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Stable catalyst design for the viable activation of methane to syngas, hydrogen, and chemicals

Problem statement

Methane and light alkanes are surplus species and by-products with relatively poor economic interest. Our goal is to activate C–H σ-bond to produce hydrogen, olefins, carbon monoxide, and carbon nanofibers, following different process strategies such as oxidative coupling (for olefins), CO2 dry reforming (for syngas), cracking or catalytic decomposition (for hydrogen-free of COx and sequestrated carbon nanotubes/nanofibers), cracking/co-cracking with CO or methanol. We work on developing, synthesizing, characterizing, and testing innovative catalysts with a twist of reaction engineering concepts, looking at multi-scale implications.

We delve into the mechanistic insights of a series of in-house synthesized metal-supported heterogeneous catalysts by combining them with dynamic reactors and ab initio calculations. We explore catalysts with promoted lifetime, activity, selectivity, and heat exchange.

We investigate novel reactor designs grounded on forced dynamic (operando) fluidized-bed reactors at high pressures to amplify the kinetic information and hydrogen.

Goals

  • Develop a microkinetic-based modeling framework to analyze the catalyst performance
  • Scale the technical catalyst for its application in demanding exothermic (oxidative coupling of methane using SiC and spray drying) or fluidized-bed (catalytic decomposition of methane) conditions
  • Develop new catalytic concepts based on Ni-alloys (Ni-Fe, -Co, -Zn…)
  • Improve the catalyst structure-function correlations using in-situ, operando, and dynamic techniques and reactors
CHA2023

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Related Publications

Effect of the particle blending-shaping method and silicon carbide crystal phase for Mn-Na-W/SiO2-SiC catalyst in oxidative coupling of methane
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Authors: Lezcano, Kulkarni, Velisoju, Musteata, Hita, Ramirez, Dikhtiarenko, Gascon, Castaño
  • CHA
  • HCE
Engineering Thermally Resistant Catalytic Particles for Oxidative Coupling of Methane Using Spray-Drying and Incorporating SiC
Ind. Eng. Chem. Res. Year: 2021
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Activation of n-pentane while prolonging HZSM-5 catalyst lifetime during its combined reaction with methanol or dimethyl ether
Catal. Today Year: 2022 DOI:https://doi.org/10.1016/j.cattod.2020.09.015
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  • O2H
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Illuminating the Intrinsic Effect of Water Co-feeding on Methane Dehydroaromatization: A Comprehensive Study
ACS Catal. Year: 2021 DOI:https://doi.org/10.1021/acscatal.1c02763
Authors: Çaǧlayan, Lucini Paioni, Dereli, Shterk, Hita, Abou-Hamad, Pustovarenko, Emwas, Dikhtiarenko, Castaño, Cavallo, Baldus, Chowdhury, Gascon
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Kinetics and Reactor Modeling of the Conversion of n-Pentane using HZSM-5 catalysts with Different Si/Al ratio
React. Chem. Eng. Year: 2019
Authors: Cordero-Lanzac, Aguayo, Castaño, Bilbao
  • CHA
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Simultaneous Modeling of the Kinetics for n-Pentane Cracking and the Deactivation of a HZSM-5 Based Catalyst
Chem. Eng. J. Year: 2018
Authors: Cordero-Lanzac, Aguayo, Gayubo, Castaño, Bilbao
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Assessment of Thermogravimetric Methods for Calculating Coke Combustion-Regeneration Kinetics of Deactivated Catalyst
Chem. Eng. Sci. Year: 2017
Authors: Ochoa, Ibarra, Bilbao, Arandes, Castaño
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Effect of Cofeeding Butane with Methanol on the Deactivation by Coke of a HZSM-5 Zeolite Catalyst
Ind. Eng. Chem. Res. Year: 2011
Authors: Aguayo, Castaño, Mier, Gayubo, Olazar, Bilbao
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