Mahendra Kumar
King Abdullah University of Science and Technology
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Publication
Featured researches published by Mahendra Kumar.
Journal of Materials Chemistry | 2017
Madhavan Karunakaran; Luis Francisco Villalobos; Mahendra Kumar; Rahul Shevate; Faheem Hassan Akhtar; Klaus-Viktor Peinemann
Advanced membrane systems with high flux and sufficient selectivity are required for industrial gas separation processes. In order to achieve high flux and high selectivity, the membrane material should be as thin as possible and it should have selective sieving channels and long term stability. This could be achieved by designing a three component material consisting of a blend of an ionic liquid and graphene oxide covered by a highly permeable low selective polymeric coating. By using a simple dip coating technique, we prepared high flux and CO2 selective ultrathin graphene oxide (GO)/ionic liquid membranes on a porous ultrafiltration support. The ultrathin composite membranes derived from GO/ionic liquid complex displays remarkable combinations of permeability (CO2 flux: 37 GPU) and selectivity (CO2/N2 selectivity: 130) that surpass the upper bound of ionic liquid membranes for CO2/N2 separation. Moreover, the membranes were stable when tested for 120 hours.
Journal of Materials Chemistry | 2017
Faheem Hassan Akhtar; Mahendra Kumar; Luis Francisco Villalobos; H. Vovusha; Rahul Shevate; Udo Schwingenschlögl; Klaus-Viktor Peinemann
Polybenzimidazole (PBI), a thermally and chemically stable polymer, is commonly used to fabricate membranes for applications like hydrogen recovery at temperatures of more than 300 °C, fuel cells working in a highly acidic environment, and nanofiltration in aggressive solvents. This report shows for the first time the use of PBI dense membranes for water vapor/gas separation applications. They showed an excellent selectivity and high water vapor permeability. The incorporation of inorganic hydrophilic titanium-based nano-fillers into the PBI matrix further increased the water vapor permeability and water vapor/N2 selectivity. The most selective mixed matrix membrane with 0.5 wt% loading of TiO2 nanotubes yielded a water vapor permeability of 6.8 × 104 barrer and a H2O/N2 selectivity of 3.9 × 106. The most permeable membrane with 1 wt% loading of carboxylated TiO2 nanoparticles had a water vapor permeability of 7.1 × 104 barrer and a H2O/N2 selectivity of 3.1 × 106. The performance of these membranes in terms of water vapor transport and selectivity is among the highest reported ones. The remarkable ability of PBI to efficiently permeate water versus other gases opens the possibility to fabricate membranes for the dehumidification of streams in harsh environments. This includes the removal of water from high temperature reaction mixtures to shift the equilibrium towards products.
Polymers | 2017
Madhavan Karunakaran; Mahendra Kumar; Rahul Shevate; Faheem Hassan Akhtar; Klaus-Viktor Peinemann
In this work, we report the successful fabrication of CO2-philic polymer composite membranes using a polyacrylonitrile-r-poly(ethylene glycol) methyl ether methacrylate (PAN-r-PEGMA) copolymer. The series of PAN-r-PEGMA copolymers with various amounts of PEG content was synthesized by free radical polymerization in presence of AIBN initiator and the obtained copolymers were used for the fabrication of composite membranes. The synthesized copolymers show high molecular weights in the range of 44–56 kDa. We were able to fabricate thin film composite (TFC) membranes by dip coating procedure using PAN-r-PEGMA copolymers and the porous PAN support membrane. Scanning electron microscopy (SEM) and atomic force microscopy (AFM) were applied to analyze the surface morphology of the composite membranes. The microscopy analysis reveals the formation of the defect free skin selective layer of PAN-r-PEGMA copolymer over the porous PAN support membrane. Selective layer thickness of the composite membranes was in the range of 1.32–1.42 μm. The resulting composite membrane has CO2 a permeance of 1.37 × 10−1 m3/m2·h·bar and an ideal CO2/N2, selectivity of 65. The TFC membranes showed increasing ideal gas pair selectivities in the order CO2/N2 > CO2/CH4 > CO2/H2. In addition, the fabricated composite membranes were tested for long-term single gas permeation measurement and these membranes have remarkable stability, proving that they are good candidates for CO2 separation.
Chemical Communications | 2015
Madhavan Karunakaran; Rahul Shevate; Mahendra Kumar; Klaus-Viktor Peinemann
Journal of Membrane Science | 2017
Faheem Hassan Akhtar; Mahendra Kumar; Klaus-Viktor Peinemann
Journal of Membrane Science | 2017
Rahul Shevate; Mahendra Kumar; Madhavan Karunakaran; Mohamed N. Hedhili; Klaus-Viktor Peinemann
Chemical Engineering Journal | 2016
Mahendra Kumar; Rahul Shevate; Roland Hilke; Klaus-Viktor Peinemann
Journal of Membrane Science | 2016
Rahul Shevate; Madhavan Karunakaran; Mahendra Kumar; Klaus-Viktor Peinemann
Journal of Materials Chemistry | 2018
Rahul Shevate; Mahendra Kumar; Madhavan Karunakaran; Christian Canlas; Klaus-Viktor Peinemann
Archive | 2017
Faheem Hassan Akhtar; Mahendra Kumar; Klaus-Viktor Peinemann