共 49 条
Sub-nanometer scale tailoring of the microstructures of composite organosilica membranes for efficient pervaporation of toluene/n-heptane mixtures
被引:11
作者:
Dong, Guanying
[1
]
Zhang, Yatao
[1
]
Pang, Xinchang
[2
]
Guo, Meng
[4
]
Moriyama, Norihiro
[3
]
Nagasawa, Hiroki
[3
]
Kanezashi, Masakoto
[3
]
Tsuru, Toshinori
[3
]
机构:
[1] Zhengzhou Univ, Sch Chem Engn, Zhengzhou 450001, Peoples R China
[2] Zhengzhou Univ, Sch Mat Sci & Engn, Zhengzhou 450001, Peoples R China
[3] Hiroshima Univ, Dept Chem Engn, 1-4-1 Kagamiyama, Higashihiroshima 7398527, Japan
[4] Changzhou Univ, Sch Petrochem Engn, Jiangsu Key Lab Adv Catalyt Mat & Technol, Changzhou 213164, Peoples R China
基金:
中国国家自然科学基金;
关键词:
Organosilica membranes;
Microstructure tailoring;
Pervaporation;
Aromatic/aliphatic hydrocarbons;
Aromatic pi-pi stacking;
HYBRID MEMBRANES;
AROMATIC/ALIPHATIC HYDROCARBONS;
THERMAL-PROPERTIES;
SILICA MEMBRANES;
SEPARATION;
PERMSELECTIVITY;
POLYMERIZATION;
POLYIMIDE;
SIZE;
D O I:
10.1016/j.memsci.2023.121469
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
Amorphous organosilica-based membranes are of enormous potential for pervaporation separation of organic mixtures, however, engineering organosilica membranes with the on-demand pore size and functionality for precise molecular sieving still remains a challenge. Herein, as a proof-of-concept, we proposed a facile and novel co-condensation strategy by pairing the biphenyl-bridged organosilica precursor (BTESBP) with another organosilica precursor (PhTES) equipped with a phenyl pendant group for efficient pervaporation of aromatic/ aliphatic mixtures. It was demonstrated that the strong aromatic pi-pi interactions between BTESBP and PhTES as well as the steric hindrance effect of PhTES allowed the tailoring of membrane pore size at the sub-nano scale, and enhanced the accessibility of biphenyl groups to aromatic hydrocarbons. At the optimal BTESBP/PhTES mass ratio of 98/2, the resulting BTESBP/PhTES composite organosilica membrane achieved superior toluene/nheptane pervaporation separation performance with a total flux surpassing 1 kg m(-2) h(-1) and a separation factor of 8-10 for a 50 wt% toluene/n-heptane feed mixture. Hopefully, this study can stimulate the rethinking of the design principles for composite organosilica membranes and the subsequent development of advanced membranes for energy-efficient pervaporation of organic mixtures.
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页数:11
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