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Researchers develop new catalysts for a direct Fischer-Tropsch to olefins (FTO) process

Researchers in the Netherlands have demonstrated the direct conversion of synthesis gas through a Fischer-Tropsch process to C2 through C4 light olefins with selectivity up to 60 wt.% using catalysts that constitute iron nanoparticles (promoted by sulfur plus sodium) homogeneously dispersed on weakly interactive α-alumina or carbon nanofiber supports. A paper on their work is published in the current issue of the journal Science.

Lower olefins are key building blocks for plastics, cosmetics, and drugs. Conventionally, light olefins are produced by steam cracking of crude oil–derived naphtha, but, as the authors note in their paper, there is a pressing need for alternative feedstocks and processes in view of supply limitations and of environmental issues.

Although Fischer-Tropsch (F-T) synthesis can convert coal-, biomass-, and natural gas-derived synthesis gas into hydrocarbon derivatives, selectivity toward lower olefins tends to be low. As a result, non-petroleum production routes for olefins usually involve at least two conversion steps, involving either cracking of FT-derived hydrocarbons or the methanol to olefins (MTO) process.

For several decades, research groups have attempted to develop iron-based catalysts to direct product selectivity of the FT synthesis toward light olefins. Relative to other FT catalysts such as cobalt, iron disfavors competing formation of methane, and furthermore catalyzes the water-gas shift reaction, enabling the use of a CO-rich syngas feed without an H2/CO ratio adjustment.

...Despite...promising results, however, the bulk iron catalysts are mechanically unstable when the reaction is performed at high temperature, which is necessary to steer product selectivity to lighter hydrocarbons...The poor mechanical stability of the bulk iron oxide catalysts may lead to plugging of the catalyst bed in fixed-bed operation or to fouling of separation equipment in a fluidized-bed process.

Supported iron catalysts display enhanced dispersion of the active phase and may withstand the mechanical degradation that threatens bulk iron catalysts. Research on supported iron catalysts has met with limited success, however.

...To overcome the low activity and mechanical stability problems, we explored the use of support materials weakly interactive toward iron.

—Galvis et al.

The team formulated and tested their supported and bulk Fe catalysts in the FT reaction initially at 1 bar and 350°C at low CO conversion (0.5 to 1%) to restrict secondary hydrogenation of olefins. Among their findings:

  • High initial activity was observed for Fe/β-SiC and Fe/CNF.

  • The activity of Fe/CNF decreased continuously during the 15 hours of reaction; the activity of the Fe/β-SiC catalyst increased during the first 5 hours of reaction, then decreased slowly afterward.

  • Fe/α-Al2O3 exhibited a lower catalytic activity than Fe/CNF and Fe/β-SiC; however, it showed remarkable stability, as the activity remained constant over 15 hours.

  • Fe/γ-Al2O3 and Fe/SiO2 displayed a low catalytic activity, comparable to the bulk Fe catalysts.

  • Fe/CNF and Fe/α-Al2O3 exhibited high selectivity toward lower olefins (~60% C) while directing comparatively little carbon to methane (<25% C)—an important attribut of an FTO catalyst.

  • Fe/β-SiC and Fe/SiO2 also showed high selectivity to C2 through C4 olefins, but the CH4 product fraction was higher than 30% C.

  • Fe/γ-Al2O3 and the bulk catalysts displayed a high selectivity to methane (>40% C).

Based on the results obtained at 1 bar, they prepared and tested additional α-Al2O3–supported catalysts with different iron loadings (6 and 25 wt % Fe) to study the effect of iron content on catalytic performance at 20 bar.

The promoted catalysts prepared using supports with low interaction with iron showed high catalytic activities combined with high selectivities to the desired products. Fe/CNF and 25 wt % Fe/α-Al2O3 exhibited high selectivities toward light olefins (>50% C) while yielding a methane product fraction lower than 15% C.

The FTO process represents a strong alternative route for the sustainable production of lower olefins from biomass-derived synthesis gas. The industrial potential of this process is greatly enhanced by the reported development of active, selective, and mechanically stable catalysts that consist of promoted iron nanoparticles dispersed on weakly interactive supports. Further suppression of methane production, maximization of the C2-C4 olefins fraction, and reduction of carbon lay-down by addition of promoters and by optimization of physical properties (e.g., Fe particle size, distribution of Fe nanoparticles on the support) will allow us to further understand and develop the performance of these catalysts.

—Galvis et al.


  • Hirsa M. Torres Galvis, Johannes H. Bitter, Chaitanya B. Khare, Matthijs Ruitenbeek, A. Iulian Dugulan, and Krijn P. de Jong (2012) Supported Iron Nanoparticles as Catalysts for Sustainable Production of Lower Olefins. Science 335 (6070), 835-838.doi: 10.1126/science.1215614



As I recall, the Mobil Methanol to Gasoline method also has an MTO for light olefins and an MTD for diesel.

Henry Gibson

The methanol to gasoline process also uses specially formulated zeolites.

A computer operated system can be made that would form diesel fuel and a proportion of exhaust gases, after using air to start, into a high octane rated gas mixture for spark ignited engines. Diesel for lorries and low taxed marked diesel for automobiles plus methanol should be the only liquid fuels sold for automobiles.

Methanol is more than an adequate fuel and engines could be tuned to use its high octane rating for more efficiency, but hydraulic hybrid systems are now the most cost effective way for higher automotive efficiency.

Electrically operated valves should be used for many engines.

Coates Limited makes an engine valve that should interest many and should at least be used in portable generators and electric automobile range extenders. The tiny and not so tiny Rotating Cylinder Valve is also a candidate for a tiny range extender. ..HG..

Alex Kovnat

I wish those Netherlands researchers all the best in mastering the art of synthesizing light olefins directly from CO + H2, instead of having to go through the process of CO + H2 --> Methanol --> light olefins. Right now, the Saudi Arabia Basic Industries Corporation would like to build a facility that would use the latter process. But if it proves feasible to produce olefins directly from CO + H2, it will be more efficient in utilizing natural gas or biomass in producing the basic building blocks of the polymer industry.


"biomass-derived synthesis gas..."

It seems like the key here is how clean is the gas. Biomass varies in composition and even with cyclones and ceramic filters, the gas still has substances in it that can contaminate the catalysts.


MTG zeolites are reconditioned by burning off the coke, this was shown in the 1980s project Mobil did in New Zealand. The Mobil process is proven, the Core Biofuels process is ramping up, there are options and now it is up to us to use them to our advantage.


Typepad is censoring my postings. Twice I have put up comments talking about oil availability in the 1980s and the Persian Gulf and twice it refused to post them.


Typepad's spam filters are a bit over-reactive for typical GCC fare. MM will rescue posts from purgatory if you ask him.


That is OK, no big deal.


He's also submitting posts to Typepad to help them tune their filters better. You might want to be part of the solution (instead of part of the precipitate).


They have the postings that were rejected, they should be able to find the keyword that triggered it.


He doesn't watch the spam-trap closely, you have to point him to the problems.



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