Preparation of amorphous, precipitated silica and siliceous filler-reinforced microporous polymeric separator

• US 4,681,750 A
• Filed: 04/18/1986
• Issued: 07/21/1987
• Est. Priority Date: 07/29/1985
• Status: Expired due to Term

• Current Assignee: PPG Industries Incorporated (Nouryon BV)
• Original Assignee: PPG Industries Incorporated (Nouryon BV)
• Inventors: Longhini, David A., Krivak, Thomas G., Johnson, Harlan B.
• Primary Examiner(s): Skapars, Anthony
• Application Number:
  US06/853,506
• Time in Patent Office: 459 Days
• Field of Search: 429/252, 429/254, 429/249-251, 423/339, 423/335, 521/50, 521/62, 521/64, 106/287.34, 106/288 B
• US Class Current: 423/339
• CPC Class Codes: C01B 33/193 of aqueous solutions of silicates
• CPC Class Codes: C01P 2002/02 Amorphous compounds
• CPC Class Codes: C01P 2004/50 Agglomerated particles
• CPC Class Codes: C01P 2004/61 Micrometer sized, i.e. from 1-100 micrometer
• CPC Class Codes: C01P 2006/12 Surface area
• CPC Class Codes: C01P 2006/19 Oil-absorption capacity, e.g. DBP values
• CPC Class Codes: C01P 2006/82 water content
• CPC Class Codes: H01M 50/414 Synthetic resins, e.g. thermoplastics or thermosetting resins
• CPC Class Codes: H01M 50/429 Natural polymers
• CPC Class Codes: H01M 50/489 Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
• CPC Class Codes: Y02E 60/10 Energy storage using batteries

Abstract

Precipitated amorphous silica useful for manufacturing microporous battery separators is prepared by establishing an aqueous solution of alkali metal silicate having an alkali metal oxide concentration of (a) from 2.1-2.6 grams per liter and a temperature of from about 179° F. to 186° F., or (b) from 5.6 to 7.2 grams per liter and a temperature of from 190° to 198° F.; adding from (a) 14.5 to 19 times or (b) 2 to 5 times respectively the amount of alkali metal silicate initially present in the initial aqueous solution simultaneously with acidifying agent, e.g., sulfuric acid, to the initial aqueous solution while maintaining the initial alkali metal oxide concentration therein substantially constant; reducing the pH of the resulting slurry to from 8 to 9; ageing the slurry at precipitation temperatures for from 15 to 90 minutes; reducing the pH of the aged slurry to from 3.8 to 4.7 and then recovering, e.g., separating, the silica from its entraining slurry, washing the recovered silica, and drying the washed precipitated silica. Optionally, the recovered and dried silica is milled after drying to produce a product having a median agglomerate particle size of from 6 to 15 micrometers.

Claims

1. In a siliceous filler-reinforced microporous polymeric battery separator, the improvement wherein the siliceous filler comprises amorphous, precipitated silica prepared by the sequential steps of:

(a) establishing an agitated aqueous solution of alkali metal silicate having (1) an initial alkali metal oxide concentration of from about 2.1 to 2.6 grams per liter and a temperature of from about 179°

F. to 186°

F., or (2) an initial alkali metal oxide concentration of from about 5.6 to 7.2 grams per liter and a temperature of between about 190°

F. and about 198°

F.,

(b) adding slowly to the said aqueous solution further alkali metal silicate in amounts of (1) from about 14.5 to about 19 times, or (2) from about 2 to about 5 times, basis the aforesaid respective initial alkali metal oxide concentration, the amount of alkali metal silicate initially present in the aqueous solution while simultaneously adding acidifying agent to the said aqueous solution in amounts sufficient to maintain the alkali metal oxide concentration in the aqueous solution at substantially its initial level, thereby to form an aqueous slurry of precipitated silica,

(c) adding additional acidifying agent to the slurry of step (b) until the pH thereof is from about 8 to about 9,

(d) ageing the slurry of step (c) at (1) between about 176°

F. and 186°

F., or (2) between about 188°

F. and 198°

F., basis the aforesaid respective initial temperatures of the initial aqueous alkali metal silicate solution, for from about 15 to 90 minutes, and thereafter

(e) adding additional acidifying agent to the slurry of step (d) in amounts such that the final solid silica product has an essentially neutral pH.

2. The battery separator of claim 1 wherein the alkali metal silicate is sodium silicate.

3. The battery separator of claim 2 wherein the acidifying agent is selected from the group consisting of carbonic acid, hydrochloric acid and sulfuric acid.

4. The battery separator of claim 3 wherein the amount of additional acidifying agent added to the slurry of step (d) is sufficient to reduce the pH thereof to from about 3.8 to about 4.7.

