Purification of finely divided, pyrogenically prepared metal oxide particles
View Patent ↗Process for removing halide compounds adhering to finely divided metal oxide particles by means of steam, wherein the metal oxide particles are applied to the upper part of an upright column and migrate downwards by means of gravity, the steam is applied at the bottom end of the column, the metal oxide particles and the steam are fed counter-currently, the metal oxide particles freed of halide residues are removed at the base of the column, steam and halide residues are removed at the head of the column, wherein the column is heated in such a manner that the temperature difference T bottom −T top between the lower part and the upper part of the column is at least 20° C. and a maximum temperature of 500° C. prevails in the column, and the metal oxide particles have a residence time in the column of from 1 second to 30 minutes.
1. A process for removing halide compounds adhering to finely divided metal oxide particles having a BET surface area of from 5 to 600 m 2 /g with steam, the metal oxide particles being formed by reaction of halide-containing starting materials by hydrolysis or oxidizing gases, wherein
said finely divided metal oxide particles containing residues of halide compounds are fed, together with reaction gases, to the upper part of an upright column and migrate downwards through the column due to gravity,
steam having a temperature of from 100° C. to 500° C., optionally mixed with air, is fed to the bottom end of the column,
the finely divided metal oxide particles containing residues of halide compounds and the steam are fed counter-currently,
the metal oxide particles freed of halide residues are removed at the base of the column, and
steam and halide residues are removed at the head of the column,
which process is characterized in that
the column is heated in such a mariner that the temperature difference T bottom −T top between the lower part and the upper part of the column is from 50° C. to 100° C., the maximum temperature in the column is in the lower part of the column, the maximum temperature in the column is from 350° C. to 425° C., and the metal oxide particles have a residence time in the column of from 1 second to 30 minutes.
2. The process according to claim 1 , characterized in that the residence time is from 5 seconds to 5 minutes.
3. The process according to claim 1 , characterized in that the metal oxide particles entering the column have a temperature of from about 100° C. to 250° C.
4. The process according to claim 1 , characterized in that the amount of steam that is introduced is from 0.0025 to 0.25 kg of steam per hour per kg of metal oxide particles.
5. The process according to claim 1 , characterized in that, after the metal oxide particles have been removed at the base of the column, they are passed through at least one further column in which the maximum temperature does not exceed 500° C.
6. The process according to claim 5 , characterized in that the metal oxide particles and the steam are fed co-currently or counter-currently in the further columns.
7. The process according to claim 5 , characterized in that the second and subsequent columns have a temperature difference T bottom −T top between the lower part and the upper part of the columns of at least 5° C.
8. The process according to claim 1 , wherein the steam entering the column has a temperature of from 120° C. to 200° C.
9. The process according to claim 2 , wherein the steam entering the column has a temperature of from 120° C. to 200° C.
10. The process according to claim 2 , wherein the amount of steam that is introduced is from 0.0025 to 0.25 kg of steam per hour per kg of metal oxide particles.
11. The process according to claim 3 , wherein the amount of steam that is introduced is from 0.0025 to 0.25 kg of steam per hour per kg of metal oxide particles.