Process for preparing a porous inorganic powder
The present invention is directed to a process for preparing an inorganic aerogel, the process comprising the steps of providing a composition (I) suitable to form an inorganic gel with a gelation time t G , spraying the composition (I) into supercritical carbon dioxide at a spraying time t S to obtain gel particles, and drying the gel particles obtained in step (ii) by supercritical liquid extraction, wherein the ratio t S :t G is in the range of from 0.2 to 0.99. The present invention further is directed to the inorganic aerogel as such as well as the use of the inorganic aerogel according to the invention in particular for medical and pharmaceutical applications or for thermal insulation.
1. A process for preparing an inorganic aerogel, the process comprising:
(i) providing a composition (I) suitable to form an inorganic gel with a gelation time t G ,
(ii) spraying the composition (I) into supercritical carbon dioxide at a spraying time t S to obtain gel particles,
(iii) drying the gel particles obtained in step (ii) by supercritical liquid extraction,
wherein the ratio t S :t G is in the range of from 0.2 to 0.99, wherein the inorganic aerogel is a silica based aerogel.
2. The process according to claim 1 , wherein composition (I) comprises at least one alkoxysilane.
3. The process according to claim 1 , wherein the ratio t S :t G is in the range of from 0.4 to 0.95.
4. The process according to claim 1 , wherein the composition (i) further comprises an additive.
5. The process according to claim 1 , wherein the carbon dioxide is used for the supercritical liquid extraction according to step (iii).
6. A process for preparing an inorganic aerogel, the process comprising:
(i) providing a composition (I) suitable to form an inorganic gel with a gelation time t G , wherein the composition (I) comprises at least one alkoxysilane,
(ii) spraying the composition (I) into supercritical carbon dioxide at a spraying time t S to obtain gel particles,
(iii) drying the gel particles obtained in step (ii) by supercritical liquid extraction,
wherein the ratio t S :t G is in the range of from 0.2 to 0.99.
7. The process according to claim 6 , wherein the ratio t S :t G is in the range of from 0.4 to 0.95.
8. The process according to claim 6 , wherein the composition (i) further comprises an additive.
9. The process according to claim 6 , wherein the carbon dioxide is used for the supercritical liquid extraction according to step (iii).