5. The battery separator of claim 3 wherein the precipitated silica of step (e) is recovered from the slurry, washed to a residual alkali metal salt content of less than about 2.5 weight percent and dried.

6. The battery separator of claim 5 wherein the washed precipitated silica is dried by spray drying or rotary drying.

7. The battery separator of claim 6 wherein the dried silica is milled to produce a product having a median agglomerate particle size of between about 12 and about 16 micrometers.

31. The battery separator of claim 1 wherein between 20 and about 75 weight percent of the siliceous filler, basis the polymeric material, is used to prepare the separator.

32. The battery separator of claim 31 wherein the polymeric material is selected from natural rubber, styrene-butadiene rubber, nitrile-butadiene rubber, polyisoprene, high molecular weight polyethylene, polypropylene, polybutene, ethylene-propylene copolymers, polyvinyl chloride and vinyl chloride-vinyl acetate copolymers.

33. The battery separator of claim 32 wherein between about 30 and about 60 weight percent of the siliceous filler, basis the polymeric material, is used to prepare the separator.

8. In a siliceous filler-reinforced microporous polymeric battery separator, the improvement wherein the siliceous filler comprises amorphous, precipitated silica prepared by the sequential steps of:

(a) establishing an aqueous solution of alkali metal silicate having an initial alkali metal oxide concentration of from about 2.1 to 2.6 grams per liter and a temperature of between about 179°

F. and about 186°

F.,

(b) adding slowly to the said aqueous solution further alkali metal silicate in amounts of from about 14.5 to about 19 times the amount of alkali metal silicate initially present in the aqueous solution while simultaneously adding acidifying agent to the said aqueous solution in amounts sufficient to maintain the alkali metal oxide concentration in the aqueous solution at substantially its initial level, thereby to form an aqueous slurry of precipitated silica,

(c) adding additional acidifying agent to the slurry of step (b) until the pH thereof is from about 8 to about 9,

(d) ageing the slurry of step (c) at between about 176°

F, and 186°

F. for from about 15 to 90 minutes, and thereafter

(e) adding additional acidifying agent step (d) in amounts such that the final solid product has an essentially neutral pH.

9. The battery separator of claim 8 wherein the alkali metal silicate is sodium silicate.

10. The battery separator of claim 9 wherein the acidifying agent is selected from the group consisting of carbonic acid, hydrochloric acid and sulfuric acid.

11. The battery separator of claim 10 wherein the amount of additional acidifying agent added to the slurry of step (d) is sufficient to reduce the pH thereof to from about 3.8 to about 4.7.

12. The battery separator of claim 11 wherein the precipitated silica of step (e) is recovered from the slurry, washed to a residual alkali metal salt content of less than about 2.5 weight percent and dried.

13. The battery separator of claim 12 wherein the washed precipitated silica is dried by spray drying or rotary drying.

14. The battery separator of claim 9 wherein the initial alkali metal oxide concentration is between about 2.1 and 2.2 grams per liter, the temperature thereof is from about 182°

F. to about 183°

F., the amount of further alkali metal silicate added in step (b) is from about 15 to 17 times the amount of alkali metal silicate initially present in the aqueous solution, and the acidifying agent is sulfuric acid.

15. The battery separator of claim 14 wherein the precipitated silica is aged in step (d) for from about 30 to 60 minutes, the precipitated silica of step (e) is recovered and washed to a residual sulfate salt content of less than about 2.0 weight percent, and the washed silica dried

16. The battery separator of claim 15 wherein the washed silica is dried in a rotary furnace and milled to provide a product having a median agglomerate particle size of between about 12 and 15 micrometers.

17. In a siliceous filler-reinforced microporous polymeric battery separator, the improvement wherein the siliceous filler comprises amorphous, precipitated silica prepared by the sequential steps of:

(a) establishing an aqueous solution of alkali metal silicate having an initial alkali metal oxide concentration of from about 5.6 to 7.2 grams per liter and a temperature of between about 190°

F. and about 198°

F.,

(b) adding slowly to the said aqueous solution further alkali metal silicate in amounts of from about 2 to about 5 times the amount of alkali metal silicate initially present in the aqueous solution while simultaneously adding acidifying agent to the said aqueous solution in amounts sufficient to maintain the alkali metal oxide concentration in the aqueous solution at substantially its initial level, thereby to form an aqueous slurry of precipitated silica,

(c) adding additional acidifying agent to the slurry of step (b) until the pH thereof is from about 8 to about 9.

(d) ageing the slurry of step (c) at between about 188°

F. and 198°

F. for from about 15 to 90 minutes, and thereafter

(e) adding additional acidifying agent to the slurry of step (d) in amounts such that the final solid product has an essentially neutral pH.

