[24]
TPAC	AC		1∶4	298.15	20.0	0.240	[24]
TPAC	AC		1∶7	298.15	20.0	0.435	[24]
TBAB	OCT+OA		1∶2	298.15	16.46	0.285	[24]
TPAC	DecA		1∶2	298.15	19.9	0.299	[46]
TMP	thymol		1∶3	313.15	10.13	1.355	[45]

HBA	HBD	助剂	HBA∶HBD∶助剂	T/K	P/kPa	CO₂溶解度(质量分数)/%	文献
ChCl	Gly	DBN	1∶2∶3	RT^③	101	9.6	[38]
ChCl	Gly	DBN	1∶2∶6	RT	101	10.3	[38]
ChCl	Gly	DBN	1∶2∶7	RT	101	10.5	[38]
ChCl	Gly	DBN	1∶2∶8	RT	101	10.3	[38]
ChCl	Gly	DBN	1∶3∶10	RT	101	10.4	[38]
ChCl	Gly	DBU	1∶2∶6	RT	101	3.55	[38]
ChCl	Gly	MTBD	1∶2∶6	RT	101	10	[38]
ChCl	MEA		1∶5	303.15	101	25.23	[38]
BmimCl	Im	DBN	1∶1∶1	298.15	101	(1.02)^①	[39]
BmimCl	Im	DBN	1∶1∶2	298.15	101	(0.97)^①	[39]
BmimCl	Im	DBN	1∶2∶1	298.15	101	(1.07)^①	[39]
DBN	DMLU		2∶1	318.15	101	4.27；2.47^②	[40]
DBN	DMU		2∶1	318.15	101	17.34；16.8^②	[38]
[HDBU][Im]	EG		7∶3	313.15	101	0.141	[40]
[HDBU][Ind]	EG		7∶3	313.15	101	0.117	[41]
[HDBU][Triz]	EG		7∶3	313.15	101	0.108	[41]
HmimCl	AP		1∶1	RT	101	2.0 (0.04)^①	[41]
HmimCl	AP		1∶2	RT	101	9.5 (0.21)^①	[41]
HmimCl	AP		1∶3	RT	101	13.9 (0.30)^①	[41]
HmimCl	AP		1∶4	RT	101	19.4 (0.37)^①	[41]
HmimCl	PEHA		1∶4	RT	101	8.4 (0.4)^①	[41]
HmimCl	DETA		1∶4	RT	101	22.8 (0.55)^①	[41]
HmimCl	EDA		1∶1	RT	101	9.0 (0.19)^①	[41]
HmimCl	EDA		1∶2	RT	101	25.0 (0.45)^①	[41]
HmimCl	EDA		1∶3	RT	101	26.7 (0.45)^①	[41]
HmimCl	EDA		1∶4	RT	101	30.8 (0.50)^①	[41]
HmimCl	TEPA		1∶4	RT	101	9.9 (0.39)^①	[41]
MEAC	AP		1∶1	RT	101	15.8 (0.28)^①	[41]
MEAC	AP		1∶2	RT	101	21 (0.37)^①	[41]
MEAC	AP		1∶3	RT	101	24.3 (0.42)^①	[41]
MEAC	AP		1∶4	RT	101	26.3 (0.46)^①	[41]
MEAC	DETA		1∶4	RT	101	25.5 (0.57)^①	[41]
MEAC	EDA		1∶1	RT	101	23.5 (0.38)^①	[41]
MEAC	EDA		1∶2	RT	101	30.9 (0.47)^①	[41]
MEAC	EDA		1∶3	RT	101	36.5 (0.54)^①	[41]
MEAC	EDA		1∶3	303.15	101	33.7	[41]
MEAC	EDA		1∶4	RT	101	39.0 (0.57)^①	[41]
MEAC	PEHA		1∶4	RT	101	12.7 (0.59)^①	[41]
MEAC	TEPA		1∶4	RT	101	16.6 (0.63)^①	[41]
[N2222][Im]	EG		1∶2	298.15	101	12.9 (0.94)^①	[41]
[N2222][Triz]	EG		1∶2	298.15	101	12.5 (0.92)^①	[42]
[P2222][Im]	EG		1∶2	298.15	101	11.8 (0.91)^①	[42]
[P2222][Triz]	EG		1∶2	298.15	101	11.8 (0.91)^①	[42]
MEACl	EDA		1∶3	303.15	101	31.5	[42]
TBAB	AMP		1∶3	RT	101	10.5 (0.35)^①	[43]
TBAB	AMP		1∶4	RT	101	12.2 (0.38)^①	[41]
TBAB	AP		1∶2	RT	101	11.1 (0.43)^①	[41]
TBAB	AP		1∶3	RT	101	15.6 (0.49)^①	[41]
TBAB	AP		1∶4	RT	101	18.1 (0.51)^①	[41]
TEAC	DA		1∶3	303.15	101	24.2	[41]
[TETA]Cl	DG		1∶2	313.15	101	0.159	[43]
[TEPA]Cl	thymol		1∶3	313.15	101	0.088 (1.355)^①	[44]
[TETA]Cl	EG		1∶3	313.15	101	0.175	[45]
[TETA]Cl	thymol		1∶3	313.15	101	0.09 (1.298)^①	[44]
UEC	EDA		1∶3	303.15	101	17.8	[45]
TPAC	EA		1∶6	298.15	20.0	0.276	[24]
TPAC	AC		1∶4	298.15	20.0	0.240	[24]
TPAC	AC		1∶7	298.15	20.0	0.435	[24]
TBAB	OCT+OA		1∶2	298.15	16.46	0.285	[24]
TPAC	DecA		1∶2	298.15	19.9	0.299	[46]
TMP	thymol		1∶3	313.15	10.13	1.355	[45]

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Development and application of deep eutectic solvents in carbon dioxide capture

低共熔溶剂在二氧化碳捕集中的发展与应用

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