Resin composition, method of manufacturing display device, and display device
US-2024294687-A1 · Sep 5, 2024 · US
US11339253B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11339253-B2 |
| Application number | US-201916570993-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 13, 2019 |
| Priority date | Jul 26, 2018 |
| Publication date | May 24, 2022 |
| Grant date | May 24, 2022 |
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 preparing comb structure temperature/pH-responsive polycarboxylic acid by end-group functionalization adopts temperature/pH-responsive monomer, unsaturated halogenated hydrocarbon, small monomer of carboxylic acid and other raw materials to prepare polycarboxylic acid material via self-polymerization, substitution and copolymerization. Temperature/pH-responsive monomers are first self-polymerized to obtain temperature/pH-responsive polymer chain with end-group functionalization, and then substitution with unsaturated halogenated hydrocarbons is conducted to obtain temperature/pH-responsive macromonomers with end-group functionalization, finally the obtained product is copolymerized with small carboxylic acid monomers to prepare comb structure polymer with polycarboxylic acid main chain and temperature/pH-responsive side chain.
Opening claim text (preview).
What is claimed is: 1. A method for preparing comb structure temperature-responsive polycarboxylic acid with end-group functionalization via self-polymerization, substitution and co-polymerization, the method comprising the following steps: (1) self-polymerization: firstly, an organic solvent is added to a reactor and heated to 50-120° C., introducing an initiator with 10-30 minutes agitation until a mixture thereof is evenly mixed, and then a mixture solution of a temperature-responsive monomer and an end-group functional agent is introduced by dropping for 1-12 hours, after dropping is completed, a self-polymerization product solution is obtained by reacting at a constant temperature of 50-120° C. for 1-6 hours; (2) substitution: an unsaturated halogenated hydrocarbon, an acid-binding agent and a catalyst are successively added into the self-polymerization product solution obtained in step (1), adjust the temperature to 30-120° C. with agitation and keep the reaction at a constant temperature of 30-120° C. for 2-15 hours to obtain unsaturated temperature-responsive macromonomer by decompressed distillation; (3) co-polymerization: the unsaturated temperature-responsive macromonomer obtained in step (2) is dissolved in solvent water and heated to 50-90° C., agitate 10-30 minutes until the mixture thereof is evenly mixed, an aqueous solution of initiator with 1-10% mass fraction, an aqueous solution of carboxylic acid small monomer with 1-30% mass fraction and an aqueous solution of chain transfer agent with 1-5% mass fraction are added at the same time by dropping for 1-6 hours, after dropping is completed, the reaction is kept at a constant temperature of 50-90° C. for 1-6 hours to obtain a temperature-responsive polycarboxylic acid solution with required concentration after adding water; wherein the organic solvent used in the self-polymerization reaction in step (1) is: tetrahydrofuran, N, N-dimethyl formamide, aniline, cyclobutyl sulfoxide or dimethyl sulfoxide, the mass ratio of the organic solvent to the temperature-responsive monomer is 1-12:1; the initiator used in the self-polymerization reaction in step (1) is: azodiisobutyl nitrile, azodiisoheptyl nitrile, dibenzoyl peroxide, tert-butyl hydrogen peroxide, tert-butyl peroxide benzoate or ditert-butyl peroxide, the molar ratio of the initiator to the temperature-responsive monomer is 0.05-0.2:1; the temperature-responsive monomer used in the self-polymerization reaction in step (1) is: N-Isopropyl acrylamide, N-isopropyl methylacrylamide, N-n-propyl acrylamide, N-tert-butyl acrylamide, N,N′-methylene diacrylamide or N,N-dimethylacrylamide; the end group functionalizing agent used in the self-polymerization reaction in step (1) is: 6-mercapto hexanol, 2-mercapto ethanol or 3-mercapto propanol, the molar ratio of the end group functionalizing agent to the temperature-responsive monomer is 0.05-0.6:1; the unsaturated halogenated hydrocarbon used in the substitution reaction in step (2) is: allyl chloride, allyl bromide, 3-chloro-2-methylpropylene, 4-bromo-1-butene or 1-chloro-3-methyl-2-butene, the molar ratio of the unsaturated halogenated hydrocarbon to the self-polymerization product in step (1) is 1-4:1; the acid-binding agent used in the substitution reaction in step (2) is: triethylamine, N,N-diisopropyl ethylamine, tetramethylenediamine or pyridine, the