Functionalized ZIF-7/Pebax® 2533 mixed matrix membranes for CO2/N2 separation

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  • Ningbo University
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OriginalspracheEnglisch
Aufsatznummer110030
FachzeitschriftMicroporous and Mesoporous Materials
Jahrgang297
Frühes Online-Datum16 Jan. 2020
PublikationsstatusVeröffentlicht - 1 Mai 2020

Abstract

Membrane-based separation technology has evolved as a competitive approach for CO2 capture from flue gas (mainly N2). To achieve high separation performance, three partially NH2-, OH- and CH3OH- functionalized mixed-linker-ZIF-7 were successfully synthesized, and incorporated into polyether-block-amide (Pebax® 2533) polymer to form mixed-matrix membranes (MMMs). As evidenced by the CO2 adsorption isotherms, introducing functional groups in the ZIF-7 framework was indeed beneficial for CO2 adsorption. All MMMs composed of ZIF-7-NH2, ZIF-7-OH and ZIF-7-CH3OH offered better CO2/N2 separation performance than the parent ZIF-7-Pebax® 2533 membrane, suggesting the positive effect of functionalized ZIF-7 fillers on the gas separation performance. Among the three functionalized ZIF-7 based MMMs, the ZIF-7-OH-Pebax MMMs exhibited the best performance for CO2/N2 separation, which might be ascribed to the highest adsorption selectivity of CO2 over N2 predicted by ideal adsorbed solution theory (IAST) for ZIF-7-OH fillers. The 14% ZIF-7-OH-Pebax MMM showed high CO2 permeability of 273 Barrer and CO2/N2 separation factor of 38, which increased by 60% and 145% as compared with the neat Pebax membrane. The strategy of preparing functionalized MOFs with strong affinity for CO2 provides an effective method to develop MMMs for highly efficient CO2 separation.

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Functionalized ZIF-7/Pebax® 2533 mixed matrix membranes for CO2/N2 separation. / Gao, Jie; Mao, Haizhuo; Jin, Hua et al.
in: Microporous and Mesoporous Materials, Jahrgang 297, 110030, 01.05.2020.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Gao J, Mao H, Jin H, Chen C, Feldhoff A, Li Y. Functionalized ZIF-7/Pebax® 2533 mixed matrix membranes for CO2/N2 separation. Microporous and Mesoporous Materials. 2020 Mai 1;297:110030. Epub 2020 Jan 16. doi: 10.1016/j.micromeso.2020.110030
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title = "Functionalized ZIF-7/Pebax{\textregistered} 2533 mixed matrix membranes for CO2/N2 separation",
abstract = "Membrane-based separation technology has evolved as a competitive approach for CO2 capture from flue gas (mainly N2). To achieve high separation performance, three partially NH2-, OH- and CH3OH- functionalized mixed-linker-ZIF-7 were successfully synthesized, and incorporated into polyether-block-amide (Pebax{\textregistered} 2533) polymer to form mixed-matrix membranes (MMMs). As evidenced by the CO2 adsorption isotherms, introducing functional groups in the ZIF-7 framework was indeed beneficial for CO2 adsorption. All MMMs composed of ZIF-7-NH2, ZIF-7-OH and ZIF-7-CH3OH offered better CO2/N2 separation performance than the parent ZIF-7-Pebax{\textregistered} 2533 membrane, suggesting the positive effect of functionalized ZIF-7 fillers on the gas separation performance. Among the three functionalized ZIF-7 based MMMs, the ZIF-7-OH-Pebax MMMs exhibited the best performance for CO2/N2 separation, which might be ascribed to the highest adsorption selectivity of CO2 over N2 predicted by ideal adsorbed solution theory (IAST) for ZIF-7-OH fillers. The 14% ZIF-7-OH-Pebax MMM showed high CO2 permeability of 273 Barrer and CO2/N2 separation factor of 38, which increased by 60% and 145% as compared with the neat Pebax membrane. The strategy of preparing functionalized MOFs with strong affinity for CO2 provides an effective method to develop MMMs for highly efficient CO2 separation.",
keywords = "CO separation, Functionalized ZIF-7, Metal-organic framework, Mixed-matrix membranes, Pebax",
author = "Jie Gao and Haizhuo Mao and Hua Jin and Chen Chen and Armin Feldhoff and Yanshuo Li",
note = "Funding Information: This work was supported by the National Natural Science Foundation of China ( 21808113 , 21622607 , 21761132009 ), National Natural Science Foundation of Zhejiang (no. LR18B060002 ) and the K. C. Wong Magna Fund in Ningbo University. Gratefully acknowledged is funding by the Deutsche Forschungsgemeinschaft (DFG, German Research Foundation) - FE928/15-1 . ",
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doi = "10.1016/j.micromeso.2020.110030",
language = "English",
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journal = "Microporous and Mesoporous Materials",
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Download

