Method for preparing precipitated silica

Patent metadata

Field	Value
Publication number	US-9567230-B2
Application number	US-201013394320-A
Country	US
Kind code	B2
Filing date	Sep 2, 2010
Priority date	Sep 3, 2009
Publication date	Feb 14, 2017
Grant date	Feb 14, 2017

Abstract

The invention relates to a method for preparing precipitated silica, consisting in: (i) forming a starter having a pH of between 2 and 5; (ii) simultaneously adding silicate and acid, such that the pH of the reaction medium is between 2 and 5; (iii) adding silicate until the pH is between 7 and 10; (iv) simultaneously adding silicate and acid, such that the pH is between 7 and 10; (v) adding acid until the pH is between 2.5 and 5.3; (vi) bringing the reaction medium into contact with the acid and the silicate, such that the pH is between 2.5 and 5.3; and (vii) adding silicate, such as to increase the pH to a value between 4.7 and 6.3.

First claim

The invention claimed is:

1. A process for preparing precipitated silica, the process comprising reacting a silicate with an acidifying agent, obtaining a silica suspension, separating and drying the suspension, wherein reacting the silicate with the acidifying agent comprises:
(i) forming an aqueous feedstock with a pH of between 2 and 5,
(ii) adding silicate and an acidifying agent simultaneously to said feedstock to form a reaction medium, such that the pH of the reaction medium is maintained between 2 and 5,
(iii) stopping the addition of the acidifying agent while continuing the addition of silicate to the reaction medium until a pH value of between 7 and 10 is obtained,
(iv) adding silicate and acidifying agent simultaneously to the reaction medium, while maintaining the pH of the reaction medium between 7 and 10,
(v) stopping the addition of the silicate while continuing the addition of the acidifying agent to the reaction medium until a pH value of between 2.5 and 5.3 is obtained,
(vi) placing the reaction medium in contact with the acidifying agent and the silicate, while maintaining the pH of the reaction medium between 2.5 and 5.3,
(vii) adding an alkaline agent to the reaction medium obtained, so as to increase the pH of the reaction medium to a value of between 4.7 and 6.3, this step (vii) being optional in the case where, in step (vi), a reaction medium with a pH of between 5.0 and 5.3 is placed in contact with the acidifying agent and the silicate, such that the pH of the reaction medium is maintained between 5.0 and 5.3.

2. A process for preparing precipitated silica comprising reacting a silicate with an acidifying agent, obtaining a silica suspension, separating and drying the suspension, wherein reacting the silicate with the acidifying agent comprises:
(i) forming an aqueous feedstock with a pH of between 2 and 5,
(ii) adding silicate and acidifying agent simultaneously to said feedstock feedstock to form a reaction medium, such that the pH of the reaction medium is maintained between 2 and 5,
(iii) stopping the addition of the acidifying agent while continuing the addition of silicate to the reaction medium until a pH value of between 7 and 10 is obtained,
(iv) adding silicate and acidifying agent simultaneously to the reaction medium, while maintaining the pH of the reaction medium between 7 and 10,
(v) stopping the addition of the silicate while continuing the addition of the acidifying agent to the reaction medium until a pH value of between 2.5 and 5.3 is obtained,
(vi) placing the reaction medium in contact with the acidifying agent and the silicate, while maintaining the pH of the reaction medium between 2.5 and 5.3, and
(vii) adding an alkaline agent to the reaction medium obtained, so as to increase the pH of the reaction medium to a value of between 4.7 and 6.3.

3. The process as claimed in claim 1 , wherein step (i) comprises adjusting the pH of the feedstock to a pH value of between 2 and 5 by adding the acidifying agent to water.

4. The process as claimed in claim 1 , wherein all the steps are performed between 75° C. and 97° C.

5. The process as claimed in claim 1 , wherein, in step (vi), the acidifying agent is first added to said reaction medium, followed by the silicate.

6. The process as claimed in claim 1 , wherein, in step (vi), the acidifying agent and the silicate are added simultaneously to said reaction medium.

7. The process as claimed in claim 1 , wherein a maturation step is performed after step (vii).

8. The process as claimed in claim 1 , wherein step (vi) is performed in a rapid mixer or in a turbulent flow zone.

9. The process as claimed in claim 5 , wherein, in step (vi), the silicate and the medium resulting from the addition of the acidifying agent to the reaction medium are placed in contact in a rapid mixer or in a turbulent flow zone.

10. The process as claimed in claim 6 , wherein, in step (vi), the acidifying agent and the silicate are placed in contact with the reaction medium in a rapid mixer or in a turbulent flow zone.

11. The process as claimed in claim 8 , wherein the reaction medium obtained in step (vi), in the rapid mixer or in the turbulent flow zone is introduced into the reactor in which step (vii) is performed.

12. The process as claimed in claim 8 , wherein, in step (vi), the rapid mixer is selected from the group consisting of symmetrical T or Y mixers or tubes, asymmetric T or Y mixers or tubes, tangential jet mixers, Hartridge-Roughton mixers, vortex mixers and rotor-stator mixers.

13. The process as claimed in claim 8 , wherein, in step (vi), a tangential-jet, Hartridge-Roughton or vortex mixer is used.

14. The process as claimed in claim 1 , wherein drying is performed by atomization.

15. The process as claimed in claim 1 , wherein separating the suspension comprises filtration performed using a filter press or using a vacuum filter.

16. The process as claimed in claim 1 wherein said silica is formed from aggregates of primary particles (A) of silica at the surface of which are primary particles (B) of silica smaller in size than the primary particles (A), the silica having:
a CTAB specific surface area (S CTAB ) of between 60 and 400 m 2 /g,
a median size d50 of aggregates, measured by XDC granulometry after ultrasound deaggregation, such that:
d 50 (nm)>(6214/S CTAB (m 2 /g))+23,

a pore volume distribution such that:
V (d5-d50) /V (d5-d100) >0.906−(0.0013′S CTAB (m 2 /g)), and

a pore size distribution (diameters) such that:
Mode (nm)>(4166/S CTAB (m 2 /g))−9.2.

17. The preparation process as claimed in claim 16 , said precipitated silica having a parameter C, measured by small-angle X-ray scattering (SAXS), such that: C/S CTAB (m 2 /g)>0.001.

18. The preparation process as claimed in claim 16 , wherein said precipitated silica is in the form of substantially spherical beads.

Assignees

• Allain Emmanuelle
• Rhodia Operations

Inventors

• Allain Emmanuelle

Classifications

• C01B33/193 Primary

  of aqueous solutions of silicates · CPC title

• B01D37/00

  Processes of filtration (processes specially adapted for filtering gases B01D46/00) · CPC title

• B01J2/00

  Processes or devices for granulating materials {, e.g. fertilisers} in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic · CPC title

• B01J19/18

  Stationary reactors having moving elements inside (B01J19/08, B01J19/26 take precedence) · CPC title