Articles
  • Graphene oxide-nanocellulose-cellulose acetate mixed matrix membrane as an efficient separator for carbon dioxide from natural gas
  • Mingyue Wanga,b,c, Qiang Weia,*, Dong Lib and Changwei Pangc

  • aChina University of Petroleum-Beijing at Karamay, Engineering College, Karamay, Xinjiang 834000, China
    bApplied Technology Research Institute of Northeast Petroleum University, Daqing, Heilongjiang 163318, China
    cChina University of Petroleum, Russia central Asia Research Center, Beijing 102249, China

  • This article is an open access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/by-nc/4.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.

Abstract

Removing carbon dioxide (CO₂) from natural gas is essential for improving fuel quality, preventing pipeline corrosion, and enhancing energy efficiency. Membrane technology offers a selective and efficient method for CO₂ removal, ensuring natural gas meets industry standards. This process reduces greenhouse gas emissions, supporting cleaner and more sustainable energy production. In this study, Mixed-matrix membranes (MMMs) incorporating graphene oxide (GO) stabilized by nanocellulose fibers (NCF) within a cellulose acetate (CA) matrix were synthesized and evaluated for CO₂/CH₄ gas separation. The CA/NCF/GO-1 membrane, with 1 wt% GO, demonstrated optimal performance, achieving a CO₂ permeability of 77.8 Barrer and an ideal CO₂/CH₄ selectivity of 24.3. SEM and FT-IR analyses confirmed the uniform dispersion of GO and strong filler-polymer interactions. XRD revealed enhanced crystallinity with GO addition, while TGA indicated thermal stability, with decomposition temperatures ranging from 277 °C to 310 °C. Mechanical testing showed increased tensile strength (up to 60 MPa) with filler addition, though excessive GO (2 wt%) caused aggregation and highly reduced % elongation at break. Gas permeabilities decreased at higher feed pressures (5 bar), aligning with the dual-sorption model. The CA/NCF/GO-1 membrane demonstrated high stability over one week and approached Robeson’s 2008 upper bound, highlighting its potential for industrial CO₂ separation.


Keywords: Mixed matrix membranes, Clean energy, Carbon dioxide separation, Graphene oxide.

This Article

  • 2024; 25(6): 1060-1068

    Published on Dec 31, 2024

  • 10.36410/jcpr.2024.25.6.1060
  • Received on Oct 2, 2024
  • Revised on Dec 14, 2024
  • Accepted on Dec 14, 2024

Correspondence to

  • Qiang Wei
  • China University of Petroleum-Beijing at Karamay, Engineering College, Karamay, Xinjiang 834000, China
    Tel : +86 13261357667 Fax: +86 13261357667

  • E-mail: 15600597779@163.com