Curable unsaturated crystalline polyester powder and methods of making the same

US10655025B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10655025-B2
Application numberUS-201815982689-A
CountryUS
Kind codeB2
Filing dateMay 17, 2018
Priority dateMay 17, 2018
Publication dateMay 19, 2020
Grant dateMay 19, 2020

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  1. Title

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Abstract

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A process for producing unsaturated polyester microparticles comprising: melt-mixing an unsaturated polyester and an oil in an extruder; washing the microparticles with an organic solvent to reduce the amount of oil; and removing the organic solvent to form the microparticles.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for making a composition comprising: providing an unsaturated polyester resin comprising: an ethylenically unsaturated monomer having the formula I wherein p and q are each independently 0 to 8, and z is 1 to 5, a first diol monomer; and a second diol monomer; mixing and heating a mixture comprising the unsaturated polyester resin and an oil at a temperature above the melting point temperature (Tm) of the unsaturated polyester resin, and applying a pressure to the mixture to form a microparticle composite; washing the microparticle composite with an organic solvent to reduce the amount of oil present in the microparticle composite; adding a thermal initiator to the microparticle composite; and removing the organic solvent to form the composition comprising microparticles with the thermal initiator on the surface of the microparticles. 2. The process of claim 1 , wherein the ethylenically unsaturated monomer is selected from the group consisting of maleic acid, maleic anhydride, fumaric acid, chloromaleic acid, itaconic acid, 3-hexenedioic acid, 2-heptenedioic acid, 2-octenedioic acid, glutaconic acid, 2-decenedioic acid, traumatic acid, muconic acid, mesaconic acid, citraconic acid, and esters and mixtures thereof. 3. The process of claim 1 , wherein the weight ratio of the oil to the unsaturated polyester resin is from about 1.0:1.6 to about 1.1:1.0. 4. The process of claim 1 , wherein the oil is selected from poppy seed oil, olive oil, peanut oil, sesame oil, cotton seed oil, soybean oil, safflower oil, corn oil, sunflower seed oil, canola oil, mineral oil, long chain paraffinic oil, liquid petrolatum, polydimethylsiloxane (PDMS), ethylmethylpolysiloxane, a copolymer of diraethylsiloxane and methylvinylsiloxane, hexamethyldisiloxane, octamethyltrisiloxane, octamethyltetracyclosiloxane, decamethylpentacyclosiloxane, and mixtures thereof. 5. The process of claim 1 , wherein the ethylenically unsaturated monomer is present from about 30 to about 95 mole percent (mol %) of the unsaturated polyester resin. 6. The process of claim 1 , wherein the unsaturated polyester resin has a crystallization temperature (Tc) of from about 50° C. to about 70° C. 7. The process of claim 1 , wherein the heating temperature is from about 75 to about 150° C. 8. The process of claim 1 , wherein the pressure is from 0 to about 50 meter grams (mg). 9. The process of claim 1 , wherein the thermal initiator is selected from the group consisting of ammonium persulfate, sodium persulfate, potassium persulfate, organic peroxides, 2,2′-azobis(2-methylpropanenitrile), 1,1′-azobis(cyanocyclohexane), 2, 2′-azobis(2-methyl-N-phenylpropionamidine) dihydrochloride, 2,2′-azobis[N-(4-chlorophenyl)-2-methylpropionamidine]dihydrochloride, 2,2′-azobis[N-(4-hydroxyphenyl)-2-methylpropionamidine]dihydrochloride, 2,2′-azobis[N-(4-amino-phenyl)-2-methylpropionamidine]tetrahydrochloride, 2,2′-azobis[2-methyl-N(phenylmethyl)propionamidine]dihydrochloride, 2,2′-azobis[2-methyl-N-2-propenylpropionamidine]dihydrochloride, 2,2′-azobis[N-(2-hydroxy-ethyl)-2-methylpropionamidine]dihydrochloride, 2,2′-azobis[2(5-methyl-2-imidazolin-2-yl)propane]dihydrochloride, 2,2′-azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride, 2,2′-azobis[2-(4,5,6,7-tetrahydro-1H-1,3-diazepin-2-yl)propane]dihydrochloride, 2,2′-azobis[2-(3,4,5,6-tetrahydropyrimidin-2-yl)propane]dihydrochloride, 2,2′-azobis[2-(5-hydroxy-3,4,5,6-tetrahydropyrimidin-2-yl)propane]dihydrochloride, 2,2′-azobis {2-[1-(2-hydroxyethyl)-2-imidazolin-2-yl]propane}dihydrochloride, and mixtures thereof.

Assignees

Inventors

Classifications

  • C08G63/52Primary

    Polycarboxylic acids or polyhydroxy compounds in which at least one of the two components contains aliphatic unsaturation · CPC title

  • Removing undesirable residual components, e.g. solvents, unreacted monomers; Degassing · CPC title

  • Unsaturated polyesters · CPC title

  • Polycarboxylic acids and polyhydroxy compounds in which at least one of the two components contains aliphatic unsaturation · CPC title

  • Polycarboxylic acids and polyhydroxy compounds in which at least one of the two components contains aliphatic unsaturation · CPC title

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What does patent US10655025B2 cover?
A process for producing unsaturated polyester microparticles comprising: melt-mixing an unsaturated polyester and an oil in an extruder; washing the microparticles with an organic solvent to reduce the amount of oil; and removing the organic solvent to form the microparticles.
Who is the assignee on this patent?
Xerox Corp
What technology area does this patent fall under?
Primary CPC classification C08G63/52. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue May 19 2020 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 5 related publications on this page (citations in our corpus or others sharing the same primary CPC).