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Rahimpour, M. R., Fathikalajahi, J., Moghtaderi, Behdad, Farahani, A. N.. John Wiley & Sons; 2005. A grade transition strategy for the prevention of melting and agglomeration of particles in an ethylene polymerization reactor.
Rezaie, N., Jahanmiri, A., Moghtaderi, Behdad, Rahimpour, M. R.. Elsevier; 2005. A comparison of homogeneous and heterogeneous dynamic models for industrial methanol reactors in the presence of catalyst deactivation.
Rahimpour, M. R., Mirvakili, A., Paymooni, K., Moghtaderi, B.. Elsevier; 2011. A comparative study between a fluidized-bed and a fixed-bed water perm-selective membrane reactor with in situ H<sub>₂</sub>O removal for Fischer-Tropsch synthesis of GTL technology.
Bayat, M., Rahimpour, M. R., Moghtaderi, B.. Elsevier; 2011. Genetic algorithm strategy (GA) for optimization of a novel dual-stage slurry bubble column membrane configuration for Fischer-Tropsch synthesis in gas to liquid (GTL) technology.
Iranshahi, D., Pourazadi, E., Paymooni, K., Rahimpour, M. R., Jahanmiri, A., Moghtaderi, B.. Elsevier; 2011. A dynamic membrane reactor concept for naphtha reforming, considering radial-flow patterns for both sweeping gas and reacting materials.
Mirvakili, A., Rostami, M., Paymooni, K., Rahimpour, M. R., Moghtaderi, B.. Elsevier; 2012. Hydrogen looping approach in optimized methanol thermally coupled membrane reactor.
Rahimpour, M. R., Moghtaderi, Behdad, Jahanmiri, A., Rezaie, N.. John Wiley & Sons; 2005. Operability of an industrial methanol synthesis reactor with mixtures of fresh and partially deactivated catalyst.