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Production of Isobutylene from Syngas – Isosynthesis Over Zirconia-Based Catalysts

  • Niko Heikkinen*
  • , Laura Keskiväli
  • , Krista Kuutti
  • , Rasmus Ikonen
  • , Bhumi A. Baraiya
  • , Ville Korpelin
  • , Manu Lahtinen
  • , Jaana Kanervo
  • , Mikko J. Heikkilä
  • , Xinwei Ye
  • , Bert M. Weckhuysen
  • , Karoliina Honkala
  • , Juha Lehtonen
  • , Matti Reinikainen
  • *Corresponding author for this work
  • University of Jyväskylä
  • Neste Oyj
  • University of Helsinki
  • Utrecht University

Research output: Contribution to journalArticleScientificpeer-review

Abstract

This study presents the conversion of syngas (synthesis gas, CO + H2) into isobutylene with monoclinic zirconia (m-ZrO2), mixed monoclinic/tetragonal zirconia (m/t-ZrO2), tetragonal zirconia (t-ZrO2) and Ce/La-doped zirconia samples. The physical and chemical properties of the catalyst samples were characterised with nitrogen physisorption, NH3 and CO2 temperature-programmed desorption (TPD) and diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS). Sample material crystal structures were analysed with powder X-ray diffraction (PXRD) analysis. The pure monoclinic ZrO2 sample showed the best catalytic performance with 66% CO conversion and 44 mol-% C/hydrocarbons isobutylene selectivity at reaction conditions of 450 °C, 45 bar, GHSV = 2000 h−1, and CO: H2 = 1:1. While pure monoclinic ZrO2 was a highly efficient catalyst for the isosynthesis reaction, pure tetragonal ZrO2 produced only a minor amount of isobutylene (~ 1 mol-%C/hydrocarbons). Interestingly, Ce/La-doped zirconia had a cubic/tetragonal crystal structure, while showing selectivity and activity comparable to m-ZrO2 (CO conversion 64% and isobutylene selectivity of 40 mol-% C/hydrocarbons). Although samples with a purely t-ZrO₂ crystal phase significantly reduced the desired isobutylene selectivity, catalysts with relatively high Ce/La loadings (17% and 5% of the total catalyst mass) in the cubic/tetragonal crystal structure achieved high isobutylene activity and selectivity, owing to the dopant-induced high base-to-acid site ratio and enhanced synthesis gas adsorption capacity. According to the results from density functional theory (DFT) calculations, the poor selectivity of the t-ZrO2 phase towards isobutylene was due to the promoted intermediate methanation on the coordinatively saturated sites of t-ZrO2. Compared to the t-ZrO2 sample, m-ZrO2 showed high isobutylene selectivity and activity related to high base to acid site ratio, high synthesis gas adsorption capacity, and kinetically favourable crystal structure to form C2+ hydrocarbons from C1 intermediates. These results are important factors in the future work to prepare intrinsically active and isobutylene selective catalysts for the isosynthesis reaction.

Original languageEnglish
Pages (from-to)2418-2432
Number of pages15
JournalTopics in Catalysis
Volume68
Issue number20
DOIs
Publication statusPublished - Dec 2025
MoE publication typeA1 Journal article-refereed

Funding

The work was financially supported by the Business Finland project Synjet (Dnro 6675/31/2021).

Keywords

  • Isobutylene
  • Isosynthesis
  • Monoclinic
  • Syngas
  • Tetragonal
  • Zirconia catalyst

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