Permselectivity improvement of PEBAX ® 2533 membrane by addition of glassy polymers (Matrimid® and polystyrene) for CO 2 / N 2 separation

Statistical analysis of CO2/N2 gas separation permeance and selectivity using taguchi method

The separation of CO2 from flue gases presents a crucial challenge that needs to be addressed. However, membrane processes offer a promising alternative solution. Polysulfone (PSF)membranes were prepared using N-methyl-2-pyrrolidone (NMP) and tetrahydrofuran (THF) using a dry-wet phase inversion technique. The membranes were fabricated with the selection of casting parameters, PSF concentration (20-30 wt%), solvent ratio of THF/NMP (0/100-35/65), and evaporation time (0-4 min). In this work, the interaction between these influencing factors during preparation and membrane performance was studied. Scanning electron microscopy (SEM) was used to characterize the membranes for morphological investigation. Taguchi statistical analysis was employed in the Minitab-19 software used for the design of the experiments in this study, and the responses of the CO2 permeance and CO2/N2 separation factor were analyzed and optimized based on the casting parameters. The results showed the CO2 permeance of the membranes was determined between 1.25 ± 0.04 and 8.47 ± 0.51GPU and selectivity was between 2.95 and 8.92. The statistical analysis indicated that casting conditions affect membrane performance in the following order: PSF concentration > solvent ratio > evaporation time. The optimum parameters for casting solution were the PSF concentration of 20 wt%, THF/NMP ratio of 17.5/82.5, and evaporation time of 4 min. The selected method also reinforces the connection between membrane casting parameters and the observed outcomes in terms of permeation and morphology.

Analysis of the Influence of Process Parameters on the Properties of Homogeneous and Heterogeneous Membranes for Gas Separation

Heterogeneous membranes, otherwise known as Mixed Matrix Membranes (MMMs), which are used in gas separation processes, are the subject of growing interest. This is due to their potential to improve the process properties of membranes compared to those of homogeneous membranes, i.e., those made of polymer only. Using such membranes in a process involves subjecting them to varying temperatures and pressures. This paper investigates the effects of temperature and feed pressure on the process properties of homogeneous and heterogeneous membranes. Membranes made of Pebax^®2533 copolymer and containing additional fillers such as SiO₂, ZIF-8, and POSS-Ph were investigated. Tests were performed over a temperature range of 25-55 °C and a pressure range of 2-8 bar for N₂, CH₄, and CO₂ gases. It was found that temperature positively influences the increase in permeability, while pressure influences permeability depending on the gas used, which is related to the effect of pressure on the solubility of the gas in the membrane.