Combination of oxidation and dehydrogenation processes of isoamylenes in the production of isoprene on iron potassium catalyst


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Abstract

A theoretical model of the industrial method of the compensation of thermal energy consumed on the endothermic dehydrogenation on a fixed catalyst layer has been described. The combination of endothermic dehydrogenation with interlayer (intermediate) oxidation of produced hydrogen has been considered based on the example of the dehydrogenation of isoamylenes to isoprene. The calculated results are compared with laboratory tests.

About the authors

E. Kh. Karimov

Sterlitamak Petrochemical Plant JSC

Author for correspondence.
Email: karimov.edyard@gmail.com
Russian Federation, Sterlitamak

L. Z. Kas’yanova

Sterlitamak Petrochemical Plant JSC

Email: karimov.edyard@gmail.com
Russian Federation, Sterlitamak

E. M. Movsumzade

Ufa State Petroleum Technological University

Email: karimov.edyard@gmail.com
Russian Federation, Ufa

R. R. Daminev

Ufa State Petroleum Technological University

Email: karimov.edyard@gmail.com
Russian Federation, Ufa

O. Kh. Karimov

Ufa State Petroleum Technological University

Email: karimov.edyard@gmail.com
Russian Federation, Ufa

M. R. Yalalov

Ufa State Petroleum Technological University

Email: karimov.edyard@gmail.com
Russian Federation, Ufa

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