Theoretical description and numerical modelling of dehydration of tert-butanol via reactive distillation at concurrent flow of liquid and vapor phases

Author:

Baiguzin F.A.,Burmistrov D.A.,Kuznetsov V.A.,Farakhov M.I.

Publisher

Elsevier BV

Subject

Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference22 articles.

1. Kinetic study on the dehydration of tert-butyl alcohol catalyzed by ion exchange resins;Abella;Int. J. Chem. Kinet.,1999

2. Baiguzin, F.A., Burmistrov, D.A., Irdinkin, S.A., Rakov, A.V., Filina, M.P., 2015. Method for producing isobutylene from a tert-butanol containing fraction (variants). Russian patent No. 2567556 (in Russian).

3. Perspectives of intensification of the process of production of polymerization grade isobutylene;Baiguzin;Chem. Industry Today.,2016

4. An overview of industrial processes for the production of olefins – C4 hydrocarbons;Bender;Chem. Bio. Eng. Rev.,2014

5. Studies of tert-butanol dehydration over sulfocationic catalysts at concurrent of liquid and vapour flows;Burmistrov;Kataliz v promyshl.,2017

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