PII.148 Effect of reaction conditions on the product yield in the CO2 hydrogenation reaction over a K-Co-Cu-Al catalyst

Autores

  • Vitor Duarte Lage Núcleo de Catálise/Programa de Engenharia Química/COPPE/Universidade Federal do Rio de Janeiro
  • Fabio Toniolo Núcleo de Catálise/Programa de Engenharia Química/COPPE/Universidade Federal do Rio de Janeiro
  • Nicolas Bion Institut de Chimie des Milieux et Matériaux de Poitiers (IC2MP) / Université de Poitiers - CNRS
  • Anthony Le Valant Institut de Chimie des Milieux et Matériaux de Poitiers (IC2MP) / Université de Poitiers - CNRS

Palavras-chave:

CO2 hydrogenation, higher alcohol production, Co-based catalyst, Cu-based catalyst, Bimetallic catalyst

Resumo

Converting CO2 into value-added chemicals is a promising alternative to recent energetic and environmental issues, but designing a non-noble metal catalyst capable of actively and selectively converting CO2 into desirable products is yet a challenge. Herein, we report on the effect of the reaction conditions on the activity and selectivity of a K-Co-Cu-Al catalyst prepared by a coprecipitation method for the CO2 hydrogenation to higher alcohols (HAs). We investigated different reduction temperatures, reaction temperatures, space velocities, and H2/CO2 ratios to optimize its HAs yield. We observed gains yield of desired products (C2+ hydrocarbons and HAs) when finding optimum reduction temperature and reducing space velocity and H2/CO2 ratio.  K Co Cu Al reduced at 400 ºC exhibits a high HAs selectivity of 45% (21% for ethanol) and space-time yield of 5.6 mmol.h‑1.gcat‑1, under mild conditions (250 °C, 30 bar, H2/CO2 ratio of 1.5, and 14200 mL.h‑1.gcat‑1), which represents one of the best performances among related studies, especially amidst Co-based catalysts.

Publicado

06-09-2023

Edição

Seção

Pôster II Catálise em refino, petroquímica e química fina (Carmenère)