IP Library Granted Patent US 9,181,395
Granted Patent B2
US 9,181,395 · App. 13/841,802 · Granted Nov 10, 2015

Optimized emulsion drying process for making micronized polyetherimide polymers

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Quick Facts
Patent No.
US 9,181,395
App. No.
13/841,802
Granted
Nov 10, 2015
Kind
B2
Abstract

A process for making ultra-fine particles of a high performance polymer in a yield greater than 90%, which includes dissolving the high performance polymer in an organic solvent capable of dissolving the polymer to form a solution; emulsifying the solution by combining the solution with water and a surfactant to form an emulsion; transferring the emulsion into a receiving water containing a surfactant to remove the organic solvent and form a slurry; and recovering particles of less than 75 microns in diameter in a yield greater than 90%.

Claims (43)

1. A process for the manufacture of ultra-fine particles of a high performance polymer in a yield greater than 90%, comprising:

a. dissolving the high performance polymer in an organic solvent capable of dissolving the polymer to form a solution;

b. emulsifying the solution by combining the solution with water and a surfactant to form an emulsion;

c. transferring the emulsion into a receiving water containing a surfactant to remove the organic solvent and form a slurry; and,

d. recovering particles of <75-micron diameter in a yield greater than 90%;

wherein the high performance polymer is a polyetherimide.

2. The process according to claim 1 , further comprising heating the emulsion up to or below the boiling point of the emulsion before transferring the emulsion into the receiving water.

3. The process according to claim 1 , further comprising heating the emulsion above the boiling point of the emulsion before transferring the emulsion into the receiving water.

4. The process according to claim 1 , farther comprising transferring the emulsion drop wise into the receiving water.

5. The process according to claim 1 , further comprising transferring the emulsion through a nozzle into the receiving water.

6. The process according to claim 1 , further comprising transferring the emulsion through a tube into the receiving water.

7. The process according to claim 1 , wherein the receiving water is de ionized.

8. The process according to claim 1 , further comprising matching the amount of surfactant in the receiving water to the amount of the surfactant in the emulsion.

9. The process according to claim 8 , wherein the step of matching raises the yield of particles above 98%.

10. The process according to claim 1 , wherein the solvent is a member selected from the group of methylene chloride, chloroform, and combinations thereof.

11. The process according to claim 1 , wherein the solvent has a boiling point that is less than 100 C and the solvent is immiscible with water.

12. The process according to claim 1 , further comprising agitating the solution of step b. to form the emulsion.

13. The process according to claim 1 , further comprising agitating the solution of step b. using a high shear mixer to form the emulsion.

14. The process according to claim 1 , further comprising adding a defoaming agent in step c.

15. The process of claim 1 , further comprising recovering particles in a yield from about 94% to about 99%.

16. The process of claim 1 , wherein the surfactant is anionic surfactant.

17. The process of claim 1 , wherein the surfactant is a surfactant selected from the group of sodium dodecyl benzene sulfonate (SDBS), sodium lauryl sulfate, and combinations thereof.

18. The process according to claim 1 , further comprising filtering the slurry to form a wet cake.

19. The process according to claim 1 , further comprising a course pre-filtering of the slurry to remove any macro particles or contaminates.

20. The process according to claim 18 , further comprising washing or re-slurrying the wet cake with de-ionized water.

21. The process according to claim 20 , further comprising drying the wet cake under heat and vacuum.

22. A process of forming ultra-fine particles of a polyetherimide (PET) polymer in a yield greater than 90% comprising:

a. dissolving a polyetherimide (PEI) polymer in a solvent to form a solution, wherein the polyetherimide is soluble in the solvent, the solvent has a boiling point that is less than 100 C and the solvent is immiscible with water;

b. emulsifying the solution by combining the solution with de-ionized water and a surfactant under agitation conditions sufficient to form an emulsion;

c. transferring the emulsion into a de-ionized receiving water, the receiving water also containing a surfactant and removing the solvent and form a slurry;

d pre-filtering the slurry to remove any macro particles or contaminates

e. filtering the slurry to form a wet cake;

f. washing or re-slurrying the wet cake with de-ionized water;

g. drying the washed wet cake under heat and vacuum; and,

h. recovering particles of polyetherimide (PET) of <75-micron diameter in a yield from about 94% to about 99%.