18. The battery separator of claim 17 wherein the alkali metal silicate is sodium silicate.

19. The battery separator of claim 18 wherein the initial alkali metal oxide concentration is between about 5.6 and 6.3 grams per liter

20. The battery separator of claim 18 wherein the initial alkali metal oxide concentration is about 7.0 grams per liter.

21. The battery separator of claim 19 wherein the temperature of the aqueous alkali metal silicate solution of step (a) is about 195°

F.

22. The battery separator of claim 19 wherein the amount of further alkali metal silicate added in step (b) is from about 2 to 3 times the amount of alkali metal silicate initially present in the solution of step (a).

23. The battery separator of claim 18 wherein the acidifying agent is carbonic acid, hydrochloric acid or sulfuric acid.

24. The battery separator of claim 22 wherein the acidifying agent is carbonic acid, hydrochloric acid or sulfuric acid.

25. The battery separator of claim 24 wherein the amount of additional acidifying agent added to the slurry of step (d) is sufficient to reduce the pH thereof to from about 3.8 to 4.7.

26. The battery separator of claim 25 wherein the period of ageing of step (d) is from about 30 to 60 minutes.

27. The battery separator of claim 25 wherein the precipitated silica of step (e) is recovered from the slurry, washed to a residual alkali metal salt content of less than about 2.5 weight percent and dried.

28. The battery separator of claim 27 wherein the washed precipitated silica is dried by spray drying or rotary drying.

29. The battery separator of claim 27 wherein the washed precipitated silica is dried by spray drying and milled to produce a product having a median agglomerate particle size of between about 12 and about 16 micrometers.

30. The battery separator of claim 27 wherein the acidifying agent is sulfuric acid and the recovered precipitated silica is washed to a residual alkali metal sulfate salt content of less than about 2 weight percent.

34. Amorphous, precipitated silica prepared by the sequential steps of:

(a) establishing an agitated aqueous solution of alkali metal silicate having (1) an initial alkali metal oxide concentration of from about 2.1 to 2.6 grams per liter and a temperature of from about 179°

F. to 186°

F., or (2) an initial alkali metal oxide concentration of from about 5.6 to 7.2 grams per liter and a temperature of between about 190°

F. and about 198°

F.,

(b) adding slowly to the said aqueous solution further alkali metal silicate in amounts if (1) from about 14.5 to about 19 times, or (2) from about 2 to about 5 times, basis the aforesaid respective initial alkali metal oxide concentration, the amount of alkali metal silicate initially present in the aqueous solution while simultaneously adding acidifying agent to the said aqueous solution in amounts sufficient to maintain the alkali metal oxide concentration in the aqueous solution at substantially its initial level, thereby to form an aqueous slurry of precipitated silica,

(c) adding additional acidifying agent to the slurry of step (b) until the pH thereof is from about 8 to about 9,

(d) ageing the slurry of step (c) at (1) between about 176°

F. and 186°

F., or (2) between about 188°

F. and 198°

F., basis the aforesaid respective initial temperatures of the initial aqueous alkali metal silicate solution, for from about 15 to 90 minutes, and thereafter

(e) adding additional acidifying agent to the slurry of step (d) in amounts such that the final solid silica product has an essentially neutral pH.

35. The silica of claim 34 wherein the alkali metal silicate is sodium silicate.

36. The silica of claim 35 wherein the acidifying agent is selected from the group consisting of carbonic acid, hydrochloric acid and sulfuric acid.

37. The silica of claim 36 wherein the amount of additional acidifying agent added to the slurry of step (d) is sufficient to reduce the pH thereof to from about 3.8 to about 4.7.

38. The silica of claim 36 wherein the precipitated silica of step (e) is recovered from the slurry, washed to a residual alkali metal salt content of less than about 2.5 weight percent and dried.

39. The silica of claim 38 wherein the washed precipitated silica is dried by spray drying or rotary drying.

40. The silica of claim 39 wherein the dried silica is milled to produce a product having a median agglomerate particle size of between about 12 and about 16 micrometers.

41. Amorphous, precipitated silica prepared by the sequential steps of:

(a) establishing an aqueous solution of alkali metal silicate having an initial alkali metal oxide concentration of from about 2.1 to 2.6 grams per liter and a temperature of between about 179°

F. and about 186°

F.

(b) adding slowly to the said aqueous solution further alkali metal silicate in amounts of from about 14.5 to about 19 times the amount of alkali metal silicate initially present in the aqueous solution while simultaneously adding acidifying agent to the said aqueous solution in amounts sufficient to maintain the alkali metal oxide concentration in the aqueous solution at substantially its initial level, thereby to form an aqueous slurry of precipitated silica,

(c) adding additional acidifying agent to the slurry of step (b) until the pH thereof is from about 8 to about 9,

(d) ageing the slurry of step (c) at between about 176°

F. and 186°

F. for from about 15 to 90 minutes, and thereafter

(e) adding additional acidifying agent to the slurry of step (d) in amounts such that the final solid product has an essentially neutral pH.

