Novel Cellulose Triacetate (CTA)/Cellulose Diacetate (CDA) Blend Membranes Enhanced by Amine Functionalized ZIF-8 for CO<sub>2</sub> Separation

Currently, cellulose acetate (CA) membranes dominate membrane-based CO<sub>2</sub> separation for natural gas purification due to their economical and green nature. However, their lower CO<sub>2</sub> permeability and ease of plasticization are the drawbacks. To overcome thes...

Full description

Bibliographic Details
Main Authors: Ayesha Raza, Susilo Japip, Can Zeng Liang, Sarah Farrukh, Arshad Hussain, Tai-Shung Chung
Format: Article
Language:English
Published: MDPI AG 2021-08-01
Series:Polymers
Subjects:
Online Access:https://www.mdpi.com/2073-4360/13/17/2946
id doaj-0f2b51615c114ac7b05998a422810865
record_format Article
spelling doaj-0f2b51615c114ac7b05998a4228108652021-09-09T13:54:28ZengMDPI AGPolymers2073-43602021-08-01132946294610.3390/polym13172946Novel Cellulose Triacetate (CTA)/Cellulose Diacetate (CDA) Blend Membranes Enhanced by Amine Functionalized ZIF-8 for CO<sub>2</sub> SeparationAyesha Raza0Susilo Japip1Can Zeng Liang2Sarah Farrukh3Arshad Hussain4Tai-Shung Chung5Department of Chemical and Biomolecular Engineering, National University of Singapore, Singapore 117585, SingaporeDepartment of Chemical and Biomolecular Engineering, National University of Singapore, Singapore 117585, SingaporeDepartment of Chemical and Biomolecular Engineering, National University of Singapore, Singapore 117585, SingaporeDepartment of Chemical and Materials Engineering, National University of Sciences and Technology, Islamabad 44000, PakistanDepartment of Chemical and Energy Engineering, Pak-Austria University, Haripur 22621, PakistanDepartment of Chemical and Biomolecular Engineering, National University of Singapore, Singapore 117585, SingaporeCurrently, cellulose acetate (CA) membranes dominate membrane-based CO<sub>2</sub> separation for natural gas purification due to their economical and green nature. However, their lower CO<sub>2</sub> permeability and ease of plasticization are the drawbacks. To overcome these weaknesses, we have developed high-performance mixed matrix membranes (MMMs) consisting of cellulose triacetate (CTA), cellulose diacetate (CDA), and amine functionalized zeolitic imidazolate frameworks (NH<sub>2</sub>-ZIF-8) for CO<sub>2</sub> separation. The NH<sub>2</sub>-ZIF-8 was chosen as a filler because (1) its pore size is between the kinetic diameters of CO<sub>2</sub> and CH<sub>4</sub> and (2) the NH<sub>2</sub> groups attached on the surface of NH<sub>2</sub>-ZIF-8 have good affinity with CO<sub>2</sub> molecules. The incorporation of NH<sub>2</sub>-ZIF-8 in the CTA/CDA blend matrix improved both the gas separation performance and plasticization resistance. The optimized membrane containing 15 wt.% of NH<sub>2</sub>-ZIF-8 had a CO<sub>2</sub> permeability of 11.33 Barrer at 35 °C under the trans-membrane pressure of 5 bar. This is 2-fold higher than the pristine membrane, while showing a superior CO<sub>2</sub>/CH<sub>4</sub> selectivity of 33. In addition, the former had 106% higher CO<sub>2</sub> plasticization resistance of up to about 21 bar and an impressive mixed gas CO<sub>2</sub>/CH<sub>4</sub> selectivity of about 40. Therefore, the newly fabricated MMMs based on the CTA/CDA blend may have great potential for CO<sub>2</sub> separation in the natural gas industry.https://www.mdpi.com/2073-4360/13/17/2946zeolitic imidazolate frameworkspolymer blendmixed matrix membraneplasticization resistanceCO<sub>2</sub> separation
collection DOAJ
language English
format Article
sources DOAJ
author Ayesha Raza
Susilo Japip
Can Zeng Liang
Sarah Farrukh
Arshad Hussain
Tai-Shung Chung
spellingShingle Ayesha Raza
Susilo Japip
Can Zeng Liang
Sarah Farrukh
Arshad Hussain
Tai-Shung Chung
Novel Cellulose Triacetate (CTA)/Cellulose Diacetate (CDA) Blend Membranes Enhanced by Amine Functionalized ZIF-8 for CO<sub>2</sub> Separation
