Silica particle manufacturing process

1. A method of forming a silica-based product comprising:

(a) providing a silica containing precursor (SCP) contained in solution that has a pH less than or equal to a pH of 7;

(b) doping the SCP with one or more metal species, wherein said doping occurs when the solution has a pH less than or equal to a pH of 7;

(c) adjusting the pH of the solution to greater than 7;

(d) adding an effective amount of exogenous salt to the solution so that the conductivity of the solution is greater than or equal to 4 mS/cm, wherein said addition occurs after the pH adjustment in step 1c, wherein said addition results in a slurry of SCP;

(e) optionally filtering and drying the SCP slurry; and

(f) optionally reacting the dried product from step e with a functional group and optionally wherein the resultant functionalized dried product is at least one of the following; a functionalized metal oxide-doped or metal sulfide-doped silica product.

2. A method of forming a silica-based product comprising:

(a) providing a silica containing precursor (SCP) contained in solution. that has a pH greater than 7;

(b) adjusting the pH of the solution to less than or equal to 7;

(c) doping the SCP with one or more metal species, wherein said doping occurs when the solution has a pH less than or equal to a pH of 7;

(d) adjusting the pH of the solution. to greater than 7;

(e)adding an effective amount of exogenous salt to the solution so that the conductivity of the solution is greater than or equal to 4 mS/cm, wherein said addition occurs after the pH adjustment in step 2d, wherein said addition results in a slurry of SCP;

(f) optionally filtering and drying the SCP; and

(g) optionally reacting the dried product from step f with a functional group and optionally wherein the resultant functionalized dried product is at least one of the following: a functionalized metal oxide-doped or metal sulfide-doped silica product.

3. The method of claim 1 , wherein the functional group in step f is an organosilane.

4. The method of claim 2 , wherein the functional group in step g is an organosilane.

5. The method of claim 1 , wherein the silicon-containing precursor is at least one of the following: a silicic acid, colloidal silica, tetraethylorthosilicate, and dispersed fumed silica.

6. The method of claim 2 , wherein the silicon-containing precursor is at least one of the following: silicic acid, colloidal silica, tetraethylorthosilicate, alkaline, silicates, and dispersed fumed silica.

7. The method of claim 2 , wherein the pH of the silicon-containing precursor is adjusted through the use of at least one of the following: carbonic acid, organic acids, mineral acidssuch that the. pH is decreased to a range of from to 2 to 7.

8. The method of claim 1 , wherein the pH range of the SCP in step 1(a) is from 3 to 4.

9. The method of claim 2 , wherein, the pH range of the SCP is adjusted to a range from3 to 4 with acetic acid.

10. The method of claim 1 , wherein the metal-doped SCP is heated to a temperature range of from 25° C. to 95 ° C.

11. The method of claim 1 , wherein the pH of the SCP is adjusted to a pH range from 7 to 11 with the use of a chemistry selected from at least one of the following: ammonium hydroxide, ammonium carbonate, mineral bases, organic bases, alkaline silicates, sulfide salts, organic dithiocarbamates, polymer-based dithiocarbamates, and polysulfide containing salts.

12. The method of claim 2 , wherein. the pH of the SCP is adjusted to a pH range from 7 to 11 with the use of a chemistry selected from at least one of the following: ammonium hydroxide, ammonium carbonate, mineral bases, organic bases, alkaline silicates, sulfide salts, organic dithiocarbamates, polymer-based dithiocarbamates, and polysulfide containing salts.

13. The method of claim 1 , wherein, the pH of the SCP is adjusted to greater than 7 by mixing said SCP with an alkaline solution at a shear rate of 6 to 23 m/s based on tip speed.

14. The method of claim 2 , wherein the pH of the SCP is adjusted to greater than 7 by mixing said SCP with an alkaline, solution at a shear rate of 6 to 23 m/s based on tip speed.

15. The method of claim 1 , wherein the resulting slurry from step d is filtered and dried such that the solid concentration of said dried and Filtered product is increased from about 5 wt % to about 99 wt %.

16. The method of claim 2 , wherein the resulting slurry from step e is filtered and dried such that the solid concentration of said dried and filtered product is increased from about 5 wt % to about 99 wt %.

17. The method of claim 1 , wherein the dried product from step e is surface treated with an organosilane via controlled hydrolysis and condensation of the silane to the silica surface in at least one of the following: organic solvent, supercritical solvent, and solvent-free process.

18. The method of claim 2 , wherein the dried product from step f is surface treated with an organosilane via controlled hydrolysis and condensation of the silane to the silica surface in at least one of the following: organic solvent, supercritical solvent, and solvent-free process.

19. The method of claim 1 , wherein the pH of the SCP is adjusted to greater than 7 by mixing said SCP with an alkaline solution via a mixing chamber; and optionally wherein the mixing chamber comprises a first conduit having one or more inlets and outlets; a second conduit having one or more inlets and outlets, wherein said first conduit secures to said second conduit and traverses said second conduit; a mixing chamber that has one or more inlets and outlets, wherein said second conduit secures to said mixing chamber and wherein said outlets of said first conduit and said outlets of said second conduit are in communication with said mixing chamber; and an adaptor that is in communication with said outlet of said mixing chamber and is secured to said mixing chamber; and said mixing chamber can then be attached or in communication with a receptacle that holds/processes a mixed product resulting from said pH adjustment of said SCP.

20. The method of claim 2 , wherein the pH of the SCP is adjusted to greater than 7 by mixing said SCP with an alkaline solution via a mixing chamber; and optionally wherein, the mixing chamber comprises a first conduit having one or more inlets and outlets; a second conduit having one or more inlets and outlets, wherein said first conduit secures to said second conduit and traverses said second conduit; a mixing chamber that has one or more inlets and outlets, wherein said second conduit secures to said mixing chamber and wherein said outlets of said first conduit and said outlets of said second conduit are in communication with said mixing chamber; and an adaptor that is in communication with said outlet of said mixing chamber and is secured to said mixing chamber; and said mixing chamber can then he attached or in communication with a receptacle that holds/processes a mixed product resulting from said pH adjustment of said SCP.