Hydrophilic precipitated silica for defoamer formulations

1. A precipitated silica having

BET

100-190 m 2 /g,

Modified Sears number

8-20 ml/(5 g),

Sears number/BET ratio

<0.12 ml/(5 m 2 ), and

pH

>8.

2. The precipitated silica as claimed in claim 1 , having a BET surface area of 120-190 m 2 /g.

3. The precipitated silica as claimed in claim 1 , having a CTAB surface area of 100-190 m 2 /g.

4. The precipitated silica as claimed in claim 1 , having a BET/CTAB ratio of 0.8-1.2.

5. The precipitated silica as claimed in claim 1 , having a DBP<300 g/(100 g).

6. The precipitated silica as claimed in claim 1 , having a mean particle size d 50 of less than 14 μm.

7. The precipitated silica as claimed in claim 1 , having an average tapped density of less than 150 g/l.

8. The precipitated silica as claimed in claim 1 , having a loss on ignition of 2-6%.

9. A defoamer formulation comprising the precipitated silica as claimed in claim 1 .

10. A silicone rubber comprising the precipitated silica as claimed in claim 1 .

11. A HTV silicon rubber comprising a lightening additive comprising the silica as claimed in claim 1 .

12. A flow assistant comprising the precipitated silica as claimed in claim 1 .

13. A carrier comprising the precipitated silica as claimed in claim 1 .

14. An antiblocking agent comprising the precipitated silica as claimed in claim 1 .

15. The precipitated silica as claimed in claim 1 , having a loss on ignition ranging from 2 to 4%.

16. A process for preparing a precipitated silica, comprising:

a) precipitating a silicate solution to form a precipitated silica,

b) filtering the precipitated silicate solution to form a filtercake of the precipitated silica,

c) liquefying the filtercake by adding water to form a suspension of the precipitated silica,

d) drying the suspension,

f) milling the precipitated silica,

wherein the process further comprises

e) alkalifying the precipitated silica by adding at least one basic agent thereto wherein the resulting precipitated silica has the following characteristics: BET 100-190 m 2 /g, Modified Sears number 8-20 ml/(5 g), Sears number/BET ratio<0.12 ml/(5 m2), and pH>8.

17. The process as claimed in claim 16 , wherein the alkalifying is carried out simultaneously with the liquefying of the filtercake.

18. The process as claimed in claim 16 , wherein the alkalifying is carried out after the liquefying of the filtercake but before the drying of the filtercake.

19. The process as claimed in claim 16 , wherein the alkalifying is carried out after the drying of the filtercake.

20. The process as claimed in claim 16 , wherein the alkalifying is carried out before and after the drying of the filtercake.

21. The process as claimed in claim 16 , wherein the alkalifying step adjusts the pH of the precipitated silica or of the suspension from 7 to 11 by addition of a basic component.

22. The process as claimed in claim 16 , wherein the basic agent is at least one member selected from the group consisting of an alkali metal hydroxide, an alkali metal carbonate, an alkaline earth metal hydroxide, an alkaline earth metal carbonate, an alkali metal oxide, an alkaline earth metal oxide, an alkali metal silicate, an alkaline earth metal silicate, ammonia, an alkali metal aluminate, an aqueous solution thereof and a mixture thereof.

23. A precipitated silica prepared by the process as claimed in claim 16 .

24. The process as claimed in claim 16 , wherein the precipitating comprises:

aa) heating an initial charge of water, or a mixture of water and a silicate, to a temperature ranging from 60 to 100° C.,

ab) simultaneously adding the silicate solution and acid to the initial charge, and

ac) lowering the pH by adding an acidifier to the charge.

25. The process as claimed in claim 24 , wherein the pH in ab) is held at a level ranging from 7 to 11.

26. The process as claimed in claim 24 , wherein the temperature of the reaction solution in ab) is held at a level ranging from 60 to 100° C.

27. The process as claimed in claim 24 , wherein the simultaneous addition of waterglass and acidifier is continued to a solids content of 40 to 70 g/l and then stopped.

28. The process as claimed in claim 24 , further comprising:

adjusting the pH to 2 to 8 in ac) by adding an acidifier.

29. The process as claimed in claim 24 , wherein the heating in aa) is carried out at a temperature ranging from 70° C. to 90° C.

30. The process as claimed in claim 24 , further comprising, after the lowering of the pH:

ad) aging the suspension at 10 to 95° C. for 0 to 72 hours.

31. The process as claimed in claim 30 , wherein the aging in ad) is carried out at a temperature ranging from 40-60° C. for a time ranging from 0-12 hours.