23. The process of claim 22 , wherein the solvent is methylene chloride.

24. The process according to claim 22 , further comprising combining a de-foaming agent in step c.

25. The process according to claim 22 , further comprising matching the amount of surfactant in the receiving water to the amount of the surfactant in the emulsion.

26. The process according to claim 25 , wherein the surfactant is sodium dodecyl benzene sulfonate (SDBS) or sodium dodecyl sulfate (SLS).

27. The process of claim 1 , wherein the high performance polymer comprises (a) a polyetherimide resin, and (b) a phosphorus-containing stabilizer, in an amount that is effective to increase the melt stability of the polyetherimide resin, wherein the phosphorus-containing stabilizer exhibits a low volatility such that, as measured by thermogravimetric analysis of an initial amount of a sample of the phosphorus-containing stabilizer, greater than or equal to 10 percent by weight of the initial amount of the sample remains unevaporated upon heating of the sample from room temperature to 300° C. at a heating rate of a 20° C. per minute under an inert atmosphere.

28. The process of claim 27 , wherein the phosphorous-containing stabilizer has a formula P—R′ a , where R′ is independently H, alkyl, alkoxy, aryl, aryl oxy, or oxy substituent and a is 3 or 4.

29. The process of claim 22 , wherein the polyetherimide polymer comprises (a) a polyetherimide resin, and (b) a phosphorus-containing stabilizer, in an amount that is effective to increase the melt stability of the polyetherimide resin, wherein the phosphorus-containing stabilizer exhibits a low volatility such that, as measured by thermogravimetric analysis of an initial amount of a sample of the phosphorus-containing stabilizer, greater than or equal to 10 percent by weight of the initial amount of the sample remains unevaporated upon heating of the sample from room temperature to 300° C. at a heating rate of a 20° C. per minute under an inert atmosphere.

30. The method of claim 29 , wherein the phosphorous-containing stabilizer has a formula P—R′ a , where R′ is independently H, alkyl, alkoxy, aryl, aryloxy, or oxy substituent and a is 3 or 4.

Assignments (6)
CORRECTIVE ASSIGNMENT TO CORRECT THE REMOVE THE APPLICATION NUMBER 15039474 PREVIOUSLY RECORDED AT REEL: 054528 FRAME: 0467. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Mar 23, 2021
From: SABIC GLOBAL TECHNOLOGIES B.V.
To: SHPP GLOBAL TECHNOLOGIES B.V.
Reel/Frame 057453/0680 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 26, 2020
From: SABIC GLOBAL TECHNOLOGIES B.V.
To: SHPP GLOBAL TECHNOLOGIES B.V.
Reel/Frame 054528/0467 →
CORRECTIVE ASSIGNMENT TO CORRECT THE 12/116841, 12/123274, 12/345155, 13/177651, 13/234682, 13/259855, 13/355684, 13/904372, 13/956615, 14/146802, 62/011336 PREVIOUSLY RECORDED ON REEL 033591 FRAME 0673. ASSIGNOR(S) HEREBY CONFIRMS THE CHANGE OF NAME. Recorded Aug 29, 2014
From: SABIC INNOVATIVE PLASTICS IP B.V.
To: SABIC GLOBAL TECHNOLOGIES B.V.
Reel/Frame 033663/0427 →
CORRECTIVE ASSIGNMENT TO CORRECT REMOVE 10 APPL. NUMBERS PREVIOUSLY RECORDED AT REEL: 033591 FRAME: 0673. ASSIGNOR(S) HEREBY CONFIRMS THE CHANGE OF NAME. Recorded Aug 28, 2014
From: SABIC INNOVATIVE PLASTICS IP B.V.
To: SABIC GLOBAL TECHNOLOGIES B.V.
Reel/Frame 033649/0529 →
CHANGE OF NAME Recorded Aug 22, 2014
From: SABIC INNOVATIVE PLASTICS IP B.V.
To: SABIC GLOBAL TECHNOLOGIES B.V.
Reel/Frame 033591/0673 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 21, 2013
From: KALAYARAMAN, VISWANATHAN; OWENS, DONALD E., III; JOHNSON, NORMAN; STELLA, ALBERT; WOODRUFF, DAVID; HOWSON, PAUL
To: SABIC INNOVATIVE PLASTICS IP B.V.
Reel/Frame 031441/0564 →