Production of Ethylene, CO, and Hydrogen by Oxidative Cracking of Oil Refinery Gas Components


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Flowsheets based on the results of experimental studies and detailed kinetic modeling were suggested for oxidative cracking of oil refinery gas components to obtain ethylene, CO, and hydrogen. The calculations show that oxidative cracking alone does not allow production of ethylene and СО in ratios required for the further catalytic carbonylation and hydroformylation of ethylene. Matrix conversion of a part of oxy-cracking products is suggested as an additional step for producing CO and hydrogen.

Sobre autores

A. Ozerskii

Institute of Problems of Chemical Physics; Semenov Institute of Chemical Physics

Autor responsável pela correspondência
Email: alex.ozersky.1992@gmail.com
Rússia, Chernogolovka, Moscow oblast, 142432; Moscow, 117977

A. Nikitin

Institute of Problems of Chemical Physics; Semenov Institute of Chemical Physics

Email: alex.ozersky.1992@gmail.com
Rússia, Chernogolovka, Moscow oblast, 142432; Moscow, 117977

I. Sedov

Institute of Problems of Chemical Physics; Moscow State University

Email: alex.ozersky.1992@gmail.com
Rússia, Chernogolovka, Moscow oblast, 142432; Moscow, 119991

I. Fokin

Institute of Problems of Chemical Physics

Email: alex.ozersky.1992@gmail.com
Rússia, Chernogolovka, Moscow oblast, 142432

V. Savchenko

Institute of Problems of Chemical Physics

Email: alex.ozersky.1992@gmail.com
Rússia, Chernogolovka, Moscow oblast, 142432

V. Arutyunov

Institute of Problems of Chemical Physics; Semenov Institute of Chemical Physics; Moscow State University

Email: alex.ozersky.1992@gmail.com
Rússia, Chernogolovka, Moscow oblast, 142432; Moscow, 117977; Moscow, 119991

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