Optical film, polarizing plate, and image display device
US-10459290-B2 · Oct 29, 2019 · US
US12435187B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12435187-B2 |
| Application number | US-202117411663-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 25, 2021 |
| Priority date | Mar 26, 2021 |
| Publication date | Oct 7, 2025 |
| Grant date | Oct 7, 2025 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A method for producing a resin particle dispersion includes: obtaining a phase-inverted emulsion by adding a neutralizer to a resin solution prepared by dissolving a resin having an acid value in an organic solvent to thereby neutralize the resin and then adding an aqueous medium to the resulting resin solution to subject the resin to phase inversion emulsification; and removing the organic solvent from the phase-inverted emulsion. In the course of obtaining the phase-inverted emulsion, a maximum agitation power per unit mass (kg) of the resin when the resin solution containing the aqueous medium added thereto is agitated to perform the phase inversion emulsification is from 0.4 W to 20 W inclusive.
Opening claim text (preview).
What is claimed is: 1. A method for producing a resin particle dispersion, the method comprising: obtaining a phase-inverted emulsion by adding a neutralizer to a resin solution prepared by dissolving a resin having an acid value in an organic solvent to thereby neutralize the resin and then adding an aqueous medium to the resulting resin solution to subject the resin to phase inversion emulsification; and removing the organic solvent from the phase-inverted emulsion, wherein, in the course of obtaining the phase-inverted emulsion, a maximum agitation power per unit mass (kg) of the resin when the resin solution containing the aqueous medium added thereto is agitated to perform the phase inversion emulsification is from 0.4 W to 20 W inclusive. 2. The method for producing a resin particle dispersion according to claim 1 , wherein the resin has an acid value of from 8 mg KOH/g to 20 mg KOH/g inclusive. 3. The method for producing a resin particle dispersion according to claim 1 , wherein the resin is a polyester resin. 4. The method for producing a resin particle dispersion according to claim 2 , wherein the resin is a polyester resin. 5. The method for producing a resin particle dispersion according to claim 1 , wherein the organic solvent contains at least one selected from ketones and at least one selected from alcohols, wherein the amount of the at least one selected from ketones relative to 10 parts by mass of the resin is from 4 parts by mass to 15 parts by mass inclusive, and wherein the amount of the at least one selected from alcohols relative to 10 parts by mass of the resin is from 1 part by mass to 5 parts by mass inclusive. 6. The method for producing a resin particle dispersion according to claim 2 , wherein the organic solvent contains at least one selected from ketones and at least one selected from alcohols, wherein the amount of the at least one selected from ketones relative to 10 parts by mass of the resin is from 4 parts by mass to 15 parts by mass inclusive, and wherein the amount of the at least one selected from alcohols relative to 10 parts by mass of the resin is from 1 part by mass to 5 parts by mass inclusive. 7. The method for producing a resin particle dispersion according to claim 3 , wherein the organic solvent contains at least one selected from ketones and at least one selected from alcohols, wherein the amount of the at least one selected from ketones relative to 10 parts by mass of the resin is from 4 parts by mass to 15 parts by mass inclusive, and wherein the amount of the at least one selected from alcohols relative to 10 parts by mass of the resin is from 1 part by mass to 5 parts by mass inclusive. 8. The method for producing a resin particle dispersion according to claim 4 , wherein the organic solvent contains at least one selected from ketones and at least one selected from alcohols, wherein the amount of the at least one selected from ketones relative to 10 parts by mass of the resin is from 4 parts by mass to 15 parts by mass inclusive, and wherein the amount of the at least one selected from alcohols relative to 10 parts by mass of the resin is from 1 part by mass to 5 parts by mass inclusive. 9. The method for producing a resin particle dispersion according to claim 5 , wherein the at least one selected from ketones is methyl ethyl ketone, and the at least one selected from alcohols is isopropanol. 10. The method for producing a resin particle dispersion according to claim 6 , wherein the at least one selected from ketones is methyl ethyl ketone, and the at least one selected from alcohols is isopropanol. 11. The method for producing a resin particle dispersion according to claim 7 , wherein the at least one selected from ketones is methyl ethyl ketone, and the at least one selected from alcohols is isopropanol. 12. The method for producing a resin particle dispersion according to claim 8 , wherein the at least one selected from ketones is methyl ethyl ketone, and the at least one selected from alcohols is isopropanol. 13. The method for producing a resin particle dispersion according to claim 1 , wherein the neutralizer is ammonia, and wherein the total amount of the neutralizer added relative to 10 parts by mass of the resin is from 0.02 parts by mass to 0.06 parts by mass inclusive. 14. The method for producing a resin particle dispersion according to claim 2 , wherein the neutralizer is ammonia, and wherein the total amount of the neutralizer added relative to 10 parts by mass of the resin is from 0.02 parts by mass to 0.06 parts by mass inclusive. 15. The method for producing a resin particle dispersion according to claim 1 , wherein the temperature of the resin solution containing the aqueous medium added thereto during the phase inversion emulsification is from 20° C. to 80° C. inclusive. 16. The method for producing a resin particle dispersion according to claim 1 , wherein the aqueous medium is continuously added to the resin solution, and wherein the rate of addition of the aqueous medium to 10 parts by mass of the resin is from 0.03 parts by mass/min to 0.80 parts by mass/min inclusive. 17. The method for producing a resin particle dispersion according to claim 1 , wherein the phase inversion emulsification of the resin is performed using an emulsification tank equipped with an anchor mixing impeller, wherein the ratio Di/Dt of an impeller diameter Di of the anchor mixing impeller to a tank diameter Dt of the emulsification tank is from 0.90 to 0.99 inclusive, and wherein the number of rotations of the anchor mixing impeller is from 10 rpm to 100 rpm inclusive. 18. The method for producing a resin particle dispersion according to claim 1 , wherein a resin particle dispersion for a toner is produced. 19. A method for producing a toner for electrostatic image development, the method comprising: forming aggregated particles by aggregating, in a dispersion containing resin particles in a resin particle dispersion obtained by the resin particle dispersion production method according to claim 1 , at least the resin particles; and fusing and coalescing the aggregated particles by heating an aggregated particle dispersion containing the aggregated particles dispersed therein to thereby form toner particles. 20. A toner for electrostatic image development comprising toner particles obtained by the method for producing a toner for electrostatic image development according to claim 19 .
Emulsions including solid particles, e.g. as solution or dispersion, i.e. molten material or material dissolved in a solvent or dispersed in a liquid · CPC title
Inversed-type emulsions · CPC title
characterised by the nature of the liquids (B01F23/47 takes precedence) · CPC title
Mixing systems, i.e. flow charts or diagrams · CPC title
using driven stirrers · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.