Process for thermal decomposition of aluminum chloride hexahydrate
AssigneeAluminum Pechiney
InventorsLothar Reh, Ludolf Plass, Hans Werner Schmidt, Gunter Schoene, Philippe Marchessaux
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Abstract
Process for the thermal decomposition of aluminum chloride hexahydrate into anhydrous Al.sub.2 O.sub.3, comprising predrying and then decomposition in a fluidization reactor, the said fluidization being ensured by recycled gaseous HCl, and finally heating at the temperature necessary to obtain the desired crystallization state, namely anhydrous Al.sub.2 O.sub.3, the said pre-drying being carried out by the gases coming from this final heating.
Claims17
A process for the thermal decomposition of aluminum chloride hexahydrate into anhydrous Al.sub.2 O.sub.3 comprising:
- (1) continuously introducing the aluminum chloride hexahydrate into a turbulent reaction zone;
- (2) continuously introducing an amount of gas below a gas distributor in the turbulent reaction zone to maintain the solid material above the distributor in a fluidized state with a decrease in the concentration of solid material from the bottom to the top of said turbulent reaction zone;
- (2') continuously introducing a secondary gas into the turbulent reaction zone at a level above the gas distributor;
- (3) continuously extracting the solid material with the gas from the upper portion of the turbulent reaction zone;
- (4) continuously separating the solid material from the gas extracted from the upper portion of the turbulent reaction zone;
- (5) continuously feeding the separated solid material to a residence reaction zone which is operatively connected and maintained separate and apart from the turbulent reaction zone;
- (6) continuously introducing gases into the residence reaction zone in an amount sufficient to maintain the solid material in a fluidized state;
- (7) continuously recycling a portion of the solid material from the residence reaction zone downwardly to an intermediate portion of the turbulent reaction zone;
- (8) extracting a portion of the solid material from the residence zone as product;
- and
- (9) maintaining the suspension density in the turbulent reaction zone in the area between the gas distributor and the secondary gas inlet at an average of 20-300 kg/m.sup.3 inlet to a value between 1 and 20 kg/m.sup.2 and maintaining the suspension density in the reaction zone at an average greater than 600 kg/m.sup.3.
Dependencies are inferred from the claim text.