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Relationships of the Production of Hydrogen-Containing Gas from Methane on a Pilot Installation with a Moving Bed of a Microspherical Catalyst and Separate Supply of the Feed and Oxidant

Authors
  • Gerzeliev, I. M.1
  • Podoprigora, E. V.1
  • Pimenov, A. A.2
  • 1 Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences, Moscow, 119991, Russia , Moscow (Russia)
  • 2 Samara State Technical University, Samara, 443100, Russia , Samara (Russia)
Type
Published Article
Journal
Russian Journal of Applied Chemistry
Publisher
Pleiades Publishing
Publication Date
Nov 01, 2020
Volume
93
Issue
11
Pages
1729–1736
Identifiers
DOI: 10.1134/S1070427220110142
Source
Springer Nature
Keywords
License
Yellow

Abstract

AbstractThe concept of a new technology for producing hydrogen-containing gas from methane is presented. The process is performed in two separate vessels, a reactor and a regenerator, between which a microspherical catalyst containing active lattice oxygen continuously circulates. The following parameters of oxidative methane conversion were reached in experiments on a pilot installation with a moving bed of a microspherical catalyst and separate supply of the feed and oxidant: methane conversion 95%, molar ratio Н2/СО = 2, catalyst performance (hydrogen output) 0.072 kghydrogen h–1 (kgcatalyst)–1. The possibility of producing a methane–hydrogen mixture free of carbon oxides under the conditions of low methane conversion at 550°С and the volumetric space velocity of the feed of 1.5 h–1 was demonstrated. The methane conversion under these conditions is 19.6%, and the hydrogen and methane concentrations are 38 and 61 mol %, respectively. The hydrogen output under these conditions is 0.038 kghydrogen h–1 (kgcatalyst)–1.

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