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Further insights into the effect of sulfur on the activity and selectivity of cobalt-based Fischer–Tropsch catalysts
KTH, Skolan för kemivetenskap (CHE), Kemiteknik, Kemisk teknologi.ORCID-id: 0000-0003-3826-1858
KTH, Skolan för kemivetenskap (CHE), Kemiteknik, Kemisk teknologi.
KTH, Skolan för kemivetenskap (CHE), Kemiteknik, Kemisk teknologi.
2016 (engelsk)Inngår i: Catalysis Today, ISSN 0920-5861, E-ISSN 1873-4308, Vol. 275, s. 119-126Artikkel i tidsskrift (Fagfellevurdert) Published
Resurstyp
Text
Abstract [en]

 A sulfur poisoning study was performed by ex situ poisoning of a platinum-promoted cobalt/alumina catalyst with different sulfur amounts. The poisoned catalyst samples were tested at relevant Fischer–Tropsch reaction conditions and at the same CO conversion in order to evaluate the effect of sulfur on catalyst activity and product selectivity. It was found that the activity and the selectivity to long-chain hydrocarbons decrease with increasing sulfur content. Moreover, it was found that sulfur has no significant effect on the CO2 selectivity. It was also shown that sulfur significantly enhances olefin hydrogenation. Finally, a deactivation model relating the catalyst activity and the sulfur to cobalt active site ratio was proposed and used to describe the experimental results.

sted, utgiver, år, opplag, sider
2016. Vol. 275, s. 119-126
Emneord [en]
Fischer–Tropsch, Sulfur, Cobalt, Deactivation, Selectivity
HSV kategori
Identifikatorer
URN: urn:nbn:se:kth:diva-182347DOI: 10.1016/j.cattod.2015.10.039ISI: 000382420300017Scopus ID: 2-s2.0-84964998582OAI: oai:DiVA.org:kth-182347DiVA, id: diva2:904222
Merknad

QC 20160926

Tilgjengelig fra: 2016-02-18 Laget: 2016-02-18 Sist oppdatert: 2017-11-30bibliografisk kontrollert
Inngår i avhandling
1. Deactivation of cobalt and nickel catalysts in Fischer-Tropsch synthesis and methanation
Åpne denne publikasjonen i ny fane eller vindu >>Deactivation of cobalt and nickel catalysts in Fischer-Tropsch synthesis and methanation
2016 (engelsk)Doktoravhandling, med artikler (Annet vitenskapelig)
Abstract [en]

            A potential route for converting different carbon sources (coal, natural gas and biomass) into synthetic fuels is the transformation of these raw materials into synthesis gas (CO and H2), followed by a catalytic step which converts this gas into the desired fuels. The present thesis has focused on two catalytic steps: Fischer-Tropsch synthesis (FTS) and methanation. The Fischer-Tropsch synthesis serves to convert synthesis gas into liquid hydrocarbon-based fuels. Methanation serves instead to produce synthetic natural gas (SNG). Cobalt catalysts have been used in FTS while nickel catalysts have been used in methanation.

            The catalyst lifetime is a parameter of critical importance both in FTS and methanation. The aim of this thesis was to investigate the deactivation causes of the cobalt and nickel catalysts in their respective reactions.

            The resistance to carbonyl-induced sintering of nickel catalysts supported on different carriers (γ-Al2O3, SiO2, TiO2 and α-Al2O3) was studied. TiO2-supported nickel catalysts exhibited lower sintering rates than the other catalysts. The effect of the catalyst pellet size was also evaluated on γ-Al2O3-supported nickel catalysts. The use of large catalyst pellets gave considerably lower sintering rates. The resistance to carbon formation on the above-mentioned supported nickel catalysts was also evaluated. Once again, TiO2-supported nickel catalysts exhibited the lowest carbon formation rates. Finally, the effect of operating conditions on carbon formation and deactivation was studied using Ni/TiO2 catalysts. The use of higher H2/CO ratios and higher pressures reduced the carbon formation rate. Increasing the temperature from 280 °C to 340 °C favored carbon deposition. The addition of steam also reduced the carbon formation rate but accelerated catalyst deactivation.

            The decline in activity of cobalt catalysts with increasing sulfur concentration was also assessed by ex situ poisoning of a cobalt catalyst. A deactivation model was proposed to predict the decline in activity as function of the sulfur coverage and the sulfur-to-cobalt active site ratio. The results also indicate that sulfur decreases the selectivity to long-chain hydrocarbons and olefins.

sted, utgiver, år, opplag, sider
Stockholm: US-AB, 2016. s. xii, 124
Serie
TRITA-CHE-Report, ISSN 1654-1081
Emneord
cobalt, nickel, Fischer-Tropsch synthesis, methanation, deactivation, carbonyl, sintering, carbon fomation. sulfur, poisoning
HSV kategori
Forskningsprogram
Kemiteknik
Identifikatorer
urn:nbn:se:kth:diva-190593 (URN)978-91-7729-060-5 (ISBN)
Disputas
2016-09-23, F3, Lindstedtsvägen 26, Stockholm, 10:00 (engelsk)
Opponent
Veileder
Forskningsfinansiär
EU, FP7, Seventh Framework Programme, 308733
Merknad

QC 20160817

Tilgjengelig fra: 2016-08-17 Laget: 2016-08-12 Sist oppdatert: 2016-08-18bibliografisk kontrollert

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