Abstract
The characteristics of air separation in a hollow-fiber membrane unit are investigated numerically aiming at generation of highly oxygen-enriched air for clean combustion applications. A 2D axisymmetric mesh was generated using Gambit software and, then, was fed to Fluent 12.1 code. Detailed numerical study is presented for air separation using different polymers. Effects of sweep gas flow rate (from zero flow up to 1.15 × 10−7 kg/s), feed gas flow rate (from 3.3 × 10−9 kg/s up to 5.89 × 10−8 kg/s), fed pressure (from 2 atm up to 10 atm) and membrane polymeric material (considering TR-PBO-co-PPL-28 and TR-PI-g-CD) on permeation fluxes and concentrations of O2 and N2 are investigated. Targeting higher exit O2 concentrations, multi-stage air separation unit is developed. The developed unit consists of three stages and the achieved oxygen mass fraction at outlet of first, second and third stages are 0.517, 0.8 and 0.914. Higher stage cut ratio is gained in the third stage as compared to first and second stages.
•Characteristics of air separation in hollow-fiber polymeric membrane are studied.•Highly oxygenated air is obtained using polymers for clean combustion applications.•Detailed numerical study is presented for air separation using different polymers.•Effects of feed and sweep flows and pressure on permeation fluxes are investigated.•Targeting higher exit O2 concentrations, multi-stage air separation unit is developed.