Catalysis of coal hydroliquefaction by synthetic iron catalysts

The following synthetic iron catalyst precursors were investigated: FeOOH and FeOOH-Al 2O 3 (90:10 wt%) co-precipitated by ammonia, washed and dried either in an oven or by spray-drying, and Fe 2O 3 prepared by flame decomposition of FeCl 3 in the gas phase. These catalyst precursors were sulphided...

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Veröffentlicht in:Fuel (Guildford) 1983, Vol.62 (1), p.69-72
Hauptverfasser: Andres, Michèle, Charcosset, Henri, Chiche, Pierre, Davignon, Léon, Djega-Mariadassou, Gérald, Joly, Jean-Pierre, Prégermain, Simone
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container_end_page 72
container_issue 1
container_start_page 69
container_title Fuel (Guildford)
container_volume 62
creator Andres, Michèle
Charcosset, Henri
Chiche, Pierre
Davignon, Léon
Djega-Mariadassou, Gérald
Joly, Jean-Pierre
Prégermain, Simone
description The following synthetic iron catalyst precursors were investigated: FeOOH and FeOOH-Al 2O 3 (90:10 wt%) co-precipitated by ammonia, washed and dried either in an oven or by spray-drying, and Fe 2O 3 prepared by flame decomposition of FeCl 3 in the gas phase. These catalyst precursors were sulphided in situ by CS 2 during the hydroliquefaction of a highly volatile bituminous coal. An increasing catalytic activity of the iron sulphide was observed as its particle size decreases down to a very low value (0.05 μm), compared to 2–3 μm and to ⪢ 5 μm. Al 2O 3 did not act as an efficient promoter, even if it gives rise to a decrease of the iron sulphide crystallite size. Diffusional limitations and/or plugging by carbonaceous or mineral solids could result in a low efficiency of the iron sulphide crystallites which lie inside one iron catalyst particle. The above cited flame method, allowing the preparation of pure or doped Fe 2O 3 with particle size even less than 0.05 μm, is worthwhile for further work in coal hydroliquefaction catalysis, where the catalyst acts as Fe 1−xS.
doi_str_mv 10.1016/0016-2361(83)90255-7
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These catalyst precursors were sulphided in situ by CS 2 during the hydroliquefaction of a highly volatile bituminous coal. An increasing catalytic activity of the iron sulphide was observed as its particle size decreases down to a very low value (0.05 μm), compared to 2–3 μm and to ⪢ 5 μm. Al 2O 3 did not act as an efficient promoter, even if it gives rise to a decrease of the iron sulphide crystallite size. Diffusional limitations and/or plugging by carbonaceous or mineral solids could result in a low efficiency of the iron sulphide crystallites which lie inside one iron catalyst particle. 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subjects catalysis
coal
coal liquefaction
iron catalysts
title Catalysis of coal hydroliquefaction by synthetic iron catalysts
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