Catalytic performance and attrition strength of spray-dried iron catalysts for slurry phase Fischer–Tropsch synthesis

. Three iron Fischer–Tropsch (F–T) catalysts were prepared by spray drying. Catalyst prepared employing colloidal silica had the highest attrition strength among all catalysts studied. After 345 h of F–T synthesis in a stirred tank slurry reactor (STSR) it retained its micro-spherical particle morph...

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Veröffentlicht in:Applied catalysis. A, General General, 2010-11, Vol.388 (1), p.240-247
Hauptverfasser: Bukur, Dragomir B., Carreto-Vazquez, Victor H., Ma, Wenping
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Carreto-Vazquez, Victor H.
Ma, Wenping
description . Three iron Fischer–Tropsch (F–T) catalysts were prepared by spray drying. Catalyst prepared employing colloidal silica had the highest attrition strength among all catalysts studied. After 345 h of F–T synthesis in a stirred tank slurry reactor (STSR) it retained its micro-spherical particle morphology. Catalytic performance of these catalysts during F–T synthesis was excellent (methane selectivity 2.0–3.5% and C 5 + hydrocarbons 78–89% on C-atom basis). [Display omitted] ▶ Micro-spherical Fe F–T catalysts were prepared by spray drying. ▶ Catalytic performance was evaluated in a stirred tank slurry reactor (STSR). ▶ One of the catalysts retained micro-spherical shape after F–T reaction in the STSR. ▶ Catalysts had low methane (1.8–3.5%) and high C 5 + hydrocarbon selectivity (75–89%). Three iron Fischer–Tropsch (F–T) catalysts (100 Fe/3 Cu/5 K/16 SiO 2 in parts by weight) in the form of micro-spherical particles were prepared by spray drying. Their particle size distribution was rather broad, ranging from 5 to 40 μm in diameter, regardless of the source of silica (colloidal silica, tetraethyl orthosilicate, or potassium silicate) employed in their preparation. Catalyst prepared employing colloidal silica had the highest attrition strength among all catalysts studied. After 345 h of testing in a stirred tank slurry reactor its morphology remained essentially unchanged, and it experienced small reductions in the volume mean diameter (5.4%) and generation of particles smaller than 10 μm in diameter was very small (0.7%). Catalytic performance of these catalysts during F–T synthesis was excellent. Syngas conversion was between 71 and 76%, whereas methane selectivity was between 2.0 and 3.5% and that of C 5 + hydrocarbons was 78–89% (on C-atom basis).
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Three iron Fischer–Tropsch (F–T) catalysts were prepared by spray drying. Catalyst prepared employing colloidal silica had the highest attrition strength among all catalysts studied. After 345 h of F–T synthesis in a stirred tank slurry reactor (STSR) it retained its micro-spherical particle morphology. Catalytic performance of these catalysts during F–T synthesis was excellent (methane selectivity 2.0–3.5% and C 5 + hydrocarbons 78–89% on C-atom basis). [Display omitted] ▶ Micro-spherical Fe F–T catalysts were prepared by spray drying. ▶ Catalytic performance was evaluated in a stirred tank slurry reactor (STSR). ▶ One of the catalysts retained micro-spherical shape after F–T reaction in the STSR. ▶ Catalysts had low methane (1.8–3.5%) and high C 5 + hydrocarbon selectivity (75–89%). Three iron Fischer–Tropsch (F–T) catalysts (100 Fe/3 Cu/5 K/16 SiO 2 in parts by weight) in the form of micro-spherical particles were prepared by spray drying. Their particle size distribution was rather broad, ranging from 5 to 40 μm in diameter, regardless of the source of silica (colloidal silica, tetraethyl orthosilicate, or potassium silicate) employed in their preparation. Catalyst prepared employing colloidal silica had the highest attrition strength among all catalysts studied. After 345 h of testing in a stirred tank slurry reactor its morphology remained essentially unchanged, and it experienced small reductions in the volume mean diameter (5.4%) and generation of particles smaller than 10 μm in diameter was very small (0.7%). Catalytic performance of these catalysts during F–T synthesis was excellent. 