open access publication

Article, 2021

Tailored monolith supports for improved ultra-low temperature water-gas shift reaction

REACTION CHEMISTRY & ENGINEERING, ISSN 2058-9883, 2058-9883, Volume 6, 11, Pages 2114-2124, 10.1039/d1re00226k

Contributors

Portela, Raquel 0000-0002-1882-4759 (Corresponding author) [1] Wolf, Patrick 0000-0002-9467-5812 [2] Marinkovic, Jakob Maximilian 0000-0002-0630-5679 [3] Serrano-Lotina, Ana 0000-0001-7498-7491 [1] Riisager, Anders 0000-0002-7086-1143 [3] Haumann, Marco 0000-0002-3896-365X (Corresponding author) [2]

Affiliations

  1. [1] CSIC Consejo Super Invest Cient, Madrid, Spain
  2. [NORA names: Spain; Europe, EU; OECD];
  3. [2] Friedrich Alexander Univ Erlangen Nurnberg, Lehrstuhl Chem Reakt Tech, Egerlandstr 3, D-91058 Erlangen, Germany
  4. [NORA names: Germany; Europe, EU; OECD];
  5. [3] Tech Univ Denmark, Dept Chem, Ctr Catalysis & Sustainable Chem, Bldg 207, DK-2800 Lyngby, Denmark
  6. [NORA names: DTU Technical University of Denmark; University; Denmark; Europe, EU; Nordic; OECD]

Abstract

Supported ionic liquid-phase (SILP) particulate catalysts consisting of Ru-complexes dissolved in an ionic liquid that is dispersed on a gamma-alumina porous substrate facilitate the water-gas shift (WGS) reaction at ultra-low temperatures. In this work, a screening of different ceramic support materials was performed to design a suitable monolithic support to disperse the SILP system with the objective of scaling up the WGS process efficiently. gamma-Alumina-rich channeled monoliths were developed with the use of natural clays as binders (10 wt% bentonite and 20 wt% sepiolite) with the following properties: i) high volume of mesopores to maximize the catalyst loading and successfully immobilize the ionic liquid-catalyst system via capillary forces, ii) mechanical resistance to withstand the impregnation process and the reaction operating conditions, and iii) surface chemistry compatible with a highly active and selective phase for WGS. The developed monolithic-SILP catalyst demonstrated high stability and long-term WGS performance at 130 degrees C with an average steady-state CO conversion of around 30% after 190 h time-on-stream (TOS) and a conversion of 23% after 320 h TOS. Interestingly, the catalyst activity proved essentially unaffected by variation in the water partial pressure during operation due to accumulation of water in the monolith, thus making the system highly durable.

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