System for preparing silica aerogel
The system for preparing silica aerogel comprises a raw material supply part transferring at least one raw material of de-ionized water, water glass, a surface modifier, an inorganic acid, and an organic solvent to a mixing part, the mixing part mixing the raw materials transferred from the raw material supply part to produce silica wet gel, a separating part separating at least one raw material of the raw materials from the mixture containing the silica wet gel transferred from the mixing part, a drying part drying the silica wet gel transferred from the separating part to produce the silica aerogel, a recovery part recovering a portion of the vaporized raw material of the raw materials used in at least one of the mixing part and the drying part, and a heat transfer part transferring heat to at least one of the mixing part and the drying part.
1. A system for preparing silica aerogel, the system comprising:
a raw material supply part transferring at least one raw material of de-ionized water, water glass, a surface modifier, an inorganic acid, and an organic solvent to a mixing part;
the mixing part mixing the raw materials transferred from the raw material supply part to produce silica wet gel;
a separating part comprising:
a liquid-liquid decanter attached to the mixing part for separating water from the mixture containing the organic solvent and silica wet gel transferred from the mixing part;
a drying part drying the silica wet gel transferred from the separating part to produce the silica aerogel;
a recovery part recovering a portion of the vaporized raw material of the raw materials used in at least one of the mixing part and the drying part; and
a heat transfer part transferring heat to at least one of the mixing part and the drying part.
2. The system of claim 1 , wherein the inorganic acid is nitric acid (HNO 3 ),
the organic solvent is hexane, and
the surface modifier is hexamethyldisilazane (HMDS).
3. The system of claim 1 , wherein the liquid-liquid decanter separates the water by using a difference in specific gravity.
4. The system of claim 1 , wherein the separating part further comprises an organic solvent separator that separates the organic solvent from the mixture passing through the water separator.
5. The system of claim 4 , wherein the organic solvent separator separates the organic solvent by using centrifugal force.
6. The system of claim 1 , wherein silica aerogel powder is produced in the drying part, and
the system further comprises a collecting part that collects the silica aerogel powder.
7. The system of claim 1 , wherein the recovery part comprises:
a condenser that liquefies the raw material recovered in a gas state;
a storage tank receiving the raw material liquefied in the condenser to store the raw material; and
a vacuum pump controlling a pressure of each of the condenser and the storage tank.
8. The system of claim 7 , wherein the recovery part further comprises a solvent separating device that separates an organic solvent from the raw material stored in the storage tank.
9. The system of claim 8 , wherein the solvent separating device separates the organic solvent by using a difference in boiling point.
10. The system of claim 9 , wherein the solvent separating device comprises a distillation column,
the organic solvent is recovered from an upper portion of the distillation column, and
the surface modifier or the surface modifier that is in an oxidized state is recovered from a lower portion of the distillation column.