Methods of making an elastomer composite reinforced with silica and products containing same

Patent metadata

Field	Value
Publication number	US-10301439-B2
Application number	US-201815935505-A
Country	US
Kind code	B2
Filing date	Mar 26, 2018
Priority date	Jul 15, 2015
Publication date	May 28, 2019
Grant date	May 28, 2019

Abstract

Methods to make a silica elastomer composite with a destabilized dispersion of a never-dried, or as-produced, precipitated silica are described, along with silica elastomer composites made from the methods. The advantages achieved with the methods are further described.

First claim

What is claimed is:

1. A method of producing a silica elastomer composite, comprising:
(a) providing a continuous flow under pressure of at least a first fluid comprising a destabilized dispersion of silica in particulate form, and having a wt % of silica of from about 6 wt % to 35 wt % based on the weight of the first fluid, wherein said silica has been obtained without drying said silica to a solids content greater than 40%, by weight; and
(b) providing a continuous flow of at least a second fluid comprising elastomer latex;
(c) providing volumetric flow of the first fluid relative to that of the second fluid to yield a silica content of about 15 phr to about 180 phr in the silica elastomer composite;
(d) combining the first fluid flow and the second fluid flow with a sufficiently energetic impact to distribute the silica within the elastomer latex to obtain a flow of a solid silica-containing continuous rubber phase or semi-solid silica-containing continuous rubber phase, wherein said flow of said solid or semi-solid silica-containing rubber phase forms in two seconds or less after combining said first fluid flow and second fluid flow; and
(e) recovering said solid or semi-solid silica-containing continuous rubber phase that is the silica elastomer composite.

2. The method of claim 1 , further comprising before step 1(a):
(a) acidifying a solution of silicate to obtain an aqueous slurry of precipitated silica; and
(b) filtering said aqueous slurry of precipitated silica to obtain precipitated silica in the form of a filter cake that has a water content of from about 60 wt % to about 90 wt % based on the weight of the filter cake,
further comprising mechanically processing said filter cake, whereby silica particle agglomeration, filter cake viscosity, or a combination thereof, is reduced.

3. The method of claim 2 , further comprising adjusting acidity of the aqueous slurry of precipitated silica.

4. The method of claim 1 , further comprising, before step 1(a):
(a) acidifying a solution of silicate to obtain an aqueous slurry of precipitated silica having an initial ionic concentration; and
(b) adjusting the initial ionic concentration of the aqueous slurry of precipitated silica to yield a destabilized dispersion of the precipitated silica having an ionic concentration of about 10 mM to about 160 mM,
wherein said adjusting comprises filtering said aqueous slurry of precipitated silica to obtain precipitated silica in the form of a filter cake, washing the filter cake with an aqueous medium and adjusting filter cake solids content and ionic concentration to yield the first fluid.

5. The method of claim 4 , wherein said filter cake has a silica particle agglomeration and a filter cake viscosity, and said method further comprising mechanically processing said filter cake, whereby said silica particle agglomeration, or said filter cake viscosity, or a combination thereof, is reduced.

6. The method of claim 1 , wherein said destabilized dispersion of silica in particulate form is a destabilized dispersion of silica coated carbon black.

7. The method of claim 1 , further comprising before step 1(a):
(a) adding an aqueous silicate solution to an aqueous slurry of carbon black particles to form a reaction mixture;
(b) adjusting the reaction mixture pH to deposit silica onto the carbon black particles and yield an aqueous slurry of silica coated carbon black particles having an initial ionic concentration; and
(c) without drying the reaction mixture to a solids content of greater than 40 wt %, adjusting the aqueous slurry of the silica coated carbon black particles to a solids content of from about 6 wt % to about 35 wt %,
further comprising adjusting the initial ionic concentration of the aqueous slurry of the silica coated carbon black particles to yield a destabilized dispersion of silica coated carbon black particles having an ionic concentration of about 10 mM to about 160 mM.

8. A method for making a rubber compound comprising
(a) conducting the method of claim 1 , and
(b) blending the silica elastomer composite with other components to form the rubber compound, wherein said other components comprise at least one antioxidant.

9. The method of claim 8 , wherein at least one antioxidant has a lower affinity to silica than 6PPD antioxidant.

10. The method of claim 8 , wherein said antioxidant comprises polymerized 2,2,4-trimethyl 1-1,2 dihydroquinoline or 2,6-di-t-butyl-4-methylphenol, 6PPD antioxidant, or a combination thereof.

11. The method of claim 1 , wherein said destabilized dispersion of silica in particulate form is a destabilized dispersion of silica that is chemically treated with at least one silane.

12. The method of claim 11 , wherein said silica is silane-treated prior to carrying out step 1(a).

13. The method of claim 1 , wherein the silica is precipitated silica.

14. The method of claim 1 , wherein said silica has a BET surface area of about 20 m 2 /g to about 450 m 2 /g.

15. The method of claim 1 , wherein said flow of said solid or semi-solid silica-containing continuous rubber phase forms in about 50 milliseconds to about 1500 milliseconds after combining said first fluid flow and second fluid flow.

16. The method of claim 1 , wherein the volumetric flow of said first fluid and of said second fluid are at a volumetric flow ratio of first fluid to second fluid of from 0.2:1 to 2.8:1.

17. The method of claim 1 , wherein the volumetric flow of said first fluid and of said second fluid are at a volumetric flow ratio of first fluid to second fluid of from 0.4:1 to 3.2:1, and said destabilized dispersion of silica includes at least one salt.

18. The method of claim 1 , wherein the volumetric flow of said first fluid and of said second fluid are at a volumetric flow ratio of first fluid to second fluid of from 0.2:1 to 2.8:1, and said destabilized dispersion of silica includes at least one acid.

19. The method of claim 1 , wherein said elastomer latex comprises a base, said destabilized dispersion of silica comprises at least one acid, and a molar ratio of hydrogen ions in said acid in said first fluid to said base in said second fluid is at least 1.0.

20. The method of claim 1 , wherein said elastomer latex comprises a base, said destabilized dispersion of silica comprises at least one acid, and a molar ratio of hydrogen ions in said acid in said first fluid to said base in said second fluid is from 1 to 4.5.

21. The method of claim 1 , wherein said destabilized dispersion of silica includes at least one salt, wherein said salt is present in said destabilized dispersion in an amount of from about 0.2 wt % to about 2 wt % based on weight of said destabilized dispersion.

22. The method of claim 1 , wherein said destabilized dispersion of silica includes at least one acid, wherein said acid is present in said destabilized dispersion in an amount of from about 0.8 wt % to about 7.5 wt % based on weight of said destabilized dispersion.

23. The method of claim 1 , wherein step (c) is carried out in a semi-confined reaction zone and the first fluid has a velocity sufficient to induce cavitation in the reaction zone upon combining with the second fluid.

24. The method of claim 23 , wherein the second fluid has a velocity sufficient to create turbulent flow.

25. The method of claim 1 , wherein said first fluid comprises an aqueous fluid.

26. The method of claim 25 , wherein said f

Assignees

• Cabot Corp

Inventors

• Xiong Jincheng
• Green Martin C
• Williams William R
• Fomitchev Dmitry
• Adler Gerald D
• Mcdonald Duane G
• Grosz Ron
• Morris Michael D

Classifications

• C08J3/16

  by coagulating dispersions {(C08J3/122 takes precedence)} · CPC title

• C08K3/04 Primary

  Carbon · CPC title

• C08L7/02

  Latex · CPC title

• C08K3/36

  Silica · CPC title

• C08K9/02

  Ingredients treated with inorganic substances · CPC title