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Structure and Site Evolution of Iron Oxide Catalyst Precursors during the Fischer−Tropsch Synthesis
Abstract
The contacting of Fe oxide precursors with synthesis gas (H 2 /CO mixtures) leads to structural and chemical changes and to the formation of the active sites required for the Fischer−Tropsch synthesis (FTS). The local structure and oxidation state of the starting Fe 2 O 3 precursors promoted by Cu and/or K were probed using in situ X-ray absorption spectroscopy during these processes. The activation of these precursors occurs via reduction to Fe 3 O 4 followed by carburization to form FeC x . FTS reaction rates increased markedly during the initial stages of carburization, suggesting that the conversion of near-surface layers of Fe 3 O 4 to FeC x is sufficient for the formation of the required active sites. Thus, bulk structural probes, and any ex situ techniques without concurrent measurements of the products evolved during activation and FTS, can lead to misleading structure−function relations. The initial rate of carburization and the extent of carburization and the FTS rate at steady-state were higher for Fe 2 O 3 precursors containing either Cu or K. These effects were stronger when both promoters were present. K and Cu provide CO and H 2 activation sites, which lead to the nucleation of multiple carbide regions on Fe oxide surfaces. The larger number of nucleation sites leads to higher initial carburization rates and to smaller FeC x crystallites. These smaller crystallites, in turn, provide higher active surface areas, shorter bulk diffusion distances, more complete carburization of Fe 2 O 3 precursors, and higher steady-state FTS rates. These effects of K and Cu on the number of available FeC x sites were confirmed by titrating surface sites using CO after FTS reactions. It appears that K and Cu act predominantly as structural promoters, which increase the surface area of the active FeC x phases. Chemical promotion of catalytic rates by these additives appears not to be required to explain the observed FTS rate enhancements in the presence of K or Cu. These structural promotion effects of Cu and K account for the apparent but non-causal correlation between bulk FeC x contents and FTS rates at steady-state, even though the carburization of only near-surface regions in bulk Fe 3 O 4 is sufficient to achieve steady-state FTS turnover rates.
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Citations
Cited by
Parkinson, G. S. (2016) · Surface Science Reports · doi:10.1016/j.surfrep.2016.02.001 · Cited by 608
Fischer‐Tropsch Catalysts for the Biomass‐to‐Liquid (BTL)‐Process
van Steen, E., & Claeys, M. (2008) · Chemical Engineering & Technology · doi:10.1002/ceat.200800067 · Cited by 360
Study of an iron-manganese Fischer–Tropsch synthesis catalyst promoted with copper
ZHANG, C., YANG, Y., TENG, B., LI, T., ZHENG, H., XIANG, H., & LI, Y. (2006) · Journal of Catalysis · doi:10.1016/j.jcat.2005.11.004 · Cited by 302
Core–Shell Fe–Pt Nanoparticles in Ionic Liquids: Magnetic and Catalytic Properties
Adamski, J., Qadir, M. I., Serna, J. P., Bernardi, F., Baptista, D. L., Salles, B. R., Novak, M. A., Machado, G., & Dupont, J. (2018) · The Journal of Physical Chemistry C · doi:10.1021/acs.jpcc.7b12219 · Cited by 32
Metadata
- Authors
- Li, S., Meitzner, G. D., & Iglesia, E.
- Venue
- The Journal of Physical Chemistry B
- Publisher
- American Chemical Society (ACS)
- Published
- 2001-05-24
- Volume
- 105
- Issue
- 24
- Pages
- 5743-5750
- ISSN
- 1520-5207 (ISSN-L)
- 1520-6106
- OpenAlex
- W1997845317
- Cited by
- 168
- References
- 0
- FWCI
- 1.64
- Type
- journal article
- Language
- en
- Open access
- closed
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