42. The silica of claim 41 wherein the alkali metal silicate is sodium silicate.

43. The silica of claim 42 wherein the acidifying agent is selected from the group consisting of carbonic acid, hydrochloric acid and sulfuric acid.

44. The silica of claim 43 wherein the amount of additional acidifying agent added to the slurry of step (d) is sufficient to reduce the pH thereof to from about 3.8 to about 4.7.

45. The silica of claim 44 wherein the precipitated silica of step (e) is recovered from the slurry, washed to a residual alkali metal salt content of less than about 2.5 weight percent and dried.

46. The silica of claim 45 wherein the washed precipitated silica is dried by spray drying or rotary drying.

47. The silica of claim 42 wherein the initial alkali metal oxide concentration is between about 2.1 and 2.2 grams per liter, the temperature thereof is from about 182°

F. to about 183°

F., the amount of further alkali metal silicate added in step (b) is from about 15 to 17 times the amount of alkali metal silicate initially present in the aqueous solution, the acidifying agent is sulfuric acid, the precipitated silica is aged in step (d) for from about 30 to 60 minutes, the precipitated silica of step (e) is recovered and washed to a residual sulfate salt content of less than about 2.0 weight percent, and the washed silica dried in a rotary furnace and milled to provide a product having a median agglomerate particle size of between about 12 and 15 micrometers.

64. The silica of claim 44 wherein the acidifying agent is sulfuric acid and the precipitated silica of step (e) is recovered, washed to a residual alkali metal salt content of less than 2.5 weight percent and rotary dried.

48. Amorphous, precipitated silica prepared by the sequential steps of:

(a) establishing an aqueous solution of alkali metal silicate having an initial alkali metal oxide concentration of from about 5.6 to 7.2 grams per liter and a temperature of between about 190°

F. and about 198°

F.,

(b) adding slowly to the said aqueous solution further alkali metal silicate in amounts of from about 2 to about 5 times the amount of alkali metal silicate initially present in the aqueous solution while simultaneously adding acidifying agent to the said aqueous solution in amounts sufficient to maintain the alkali metal oxide concentration in the aqueous solution at substantially its initial level, thereby to form an aqueous slurry of precipitated silica,

(c) adding additional acidifying agent to the slurry of step (b) until the pH thereof is from about 8 to about 9

(d) ageing the slurry of step (c) at between about 188°

F. and 198°

F. for from about 15 to 90 minutes, and thereafter

(e) adding additional acidifying agent to the slurry of step (d) in amounts such that the final solid product has an essentially neutral pH.

49. The silica of claim 48 wherein the alkali metal silicate is sodium silicate.

50. The silica of claim 49 wherein the initial alkali metal oxide concentration is between about 5.6 and 6.3 grams per liter.

51. The silica of claim 49 wherein the initial alkali metal oxide concentration is about 7.0 grams per liter.

52. The silica of claim 50 wherein the temperture of the aqueous alkali metal silicate solution of step (a) is about 195°

F.

53. The silica of claim 50 wherein the amount of further alkali metal silicate added in step (b) is from about 2 to 3 times the amount of alkali metal silicate initially present in the solution of step (a).

54. The silica of claim 49 wherein the acidifying agent is carbonic acid, hydrochloric acid or sulfuric acid.

55. The silica of claim 53 wherein the acidifying agent is carbonic acid, hydrochloric acid or sulfuric acid.

56. The silica of claim 55 wherein the amount of additional acidifying agent added to the slurry of step (d) is sufficient to reduce the pH thereof to from about 3.8 to 4.7, and the period of ageing of step (d) is from about 30 to 60 minutes.

57. The silica of claim 56 wherein the precipitated silica of step (e) is recovered from the slurry, washed to a residual alkali metal salt content of less than about 2.5 weight percent and dried.

58. The silica of claim 57 wherein the washed precipitated silica is dried by spray drying or rotary drying.

59. The battery separator of claim 57 wherein the washed precipitated silica is dried by spray drying and milled to produce a product having a median agglomerate particle size of between about 12 and about 16 micrometers.

60. The silica of claim 54 wherein the precipitated silica of step (e) is recovered, washed to a residual alkali metal salt content of less than about 2.5 weight percent and spray dried.

61. The silica of claim 60 wherein the amount of additional acidifying agent added to the slurry of step (d) is sufficient to reduce the pH thereof to from about 3.8 to 4.7 and the acidifying agent is sulfuric acid.

62. The silica of claim 58 wherein the acidifying agent is carbonic acid, hydrochloric acid or sulfuric acid.

63. The silica of claim 62 wherein the acidifying agent is sulfuric acid and the precipitated silica of step (e) is recovered, washed to a residual alkali metal salt content of less than 2.5 weight percent and spray dried.