NEW CONTRIBUTIONS TO MODELLING AND SIMULATION OF TAME SYNTHESIS BY CATALYTIC DISTILLATION by A.-.E. Bonet-Ruiz, J. Bonet-Ruiz, G. Bozga, V. Plesu

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Modeling of the Extent of Reaction Curve for the Transesterification Process Between 2-methylpropan-1-ol and Methyl Ethanoate by A. Calvet-Tarragona, J. Bonet, A.E. Bonet-Ruiz, J. Costa Lopez

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Number of Transfer Units Information on Residue Curve Maps. by A.E. Bonet-Ruiz, J. Bonet, G. Bozga, J. Llorens Llacuna, V. Plesu

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Minimum Gas/Liquid Flow Rate for Absorption Columns by M. Sala, J. Bonet, V. Plesu, A.E. Bonet Ruiz, P. Iancu, J. Llorens

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Minimum Solvent Flow Rate for Counter-Current Liquid-Liquid Extraction Columns by J. Bonet, V. Plesu, A.E. Bonet Ruiz, A. Tuluc, J. Llorens, P. Iancu

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Isobaric Vapour Liquid Equilibrium at 101.3 kPa for the Binary Mixtures 2-Methyl-2-Butene / Methanol and Isopentane / Methanol by M. Bernabeu Diaz, V. Plesu, J. Bonet Ruiz, A.E. Bonet Ruiz, J. Llorens Llacuna

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A Non-dimensional Simplified Cost Function for Distillation Systems Evaluation. by J. Bonet, A.E. Bonet-Ruiz, C.V. Radu, J. Llorens Llacuna, J. Costa Lopez

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Isobaric Vapor Liquid Equilibrium at 101.3 kPa for the Binary Mixtures 2-Methyl-2-Butene / TAME and 2-Methyl-1- Butene / TAME by M. Bernabeu Diaz, V. Plesu, J. Bonet Ruiz, A.E. Bonet Ruiz, J. Llorens Llacuna

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Simulation and Process Integration of Clean Acetone Plant by M.C. Tohaneanu, V. Plesu, P. Iancu, G. Bumbac, A.E. Bonet Ruiz, J. Bonet Ruiz

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Simulation of a Continuous Process for Biodiesel Synthesis from Triacylglycerol Based on Reactive Distillation by J. Bonet, A.E. Bonet-Ruiz, J. Lorens Llacuna, V. Plesu, M.T. Bercaru, R.E. Bozga

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