molar ratio of the acid-binding agent to the self-polymerization product in (1) is 2-12:1; the catalyst used in the substitution reaction in step (2) is: ammonium tetrabutyl sulfate, benzyl trimethylammonium chloride, benzyl triethyl ammonium chloride, tetrabutyl ammonium chloride, tetrabutyl ammonium bromide or tetrabutyl ammonium iodide, the molar ratio of the catalyst to the self-polymerization product in step (1) is 0.02-0.06:1; the mass ratio between the solvent water used in the copolymerization reaction in step (3) and the unsaturated temperature-responsive macromonomer obtained in step (2) is 0.5-1.2:1; a solute in the aqueous solution of initiator is: ammonium persulfate, potassium persulfate, sodium persulfate, or hydrogen peroxide, the molar ratio of the solute to the unsaturated temperature-responsive macromonomer in step (2) is: 0.05-0.2:1; a solute in the aqueous solution of carboxylic acid small monomer is: acrylic acid, methacrylic acid, itaconic acid, maleic anhydride or fumaric acid, the molar ratio of the solute to the unsaturated temperature-responsive macromonomer in step (2) is: 1-10:1; a solute in the aqueous solution of chain transfer agent is: isopropanol, thioglycolic acid, 3-thioglycolic acid or sodium formate, the molar ratio of the solute to the unsaturated temperature-responsive macromonomer in step (2) is: 0.05-0.6:1. 2. A comb structure temperature-responsive polycarboxylic acid prepared by the method according to claim 1 , having the following structural expression: where, R 1 represents hydrogen, methyl, or methylene carboxyl groups; R 2 represents hydrogen or carboxyl; R 3 , R 4 and R 5 represents hydrogen or methyl; R 6 represents methylene or dimethylene; R 7 represents dimethylene, trimethylene, or hexamethylene; R 8 represents N-Isopropyl methyl amides, N-n-propyl amides, N-tert-butyl amides, N-methylene, N,N′-acrylamide or N,N-dimethyl acyl; R 9 represents hydrogen or methyl; wherein a and b are positive integers indicating the number of repeating units distributed randomly in main molecular chains, a:b=1-10:1; wherein n is a positive integer, indicating the number of repeat units in side molecular chains, a range of n is 5-120. 3. A method for preparing comb structure pH-responsive polycarboxylic acid with end-group functionalization via self-polymerization, substitution and co-polymerization, the method comprising the following steps: (1) self-polymerization: firstly, an organic solvent is added to a reactor and heated to 50-120° C., introducing an initiator with 10-30 minutes agitation until a mixture thereof is evenly mixed, and then a mixture solution of a pH-responsive monomer and an end-group functional agent is introduced by dropping for 1-12 hours, after dropping is completed, a self-polymerization product solution is obtained by reacting at a constant temperature of 50-120° C. for 1-6 hours; (2) substitution: an unsaturated halogenated hydrocarbon, an acid-binding agent and a catalyst are successively added into the self-polymerization product solution obtained in step (1), adjust the temperature to 30-120° C. with agitation and keep the reaction at a constant temperature of 30-120° C. for 2-15 hours to obtain unsaturated pH-responsive macromonomer by decompressed distillation; (3) co-polymerization: the unsaturated pH-responsive macromonomer obtained in step (2) is dissolved in solvent water and heated to 50-90° C., agitate 10-30 minutes until the mixture thereof is evenly mixed, an aqueous solution of initiator with 1-10% mass fraction, an aqueous solution of carboxylic acid small monomer with 1-30% mass fraction and an aqueous solution of chain transfer agent with 1-5% mass fraction are added at the same time by dropping for 1-6 hours, after dropping is completed, the reaction is kept at a constant temperature of 50-90° C. for 1-6 hours to obtain a pH-responsive polycarboxylic acid solution with required concentration after adding water; wherein the organic solvent used in the self-polymerization reaction in step (1) is: tetrahydrofuran, N, N-dimethyl formamide, aniline, cyclobutyl sulfoxide or dimethyl sulfoxide, the mass ratio of the organic solvent to the pH-responsive monomer is 1-12:1; the initiator used in the self-polymerization reaction in step (1) is: azodiisobutyl nitrile, azodiisoheptyl nitrile, dibenzoyl peroxide, tert-butyl hydrogen peroxide, tert-butyl perox
on to polymers of monomers containing heterocyclic nitrogen · CPC title
Polymerisation of acrylate or methacrylate esters on to polymers thereof · CPC title
Dendritic macromolecules · CPC title
on to polymers of amides or imides · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.