Polymeric hollow fiber supported ionic liquid membranes were fabricated utilizing Matrimid (R) and 1-hexyl-3-methylimidalzolium bis(trifluoromethylsulfonyl)imide ([hmim][Tf2N]) as the selected polymeric and ionic liquid materials, respectively. The fibers were spun via a dry-wet nonsolvent-induced phase separation procedure, employing a single layer spinneret extrusion system. Four different types of membranes were fabricated using four morphologically different hollow fiber supports. These membranes take advantage of the fiber morphology combined with a supported ionic liquid to enable more efficient mass transfer than flat membranes. Initially the membranes had a low separation performance for CO2/H-2; however, upon changing the porosity and support morphology, better permeance and selectivity were achieved. Transport properties of CO2 and H-2 are reported for hollow fiber membranes containing an ionic liquid in the temperature range from 37 to 150 degrees C. The glass transition temperature, Youngs modulus, and tensile strength are also reported. The volume fractions of polymer, macro-voids, and micro-voids were determined using a combination of density measurements and an SEM image analysis technique. These quantities were then used to calculate both the bulk fiber porosity and the porosity of the micro-porous region. The surface porosity was also estimated by image analysis. It was observed that the transport and mechanical properties of the fiber were influenced by porosity. (C) 2013 Elsevier B.V. All rights reserved.