High performance compatible thiazole-based polymeric blend cellulose acetate membrane as selective CO2 absorbent and molecular sieve

Akbarzadeh E., Shockravi A., Vatanpour Sargheın V.

CARBOHYDRATE POLYMERS, cilt.252, 2021 (SCI-Expanded) identifier identifier identifier

  • Yayın Türü: Makale / Tam Makale
  • Cilt numarası: 252
  • Basım Tarihi: 2021
  • Doi Numarası: 10.1016/j.carbpol.2020.117215
  • Dergi Adı: CARBOHYDRATE POLYMERS
  • Derginin Tarandığı İndeksler: Science Citation Index Expanded (SCI-EXPANDED), Scopus, Academic Search Premier, PASCAL, BIOSIS, Biotechnology Research Abstracts, CAB Abstracts, Chemical Abstracts Core, EMBASE, Food Science & Technology Abstracts, MEDLINE, Veterinary Science Database
  • Anahtar Kelimeler: Cellulose acetate (CA), Polymeric blend membrane, Gas separation, Permeation, Thiazole, CO2 capture, GAS PERMEATION PROPERTIES, MIXED MATRIX MEMBRANE, CARBON-DIOXIDE, NATURAL-GAS, PROCESS INTENSIFICATION, SEPARATION PERFORMANCE, HYDROGEN PURIFICATION, METAL-IONS, FLUE-GAS, CO2/N-2
  • İstanbul Teknik Üniversitesi Adresli: Hayır

Özet

Green blend membranes comprise of high thermal resistance ortho-linked thiazole-based polyimine (PM-4) including thioether linkage were fabricated in combination of glassy cellulose acetate (CA). The thermal stabilities of PMs were examined using thermogravimetric analysis (TGA) and differential scanning calorimetry (DSC). Morphological aspects and functional groups of the membranes were investigated via field emission scanning electron microscopy (FESEM) and Fourier transform infrared spectroscopy-attenuated total reflectance (FTIR-ATR) analysis respectively. X-ray diffraction (XRD) and mechanical strength were determined as well. The effects of polyimine content, pressure and temperature were studied on CO2 permeability (P) and selectivity. The pressure changes revealed exponentially increases on CO2 permeability by plasticization, facilitated transfer and solution-diffusion mechanisms, but decreases on CH4 and N-2 permeations. Remarkable permeation (P = 3000 Barrer) of CA/PM-4 (1:3 % w/w) and ideal selectivity ratios of CO2/N-2 = 59, CO2/CH4 = 33.7 were obtained at 3 bar and 35 degrees C versus neat CA membrane.