Deactivation of Ni catalyst in three-phase CO2 methanation

Abstract

In three-phase CO2 methanation dibenzyl toluene is used as the liquid phase in a slurry bubble column reactor. At reactor temperatures (TR) higher than 260 °C deactivation of the Ni/SiO2 catalyst was observed. After deactivation for 120 h at TR = 320 °C, stationary operation is possible with a loss of catalytic activity of ≈50%. Based on experimental results, it can be stated that deactivation is caused by decomposition of dibenzyl toluene at high reactor temperature, resulting in carbon deposition on the catalyst surface.

Graphical abstract: Deactivation of Ni catalyst in three-phase CO2 methanation

Article information

Article type
Paper
Submitted
04 Apr 2025
Accepted
06 Aug 2025
First published
21 Aug 2025
This article is Open Access
Creative Commons BY license

React. Chem. Eng., 2025, Advance Article

Deactivation of Ni catalyst in three-phase CO2 methanation

M. Held, A. Holfelder, S. Bajohr and T. Kolb, React. Chem. Eng., 2025, Advance Article , DOI: 10.1039/D5RE00152H

This article is licensed under a Creative Commons Attribution 3.0 Unported Licence. You can use material from this article in other publications without requesting further permissions from the RSC, provided that the correct acknowledgement is given.

Read more about how to correctly acknowledge RSC content.

Social activity

Spotlight

Advertisements