Method for the pneumatic delivery of superabsorbent particles

US11859059B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11859059-B2
Application numberUS-201916962659-A
CountryUS
Kind codeB2
Filing dateJan 28, 2019
Priority dateFeb 6, 2018
Publication dateJan 2, 2024
Grant dateJan 2, 2024

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

A method of pneumatically conveying superabsorbent particles, wherein the superabsorbent particles have been admixed with an aqueous wax dispersion prior to the pneumatic conveying, the wax has a glass transition temperature of at least 65° C. and, based on the untreated superabsorbent particles, from 0.020% to 0.20% by weight of wax has been used.

First claim

Opening claim text (preview).

The invention claimed is: 1. A method of pneumatically conveying superabsorbent particles comprising admixing the superabsorbent particles with an aqueous wax dispersion prior to pneumatic conveying, wherein the wax has a glass transition temperature of at least 65° C. and, based on the untreated superabsorbent particles, from 0.020% to 0.20% by weight of wax is admixed. 2. The method according to claim 1 , wherein the wax has a glass transition temperature of at least 80° C. 3. The method according to claim 1 , wherein, based on the superabsorbent particles, from 0.035% to 0.08% by weight of wax is admixed. 4. The method according to claim 1 , wherein the wax is a copolymer of 70 to 95 mol % of at least one ethylenically unsaturated hydrocarbon and 5 to 30 mol % of at least one ethylenically unsaturated carboxylic acid. 5. The method according to claim 1 , wherein the superabsorbent particles have an average particle size of 250 to 500 μm. 6. The method according to claim 1 , wherein the superabsorbent particles have an average sphericity (ASPHT) of greater than 0.72. 7. The method according to claim 1 , wherein a temperature of the superabsorbent particles during the pneumatic conveying is at least 40° C., and at least 20° C. less than the glass transition temperature of the wax. 8. The method according to claim 1 , wherein an initial gas velocity in the pneumatic conveying corresponds to a Froude number of 2 to 40. 9. The method according to claim 1 , wherein a conveying material load in the pneumatic conveying is from 1 to 30 kg/kg and the conveying material load is the quotient of conveying material mass flow rate and gas mass flow rate. 10. A composition comprising superabsorbent particles and wax particles, wherein the wax particles are on the surface of the superabsorbent particles, the wax particles are dispersible in water and have a glass transition temperature of at least 65° C., a proportion of the wax particles based on the superabsorbent particles is from 0.02% to 0.2% by weight, and the composition has an absorption under a pressure of 4.83 kPa (AUL0.7 psi) of at least 10 g/g. 11. The composition according to claim 10 , wherein the wax has a glass transition temperature of at least 80° C. 12. The composition according to claim 10 , wherein, based on the superabsorbent particles, the proportion of wax particles is from 0.035% to 0.08% by weight of wax. 13. The composition according to claim 10 , wherein the wax is a copolymer of 5 to 30 mol % of at least one ethylenically unsaturated carboxylic acid and 70 to 95 mol % of at least one ethylenically unsaturated hydrocarbon. 14. The composition according to claim 10 , wherein the superabsorbent particles have an average particle size of 250 to 500 μm. 15. The composition according to claim 10 , wherein the superabsorbent particles have an average sphericity (ASPHT) of greater than 0.72.

Assignees

Inventors

Classifications

  • C08J3/124Primary

    Treatment for improving the free-flowing characteristics · CPC title

  • A61L15/60Primary

    Liquid-swellable gel-forming materials, e.g. super-absorbents · CPC title

  • with pneumatic injection of the materials by the propelling gas · CPC title

  • Waxes · CPC title

  • with unsaturated acids, e.g. [meth]acrylic acid; with unsaturated esters, e.g. [meth]acrylic acid esters · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US11859059B2 cover?
A method of pneumatically conveying superabsorbent particles, wherein the superabsorbent particles have been admixed with an aqueous wax dispersion prior to the pneumatic conveying, the wax has a glass transition temperature of at least 65° C. and, based on the untreated superabsorbent particles, from 0.020% to 0.20% by weight of wax has been used.
Who is the assignee on this patent?
Basf Se
What technology area does this patent fall under?
Primary CPC classification C08J3/124. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jan 02 2024 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).