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Google Scholar Separation of methanol—n-butyl acetate mixtures by pervaporation: Potential of 10 commercial membranes. Vapor-Liquid Equilibrium Data Collection.

Frankfurt: Dechema,1 1 — Akita K, Yoshida F. Phase-equilibria in methanol-ethyl acetate-water system.

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Vapor—Liquid equilibrium of binary mixtures containing isopropyl acetate and alkanols at Evaluation of the accuracy of modelling the separation of highly non-ideal mixtures: Extractive heterogeneous-azeotropic distillation. Andre A.

Carbohydrate-based immune adjuvants

Isobutanol-water separation with heterogeneous-azeotropic distillation. Dissertation for the Master Degree.

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Modelling of pervaporation: Parameter estimation and model development. Pervaporation membrane separation processes.

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One-dimensional modeling of pervaporation systems using a semiempirical flux model. Koch K, Gorak A. Pervaporation of binary and ternary mixtures of acetone, isopropyl alcohol and water using polymeric membranes: Experimental characterisation and modelling.

megszabadítsa a testet az összes parazitától

New horizon for the membrane separation: Combination of organophilic and hydrophilic pervaporations. Toth A J.

Orvos válaszol

Liquid waste treatment with physicochemical tools for environmental protection. Dissertation for the Doctoral Degree.

A lack of animal studies or trials comparing multiple adjuvants with the same antigens is often noted as an impediment to adjuvant selection. However, even if they were available, extensive head-to-head comparisons of adjuvants in animals could be extremely misleading as many adjuvant effects including potency vary from species to species and thus comparisons of adjuvant potency performed, for example, in mice are often not predictive of relative adjuvant potency in humans.

Rigorous modelling and optimization of hybrid separation processes based on pervaporation. Use of pervaporation systems in the chemical industry. Energy-efficient separation process and control scheme for extractive distillation of ethanol-water using deep eutectic solvent.

Laboratóriumi vizsgálatok

Improving the performance of heat pump-assisted azeotropic dividing wall distillation. Energy-efficient extractive distillation process by combining preconcentration column and entrainer recovery column.

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Insight into pressure-swing distillation from azeotropic phenomenon to dynamic control. Design, optimization and control of extractive distillation for the separation of isopropanol-water papilloma th c qu n ionic liquids. Investigation about energy saving for synthesis of isobutyl acetate in the reactive dividing-wall column.

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Energy-saving thermally coupled ternary extractive distillation process by combining with mixed entrainer for separating ternary mixture containing bioethanol. Energy,—