This paper compares separation efficiency and operational stability in the distillation process of two pairs of light hydrocarbon mixtures (iso-/n-butane and propylene/propane) using a distillation column made of micro-porous hollow fibers. The hollow fibers used in the column are non-selective and wetable by the process fluid In the column with a 36 5 cm length, more than 25% enrichment of iso-butane is obtained from a iso-/n-butane (55/45%) mixture while similar to 8% enrichment of propylene is obtained from a propylene/propane (65/35%) mixture Because of a slightly larger relative volatility of iso-/n-butane than that of propane/propylene, a wider and a more stable operational range is obtained for the former pair The pressure drop of the hollow fiber packings on both vapor and liquid sides is also discussed. Within the loading range (F-factor <2.0 Pa(0 5)), a pressure drop of less than 10 mbar/m is obtained in vapor phase for these two pairs of mixtures Mass transfer coefficients of >0 15 and 004 cm/s are obtained for iso-/n-butane and propylene/propane, respectively, even though the membrane layer contributes an additional mass transfer resistance to the overall mass transfer process Furthermore, without effectively separating individual fibers, a high packing density may result in a severe channeling problem and thus decrease the separation efficiency (C) 2010 Elsevier B.V All rights reserved.