IP Library Granted Patent US 12,371,538
Granted Patent B2
US 12,371,538 · App. 17/626,910 · Granted Jul 29, 2025

Method of preparing polymer particles and polymer particles prepared thereby

Inventor: Viswanathan Kalyanaraman (Mt Vernon, IN)
Assignee: SHPP GLOBAL TECHNOLOGIES B.V.
C08J3/14C08J2300/12C08J2367/03C08J2369/00C08J2371/00C08J2371/10C08J2371/12C08J2381/04C08J2381/06
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Quick Facts
Patent No.
US 12,371,538
App. No.
17/626,910
Granted
Jul 29, 2025
Kind
B2
Abstract

Fine polymer particles are prepared by dissolving a polycarbonate, a poly(arylene ether), or a poly(arylene ether sulfone), each in a specific solvent, to form a slurry, heating the slurry to a temperature greater than the solvent boiling point to form a homogeneous solution, cooling the solution to form a dispersion of fine particles, and isolating the fine particles. A volume-based distribution of the isolated fine particles has a median equivalent spherical diameter less than or equal to 125 micrometers.

Claims (26)

1. A method of preparing polymer particles, the method comprising

combining a polymer and a solvent at a first temperature to provide a slurry, wherein the polymer is not soluble in the solvent at the first temperature, and wherein

the polymer is a poly(arylene ether) and the solvent is selected from the group consisting of acetone, methyl ethyl ketone, methyl n-butyl ketone, methyl iso-butyl ketone, di(iso-butyl) ketone, diacetone alcohol, cyclopentanone, cyclohexanone, anisole, and combinations thereof;

heating the slurry to a second temperature and at a pressure effective to dissolve the polymer in the solvent to provide a homogeneous solution, wherein the pressure is 7 to 2068 kilopascals;

cooling the homogeneous solution to a third temperature to provide a dispersion comprising a plurality of polymer particles; and

isolating the polymer particles from the dispersion;

wherein the isolated polymer particles have a Dv50 particle size of less than or equal to 125 micrometers, determined by laser diffraction according to ISO 13320:2020.

2. The method of claim 1 , wherein the polymer is the poly(arylene ether) and the solvent is selected from the group consisting of acetone, methyl ethyl ketone, methyl n-butyl ketone, methyl iso-butyl ketone, di(iso-butyl) ketone, diacetone alcohol, cyclopentanone, cyclohexanone, anisole, and combinations thereof.

3. The method of claim 1 , wherein

the first temperature is less than or equal to 100° C.;

the second temperature is at least 2° C. greater than the boiling point of the solvent;

the third temperature is less than or equal to 100° C.; or

a combination comprising at least two of the foregoing.

4. The method of claim 1 , wherein the polymer is the poly(arylene ether) and the solvent is selected from the group consisting of acetone, methyl ethyl ketone, methyl n-butyl ketone, methyl iso-butyl ketone, di(iso-butyl) ketone, diacetone alcohol, and combinations thereof.

5. The method of claim 1 , wherein the slurry has a solids content of 1 to 50 weight percent, based on a total weight of the slurry.

6. The method of claim 1 , wherein isolating the polymer powder comprises filtration.

7. The method of claim 1 , wherein the polymer is amorphous when it is combined with the solvent, and the isolated polymer particles comprise semi-crystalline polymer.

8. A method of preparing polymer particles, the method comprising

combining a polymer and a solvent at a first temperature to provide a slurry, wherein the polymer is not soluble in the solvent at the first temperature, wherein

the polymer is a poly(arylene ether) and the solvent is selected from the group consisting of methyl ethyl ketone, methyl isobutyl ketone, and combinations thereof,

wherein the first temperature is 15 to 50° C.; and wherein the polymer is present in the slurry at a concentration of 5 to 30 weight percent, based on a total weight of the slurry;

heating the slurry to a second temperature and at a pressure effective to dissolve the polymer in the solvent to provide a homogeneous solution, wherein the pressure is 107 to 1750 kilopascals; wherein the second temperature is at least 2° C. greater than the boiling point of the solvent, or at least 5° C. greater than the boiling point of the solvent, or at least 10° C. greater than the boiling point of the solvent;

cooling the homogeneous solution to a third temperature to provide a dispersion comprising a plurality of polymer particles; wherein the third temperature is 15 to 50° C.; and

isolating the polymer particles from the dispersion; wherein the isolating the polymer particles comprises filtration of the polymer particles; and

wherein the isolated polymer particles have a Dv50 particle size of 5 to 125 micrometers, determined by laser diffraction according to ISO 13320:2020.

9. Polymer particles prepared by the method of claim 1 , wherein the polymer particles comprise semi-crystalline polymer.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 7, 2022
From: SABIC GLOBAL TECHNOLOGIES B.V.
To: SHPP GLOBAL TECHNOLOGIES B.V.
Reel/Frame 059335/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 1, 2022
From: KALYANARAMAN, VISWANATHAN
To: SABIC GLOBAL TECHNOLOGIES B.V.
Reel/Frame 058918/0331 →
Priority Claims (1)
EP 19197564 · Sep 16, 2019 · regional
Continuity (1)
Related Publication 20220251309A1 · Aug 11, 2022
References Cited (30)
US 2071250A · Carothers · 1937 [cited by applicant]
US 2071251A · Carothers · 1937 [cited by applicant]
US 2130523A · Carothers · 1938 [cited by applicant]
US 2130948A · Carothers · 1938 [cited by applicant]
US 2241322A · Hanford · 1941 [cited by applicant]
US 2312966A · Hanford · 1943 [cited by applicant]
US 2512606A · Bolton et al. · 1950 [cited by applicant]
US 4012461A · Van Brederode · 1977 [cited by applicant]
US 4176222A · Cinderey et al. · 1979 [cited by applicant]
US 4970272A · Gallucci · 1990 [cited by applicant]
US 4975525A · Hostetler et al. · 1990 [cited by applicant]
US 5043112A · Beck · 1991 [cited by applicant]
US 6887930B2 · Uchida et al. · 2005 [cited by applicant]
US 20040054121A1 · Peemans · 2004 [cited by examiner]
US 20050113558A1 · Johnson et al. · 2005 [cited by applicant]
US 20060069236A1 · Brunelle et al. · 2006 [cited by applicant]
US 20060167216A1 · Johnson et al. · 2006 [cited by applicant]
US 20140100312A1 · Peters · 2014 [cited by examiner]
DE 102011103468A1 · 2012 [cited by examiner]
EP 0376653A2 · 1990 [cited by applicant]
EP 0411217A1 · 1991 [cited by applicant]
EP 2686368 · 2012 [cited by applicant]
EP 3341184 · 2017 [cited by applicant]
GB 962941 · 1964 [cited by applicant]
JP 2009173878A · 2009 [cited by applicant]
WO 2018080911A1 · 2018 [cited by applicant]
WO 2019040314A1 · 2019 [cited by applicant]
International Search Report mailed Dec. 23, 2020; International Application No. PCT/US2020/050635; International Filing Date Sep. 14, 2020 (6 pgs). [cited by applicant]
Kim, K-J, “Nano/micro spherical poly(Methyl methacrylate) particle formation by cooling from polymer solution” Powder Technology, Elsevier, Basel (CH), vol. 154, No. 2-3 (2005) (156-163). [cited by applicant]
Written Opinion mailed Dec. 23, 2020; International Application No. PCT/US2020/050635; International Filing Date Sep. 14, 2020 (10 pgs). [cited by applicant]