Polymers
zeolitic imidazolate frameworks
polymer blend
mixed matrix membrane
plasticization resistance
CO<sub>2</sub> separation
author_facet Ayesha Raza
Susilo Japip
Can Zeng Liang
Sarah Farrukh
Arshad Hussain
Tai-Shung Chung
author_sort Ayesha Raza
title Novel Cellulose Triacetate (CTA)/Cellulose Diacetate (CDA) Blend Membranes Enhanced by Amine Functionalized ZIF-8 for CO<sub>2</sub> Separation
title_short Novel Cellulose Triacetate (CTA)/Cellulose Diacetate (CDA) Blend Membranes Enhanced by Amine Functionalized ZIF-8 for CO<sub>2</sub> Separation
title_full Novel Cellulose Triacetate (CTA)/Cellulose Diacetate (CDA) Blend Membranes Enhanced by Amine Functionalized ZIF-8 for CO<sub>2</sub> Separation
title_fullStr Novel Cellulose Triacetate (CTA)/Cellulose Diacetate (CDA) Blend Membranes Enhanced by Amine Functionalized ZIF-8 for CO<sub>2</sub> Separation
title_full_unstemmed Novel Cellulose Triacetate (CTA)/Cellulose Diacetate (CDA) Blend Membranes Enhanced by Amine Functionalized ZIF-8 for CO<sub>2</sub> Separation
title_sort novel cellulose triacetate (cta)/cellulose diacetate (cda) blend membranes enhanced by amine functionalized zif-8 for co<sub>2</sub> separation
publisher MDPI AG
series Polymers
issn 2073-4360
publishDate 2021-08-01
description Currently, cellulose acetate (CA) membranes dominate membrane-based CO<sub>2</sub> separation for natural gas purification due to their economical and green nature. However, their lower CO<sub>2</sub> permeability and ease of plasticization are the drawbacks. To overcome these weaknesses, we have developed high-performance mixed matrix membranes (MMMs) consisting of cellulose triacetate (CTA), cellulose diacetate (CDA), and amine functionalized zeolitic imidazolate frameworks (NH<sub>2</sub>-ZIF-8) for CO<sub>2</sub> separation. The NH<sub>2</sub>-ZIF-8 was chosen as a filler because (1) its pore size is between the kinetic diameters of CO<sub>2</sub> and CH<sub>4</sub> and (2) the NH<sub>2</sub> groups attached on the surface of NH<sub>2</sub>-ZIF-8 have good affinity with CO<sub>2</sub> molecules. The incorporation of NH<sub>2</sub>-ZIF-8 in the CTA/CDA blend matrix improved both the gas separation performance and plasticization resistance. The optimized membrane containing 15 wt.% of NH<sub>2</sub>-ZIF-8 had a CO<sub>2</sub> permeability of 11.33 Barrer at 35 °C under the trans-membrane pressure of 5 bar. This is 2-fold higher than the pristine membrane, while showing a superior CO<sub>2</sub>/CH<sub>4</sub> selectivity of 33. In addition, the former had 106% higher CO<sub>2</sub> plasticization resistance of up to about 21 bar and an impressive mixed gas CO<sub>2</sub>/CH<sub>4</sub> selectivity of about 40. Therefore, the newly fabricated MMMs based on the CTA/CDA blend may have great potential for CO<sub>2</sub> separation in the natural gas industry.
topic zeolitic imidazolate frameworks
polymer blend
mixed matrix membrane
plasticization resistance
CO<sub>2</sub> separation
url https://www.mdpi.com/2073-4360/13/17/2946
work_keys_str_mv AT ayesharaza novelcellulosetriacetatectacellulosediacetatecdablendmembranesenhancedbyaminefunctionalizedzif8forcosub2subseparation
AT susilojapip novelcellulosetriacetatectacellulosediacetatecdablendmembranesenhancedbyaminefunctionalizedzif8forcosub2subseparation
AT canzengliang novelcellulosetriacetatectacellulosediacetatecdablendmembranesenhancedbyaminefunctionalizedzif8forcosub2subseparation
AT sarahfarrukh novelcellulosetriacetatectacellulosediacetatecdablendmembranesenhancedbyaminefunctionalizedzif8forcosub2subseparation
AT arshadhussain novelcellulosetriacetatectacellulosediacetatecdablendmembranesenhancedbyaminefunctionalizedzif8forcosub2subseparation
AT taishungchung novelcellulosetriacetatectacellulosediacetatecdablendmembranesenhancedbyaminefunctionalizedzif8forcosub2subseparation
_version_ 1717759559976615936