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Generally fixed bed reduction indicated higher gas conversion although coarser particles were used.
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To this end, experiments were run using nominally 1000 g of hematite material in a fixed bed reactor cycling between reduction and re-oxidation.
Since the reduction temperature in the fixed bed reactor was 450 °C, only nickel species in band ε and band α can be reduced to the metal phase.
It is based on the alternating reduction of an iron oxide fixed bed with synthesis gas and its subsequent oxidation with steam.
The slurry stirred tank reactor shows much lower hydrocarbon productivity than the milli- and centimetric fixed bed reactors, which is probably due to incomplete catalyst reduction.
The effect of tungsten and barium on the thermal stability of V2O5/TiO2 catalyst for NO reduction by NH3 was examined over a fixed bed flow reactor system.
Synthesis of higher alcohols was carried out after the reduction and sulfidation of catalysts in a fixed bed reactor at 320°C, 70 bars, gas hourly space velocity of 3.6 nLit/g cat./h, and H2/CO = 2.
The behaviour of a fixed bed porous flow-through monel electrode has been investigated for the reduction of nitrobenzene to p-aminophenol in an aqueous acidic electrolyte and under essentially activation controlled conditions.
The behavior of a fixed bed consisting of amalgamated copper screens has been investigated for the electrolytic reduction of nitrobenzene to p-aminophenol under potentiostatic condition (controlled potential).
The method used is based on the reduction of ferricyanide ions on a cathode consisting of a fixed bed of spherical conducting grains.
These consisted of reduction steps with hydrogen and oxidations with steam along five alternated cycles in a fixed bed reactor.
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