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武汉工程大学 化工与制药学院,湖北 武汉 430205
郑佳豪(2001—),硕士研究生,研究方向为碳捕集,E-mail:18834715561@163.com。
马倩(1996—),博士,研究方向为碳一转化,E-mail:mm1171228@163.com;
易群(1985—),博士,教授,研究方向为分离材料与过程强化,E-mail:yq20071001@163.com。
收稿:2026-02-06,
修回:2026-03-17,
网络首发:2026-06-29,
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郑佳豪,侯艺菲,史利娟等.ZIF-8/水相多孔吸附体系的构建及其CO2吸附性能研究[J].低碳化学与化工,DOI:10.12434/j.issn.2097-2547.20260069.
ZHENG Jiahao,HOU Yifei,SHI Lijuan,et al.Construction of ZIF-8/aqueous phase porous adsorption system and its CO2 capture performance study[J].Low-Carbon Chemistry and Chemical Engineering,DOI:10.12434/j.issn.2097-2547.20260069.
郑佳豪,侯艺菲,史利娟等.ZIF-8/水相多孔吸附体系的构建及其CO2吸附性能研究[J].低碳化学与化工,DOI:10.12434/j.issn.2097-2547.20260069. DOI:
ZHENG Jiahao,HOU Yifei,SHI Lijuan,et al.Construction of ZIF-8/aqueous phase porous adsorption system and its CO2 capture performance study[J].Low-Carbon Chemistry and Chemical Engineering,DOI:10.12434/j.issn.2097-2547.20260069. DOI:
作为实现碳减排的关键技术,CO
2
捕集、封存与利用正发挥着越来越重要的作用。然而,以传统多孔液体进行CO
2
捕集面临着依赖有机溶剂、成本高和环境不友好等问题。以ZIF-8为吸附质,筛选了稳定剂,调控了稳定剂与ZIF-8的质量比以及ZIF-8固含量(
m
(ZIF-8)/(
m
(ZIF-8) +
m
(水))),构建了ZIF-8/水相多孔吸附体系,并对其CO
2
吸附性能进行了测试。结果表明,聚乙烯醇(PVA)为优选稳定剂,在
m
(PVA):
m
(ZIF-8) = 1.0:0.5、ZIF-8固含量为5%时,体系具备良好的流动性与分散稳定性,在常温常压下(25 °C、101.3 kPa)的CO
2
吸附量为0.663 mmol/g。经过5次吸/脱附循环后,该体系的CO
2
吸附量仍保持在初始CO
2
吸附量的86%以上。本研究将为开发低成本、低能耗且环境友好的CO
2
吸附体系提供新思路。
As a key technology for achieving carbon reduction
CO
2
capture
storage
and utilization is playing an increasingly important role. However
CO
2
capture using traditional porous liquids faces problems such as dependence on organic solvents
high cost and environmental unfriendliness. Using ZIF-8 as the adsorption medium
stabilizers were screened
and the mass ratios of stabilizers to ZIF-8 and the ZIF-8 solid contents (
m
(ZIF-8)/(
m
(ZIF-8) +
m
(water))) were adjusted. The ZIF-8/aqueous phase porous adsorption system was constructed
and its CO
2
adsorption performance was tested. The results show that polyvinyl alcohol (PVA) is the preferred stabilizer. When
m
(PVA):
m
(ZIF-8) = 1.0:0.5 and the ZIF-8 solid content of 5%
the system exhibits good fluidity and dispersion stability
achieving a CO
2
adsorption capacity of 0.663 mmol/g at ambient temperature and pressure (25 °C
101.3 kPa). After five adsorption/desorption cycles
the CO
2
adsorption capacity remains above 86% of the initial CO
2
adsorption capacity. This study will provide new ideas for developing low-cost
low-energy and environmentally friendly CO
2
capture systems.
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