TY - JOUR

T1 - Functionalized ZIF-7/Pebax® 2533 mixed matrix membranes for CO2/N2 separation

AU - Gao, Jie

AU - Mao, Haizhuo

AU - Jin, Hua

AU - Chen, Chen

AU - Feldhoff, Armin

AU - Li, Yanshuo

N1 - Funding Information: This work was supported by the National Natural Science Foundation of China ( 21808113 , 21622607 , 21761132009 ), National Natural Science Foundation of Zhejiang (no. LR18B060002 ) and the K. C. Wong Magna Fund in Ningbo University. Gratefully acknowledged is funding by the Deutsche Forschungsgemeinschaft (DFG, German Research Foundation) - FE928/15-1 .

PY - 2020/5/1

Y1 - 2020/5/1

N2 - Membrane-based separation technology has evolved as a competitive approach for CO2 capture from flue gas (mainly N2). To achieve high separation performance, three partially NH2-, OH- and CH3OH- functionalized mixed-linker-ZIF-7 were successfully synthesized, and incorporated into polyether-block-amide (Pebax® 2533) polymer to form mixed-matrix membranes (MMMs). As evidenced by the CO2 adsorption isotherms, introducing functional groups in the ZIF-7 framework was indeed beneficial for CO2 adsorption. All MMMs composed of ZIF-7-NH2, ZIF-7-OH and ZIF-7-CH3OH offered better CO2/N2 separation performance than the parent ZIF-7-Pebax® 2533 membrane, suggesting the positive effect of functionalized ZIF-7 fillers on the gas separation performance. Among the three functionalized ZIF-7 based MMMs, the ZIF-7-OH-Pebax MMMs exhibited the best performance for CO2/N2 separation, which might be ascribed to the highest adsorption selectivity of CO2 over N2 predicted by ideal adsorbed solution theory (IAST) for ZIF-7-OH fillers. The 14% ZIF-7-OH-Pebax MMM showed high CO2 permeability of 273 Barrer and CO2/N2 separation factor of 38, which increased by 60% and 145% as compared with the neat Pebax membrane. The strategy of preparing functionalized MOFs with strong affinity for CO2 provides an effective method to develop MMMs for highly efficient CO2 separation.

AB - Membrane-based separation technology has evolved as a competitive approach for CO2 capture from flue gas (mainly N2). To achieve high separation performance, three partially NH2-, OH- and CH3OH- functionalized mixed-linker-ZIF-7 were successfully synthesized, and incorporated into polyether-block-amide (Pebax® 2533) polymer to form mixed-matrix membranes (MMMs). As evidenced by the CO2 adsorption isotherms, introducing functional groups in the ZIF-7 framework was indeed beneficial for CO2 adsorption. All MMMs composed of ZIF-7-NH2, ZIF-7-OH and ZIF-7-CH3OH offered better CO2/N2 separation performance than the parent ZIF-7-Pebax® 2533 membrane, suggesting the positive effect of functionalized ZIF-7 fillers on the gas separation performance. Among the three functionalized ZIF-7 based MMMs, the ZIF-7-OH-Pebax MMMs exhibited the best performance for CO2/N2 separation, which might be ascribed to the highest adsorption selectivity of CO2 over N2 predicted by ideal adsorbed solution theory (IAST) for ZIF-7-OH fillers. The 14% ZIF-7-OH-Pebax MMM showed high CO2 permeability of 273 Barrer and CO2/N2 separation factor of 38, which increased by 60% and 145% as compared with the neat Pebax membrane. The strategy of preparing functionalized MOFs with strong affinity for CO2 provides an effective method to develop MMMs for highly efficient CO2 separation.

KW - CO separation

KW - Functionalized ZIF-7

KW - Metal-organic framework

KW - Mixed-matrix membranes

KW - Pebax

UR - http://www.scopus.com/inward/record.url?scp=85078682358&partnerID=8YFLogxK

U2 - 10.1016/j.micromeso.2020.110030

DO - 10.1016/j.micromeso.2020.110030

M3 - Article

AN - SCOPUS:85078682358

VL - 297

JO - Microporous and Mesoporous Materials

JF - Microporous and Mesoporous Materials

SN - 1387-1811

M1 - 110030

ER -

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