Degradable polymeric compositions and articles comprising same
US-2024425683-A1 · Dec 26, 2024 · US
US11859059B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11859059-B2 |
| Application number | US-201916962659-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 28, 2019 |
| Priority date | Feb 6, 2018 |
| Publication date | Jan 2, 2024 |
| Grant date | Jan 2, 2024 |
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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.
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.
Treatment for improving the free-flowing characteristics · CPC title
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
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