Aromatic polysulfone
US-2018057636-A1 · Mar 1, 2018 · US
US11230628B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11230628-B2 |
| Application number | US-201716475584-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 25, 2017 |
| Priority date | Jan 6, 2017 |
| Publication date | Jan 25, 2022 |
| Grant date | Jan 25, 2022 |
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A resin microparticle production method includes a step of pulverizing resin particles having a thermoplastic resin as a forming material and having a BET specific surface area of equal to or more than 5 m2/g using an impact type pulverizer.
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The invention claimed is: 1. A resin microparticle production method, comprising: a step of pulverizing resin particles which are a thermoplastic resin of an aromatic polyether sulfone having a BET specific surface area of equal to or more than 5 m 2 /g using an impact type pulverizer; wherein a median particle diameter D 50 of the resin particles is equal to or more than 200 and wherein a median particle diameter D 50 of the resin microparticle is equal to or less than 100 μm. 2. The resin microparticle production method according to claim 1 , further comprising: a step of synthesizing the thermoplastic resin by polymerizing a monomer in a solvent; a step of precipitating the thermoplastic resin from a reaction mixture obtained in the synthesizing step to obtain intermediate particles containing the thermoplastic resin; and a step of washing the obtained intermediate particles in a fixed phase to obtain the resin particles, prior to the pulverizing step. 3. The resin microparticle production method according to claim 1 , wherein the thermoplastic resin has a sulfonyl group in the main chain. 4. The resin microparticle production method according to claim 3 , wherein the thermoplastic resin is aromatic polyether sulfone. 5. The resin microparticle production method according to claim 1 , wherein a reduced viscosity (Rv) of the thermoplastic resin is equal to or less than 0.36 dL/g. 6. The resin microparticle production method according to claim 2 , wherein the thermoplastic resin has an aromatic group in a main chain. 7. The resin microparticle production method according to claim 6 , wherein the thermoplastic resin has a sulfonyl group in the main chain. 8. The resin microparticle production method according to claim 2 , wherein a reduced viscosity (Rv) of the thermoplastic resin is equal to or less than 0.36 dL/g. 9. The resin microparticle production method according to claim 1 , wherein a reduced viscosity (Rv) of the thermoplastic resin is equal to or less than 0.36 dL/g. 10. The resin microparticle production method according to claim 3 , wherein a reduced viscosity (Rv) of the thermoplastic resin is equal to or less than 0.36 dL/g. 11. The resin microparticle production method according to claim 4 , wherein a reduced viscosity (Rv) of the thermoplastic resin is equal to or less than 0.36 dL/g. 12. The resin microparticle production method according to claim 1 , wherein the aromatic polyether sulfone has general formula (E) as a constituent unit, wherein Y represents —SO 2 —, Z represents a single bond, an alkylidene group having 1 to 10 carbon atoms, —SO 2 —, or —CO—, R 1 , R 2 , R 3 and R 4 each independently represents an alkyl group having 1 to 4 carbon atoms or an alkoxy group having 1 to 4 carbon atoms, and n 1 , n 2 , n 3 , and n 4 each independently represents an integer of 0 to 4, and when n 1 , n 2 , n 3 , or n 4 is an integer of 2 to 4, a plurality of R 1 , R 2 , R 3 or R 4 may be the same or different from one another.
Powdering or granulating · CPC title
the non-solvent being aqueous · CPC title
Polyethersulfones · CPC title
Post-polymerisation treatment · CPC title
by dividing preformed material, e.g. sheets, rods · CPC title
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