Synthesis, characterization, and gas separation performances of polysulfone and cellulose acetate-based mixed matrix membranes

2020 ◽  
Vol 59 (12) ◽  
pp. 1300-1307
Author(s):  
Putu Doddy Sutrisna ◽  
Emma Savitri ◽  
Maria A. Gunawan ◽  
Isra Herdina F. Putri ◽  
Samuel G. B. de Rozari
2021 ◽  
Vol 11 (2) ◽  
pp. 313-330
Author(s):  
Ovaid Mehmood ◽  
Sarah Farrukh ◽  
Arshad Hussain ◽  
Mohammad Younas ◽  
Zarrar Salahuddin ◽  
...  

2021 ◽  
Vol 3 (4) ◽  
pp. 344-350
Author(s):  
Dong Fan ◽  
Aydin Ozcan ◽  
Naseem A. Ramsahye ◽  
Dan Zhao ◽  
Guillaume Maurin ◽  
...  

2021 ◽  
Vol 333 ◽  
pp. 04008
Author(s):  
Yongsheng Liu ◽  
Kyosuke Takata ◽  
Yu Mukai ◽  
Hidetoshi Kita ◽  
Kazuhiro Tanaka

The commercial SAPO-34 zeolite with 0.38 nm pore size and ZIF-8 particles with 0.34 nm aperture size were separately dispersed into different polymer matrix, to prepare the mixed matrix membranes (MMMs) for gas separation. The dispersed situation of the SAPO-34 and ZIF-8 particles in matrix and the influence of the fillers on the separation performance of the membrane had been investigated in this study. The as-synthesized MMMs showed a better trade-off between permeability and selectivity than the pure polymer membrane and the performance could exceed or close to the upper bound line of polymer membrane for CO2 and CH4 separation. The CO2 permeability and CO2/CH4 ideal selectivity of the 6FDA-mDAT MMM containing 40 wt% SAPO-34 zeolite was 190 barrer and ca. 60, respectively. The 6FDA-TrMPD based MMMs containing 20 wt% ZIF-8 provided a permeability of C3H6 and an ideal selectivity of C3H6/C3H8 at 24 barrer and ca. 17, respectively. These separation performances were in a suitable agreement of the theoretical value from Maxwell model.


2021 ◽  
Vol 0 (0) ◽  
Author(s):  
Mehtap Safak Boroglu ◽  
Ismail Boz ◽  
Busra Kaya

Abstract In our study, the synthesis of zeolitic imidazolate framework (ZIF-12) crystals and the preparation of mixed matrix membranes (MMMs) with various ZIF-12 loadings were targeted. The characterization of ZIF-12 and MMMs were carried out by Fourier transform infrared spectroscopy analysis, thermogravimetric analysis, scanning electron microscopy (SEM), and thermomechanical analysis. The performance of MMMs was measured by the ability of binary gas separation. Commercial polyetherimide (PEI-Ultem® 1000) polymer was used as the polymer matrix. The solution casting method was utilized to obtain dense MMMs. In the SEM images of ZIF-12 particles, the particles with a rhombic dodecahedron structure were identified. From SEM images, it was observed that the distribution of ZIF-12 particles in the MMMs was homogeneous and no agglomeration was present. Gas permeability experiments of MMMs were measured for H2, CO2, and CH4 gases at steady state, at 4 bar and 35 °C by constant volume-variable pressure method. PEI/ZIF-12-30 wt% MMM exhibited high permeability and ideal selectivity values for H2/CH4 and CO2/CH4 were P H 2 / CH 4 = 331.41 ${P}_{{\text{H}}_{2}/{\text{CH}}_{4}}=331.41$ and P CO 2 / CH 4 = 53.75 ${P}_{{\text{CO}}_{2}/{\text{CH}}_{4}}=53.75$ gas pair.


2012 ◽  
Vol 35 (5) ◽  
pp. 885-892 ◽  
Author(s):  
H. Karkhanechi ◽  
H. Kazemian ◽  
H. Nazockdast ◽  
M. R. Mozdianfard ◽  
S. M. Bidoki

2019 ◽  
Vol 573 ◽  
pp. 359-369 ◽  
Author(s):  
Yanfang Fan ◽  
Cong Li ◽  
Xiaosa Zhang ◽  
Xiaomei Yang ◽  
Xingyu Su ◽  
...  

2019 ◽  
Author(s):  
Andrew Paul Han ◽  
Frederick F Stewart ◽  
Christopher J Orme

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