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A, General</title><description>. Three iron Fischer–Tropsch (F–T) catalysts were prepared by spray drying. Catalyst prepared employing colloidal silica had the highest attrition strength among all catalysts studied. After 345 h of F–T synthesis in a stirred tank slurry reactor (STSR) it retained its micro-spherical particle morphology. Catalytic performance of these catalysts during F–T synthesis was excellent (methane selectivity 2.0–3.5% and C 5 + hydrocarbons 78–89% on C-atom basis). [Display omitted] ▶ Micro-spherical Fe F–T catalysts were prepared by spray drying. ▶ Catalytic performance was evaluated in a stirred tank slurry reactor (STSR). ▶ One of the catalysts retained micro-spherical shape after F–T reaction in the STSR. ▶ Catalysts had low methane (1.8–3.5%) and high C 5 + hydrocarbon selectivity (75–89%). Three iron Fischer–Tropsch (F–T) catalysts (100 Fe/3 Cu/5 K/16 SiO 2 in parts by weight) in the form of micro-spherical particles were prepared by spray drying. Their particle size distribution was rather broad, ranging from 5 to 40 μm in diameter, regardless of the source of silica (colloidal silica, tetraethyl orthosilicate, or potassium silicate) employed in their preparation. Catalyst prepared employing colloidal silica had the highest attrition strength among all catalysts studied. After 345 h of testing in a stirred tank slurry reactor its morphology remained essentially unchanged, and it experienced small reductions in the volume mean diameter (5.4%) and generation of particles smaller than 10 μm in diameter was very small (0.7%). Catalytic performance of these catalysts during F–T synthesis was excellent. 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Granulometry. Electrokinetic phenomena</topic><topic>Silicon dioxide</topic><topic>Slurries</topic><topic>Spray drying</topic><topic>Stirred tank slurry reactor</topic><topic>Synthesis</topic><topic>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Bukur, Dragomir B.</creatorcontrib><creatorcontrib>Carreto-Vazquez, Victor H.</creatorcontrib><creatorcontrib>Ma, Wenping</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Applied catalysis. 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Catalytic performance of these catalysts during F–T synthesis was excellent (methane selectivity 2.0–3.5% and C 5 + hydrocarbons 78–89% on C-atom basis). [Display omitted] ▶ Micro-spherical Fe F–T catalysts were prepared by spray drying. ▶ Catalytic performance was evaluated in a stirred tank slurry reactor (STSR). ▶ One of the catalysts retained micro-spherical shape after F–T reaction in the STSR. ▶ Catalysts had low methane (1.8–3.5%) and high C 5 + hydrocarbon selectivity (75–89%). Three iron Fischer–Tropsch (F–T) catalysts (100 Fe/3 Cu/5 K/16 SiO 2 in parts by weight) in the form of micro-spherical particles were prepared by spray drying. Their particle size distribution was rather broad, ranging from 5 to 40 μm in diameter, regardless of the source of silica (colloidal silica, tetraethyl orthosilicate, or potassium silicate) employed in their preparation. Catalyst prepared employing colloidal silica had the highest attrition strength among all catalysts studied. 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subjects Attrition
Attrition strength
Catalysis
Catalysts
Chemistry
Colloidal state and disperse state
Colloids
Exact sciences and technology
Fischer–Tropsch synthesis
General and physical chemistry
Iron
Iron catalyst
Physical and chemical studies. Granulometry. Electrokinetic phenomena
Silicon dioxide
Slurries
Spray drying
Stirred tank slurry reactor
Synthesis
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
title Catalytic performance and attrition strength of spray-dried iron catalysts for slurry phase Fischer–Tropsch synthesis
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