Novel esterified cellulose ethers of very low viscosity
US-2015376299-A1 · Dec 31, 2015 · US
US2025034284A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025034284-A1 |
| Application number | US-202418784053-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 25, 2024 |
| Priority date | Jul 26, 2023 |
| Publication date | Jan 30, 2025 |
| Grant date | — |
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.
Provided is a method of producing hydroxypropyl methylcellulose acetate succinate powder capable of inhibiting aggregation of particles of the precipitated esterified cellulose ether and reducing produced amount of fine powder to thereby obtain the esterified cellulose ether in high yield. The method of producing hydroxypropyl methylcellulose acetate succinate powder comprises an esterification reaction step, a precipitation step, a washing/recovering step and a drying step, wherein the precipitation step is a step of introducing the reaction solution, obtained in the esterification reaction step, and water into a mixer provided with a rotatable rotor having blades and a perforated plate arranged to surround the rotor in a direction perpendicular to a radial direction of the rotor to allow a suspension, containing precipitated hydroxypropyl methylcellulose acetate succinate particles, to pass through the perforated plate to be discharged therethrough.
Opening claim text (preview).
What is claimed is: 1 . A method of producing hydroxypropyl methylcellulose acetate succinate powder comprising the steps of: esterifying hydroxypropyl methylcellulose with an acetylating agent and a succinoylating agent in the presence of an aliphatic carboxylic acid to prepare a reaction solution containing hydroxypropyl methylcellulose acetate succinate; introducing the reaction solution and water into a mixer provided with a rotatable rotor having blades and a perforated plate arranged to surround the rotor in a direction perpendicular to a radial direction of the rotor for precipitation, and allowing a suspension, containing precipitated hydroxypropyl methylcellulose acetate succinate particles, to pass through the perforated plate to be discharged therethrough; washing the hydroxypropyl methylcellulose acetate succinate particles in the suspension and recovering the washed hydroxypropyl methylcellulose acetate succinate particles; and drying the washed hydroxypropyl methylcellulose acetate succinate particles. 2 . The method according to claim 1 , wherein the perforated plate has openings each having an opening area of 0.1 to 10.0 mm 2 . 3 . The method according to claim 1 , wherein a peripheral speed of the outermost circumference of the blades is 5.0 to 20.0 m/s. 4 . The method according to claim 1 , wherein 200 to 600 parts by mass of water per 100 parts by mass of the reaction solution is added into the reaction solution. 5 . The method according to claim 1 , wherein an average particle diameter of the hydroxypropyl methylcellulose acetate succinate particles is 500 to 2000 μm when the diameter is estimated from particle size distribution of the hydroxypropyl methylcellulose acetate succinate particles in the suspension in accordance with a wet sieving test as set forth in JIS Z8815, and wherein a mass percentage of the particles having a diameter of 250 μm or less in the total mass of the particles is 15.0% or less. 6 . A hydroxypropyl methylcellulose acetate succinate powder, wherein an average particle diameter of the hydroxypropyl methylcellulose acetate succinate powder as determined in accordance with a dry sieving test as set forth in JIS Z8815 is 300 μm or more and 1000 μm or less, the powder has a loose bulk density of 0.30 g/mL or less, and a degree of compression of the powder, defined as a ratio of the difference between a tapped bulk density and a loose bulk density relative to the tapped bulk density, is 10% or less.
Post-etherification treatments of chemical or physical type, {e.g. mixed etherification in two steps}, including purification · CPC title
Fractionation of cellulose, e.g. separation of cellulose crystallites · CPC title
Isolation · CPC title
Preparation of cellulose ether-esters · CPC title
Preparation of mixed organic cellulose esters {, e.g. cellulose aceto-formate or cellulose aceto-propionate} · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.