Methods, systems, and devices for generating defined fiber constructs
US-2024216584-A1 · Jul 4, 2024 · US
US12522950B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12522950-B2 |
| Application number | US-202318098860-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 19, 2023 |
| Priority date | Jan 19, 2023 |
| Publication date | Jan 13, 2026 |
| Grant date | Jan 13, 2026 |
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The present invention discloses a method for preparing a polyurethane film, comprising the steps of: i) dissolving polyurethane into a first solvent to form a first solution; ii) dissolving salt into a second solvent to form a second solution; iii) preparing a spinning stock solution by mixing said first solution and said second solution; iv) spinning said spinning stock solution in an electrospinning device to obtain a polyurethane film; v) providing a container to which a third solvent is sprayed; and vi) arranging said polyurethane film in said container for a period of time.
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The invention claimed is: 1 . A method for preparing a polyurethane film, comprising the steps of: i) dissolving polyurethane into a first solvent to form a first solution; ii) dissolving salt into a second solvent to form a second solution; iii) preparing a spinning stock solution by mixing said first solution and said second solution; iv) spinning said spinning stock solution in an electrospinning device to obtain a polyurethane film; v) providing a container to which a third solvent is sprayed; and vi) arranging said polyurethane film in said container for a period of time. 2 . A method as claimed in claim 1 , wherein said polyurethane is a hydrophobic polyester thermoplastic polyurethane. 3 . A method as claimed in claim 2 , wherein said polyurethane is a ABn-type block linear polymer, wherein A is a polyester and B is a diol. 4 . A method as claimed in claim 3 , wherein said polyester has molecular weight of 1000-6000. 5 . A method as claimed in claim 3 , wherein said diol contains 2-12 linear carbon atoms. 6 . A method as claimed in claim 3 , wherein the chemical structure between the AB segments is diisocyanate. 7 . A method as claimed in claim 6 , wherein the density of said polyurethane is 1.10-1.25 g/cm3. 8 . A method as claimed in claim 1 , wherein said salt is inorganic salt selected from a group comprising lithium chloride, sodium chloride, potassium chloride, lithium carbonate, sodium carbonate, potassium carbonate, sodium bicarbonate, lithium nitrate, sodium nitrate, and a combination thereof; and/or organic salt selected from a group comprising octadecyltrimethylammonium chloride, tetraethylammonium bromide, and a combination thereof. 9 . A method as claimed in claim 1 , wherein said first solvent, said second solvent, and said third solvent are selected from a group comprising acetone, N,N-dimethylformamide, N,N-dimethylacetamide, tetrahydrofuran, acetonitrile, ether, ethane, ethanol, formic acid, acetic acid, chloroform, carbon tetrachloride, sulfolane, pyrimidine, formamide, n-hexane, chlorobenzene, dioxane, vinyl glycol, methylcyclohexane, 1,2-Dichloroethylene xylene, cyclohexane, pentane, anisole, butyl acetate, isopropyl acetate, dimethyl alum, N-methylpyrrolidone, dichloromethane, dichloroethyl alkane, chloromethane, benzene, toluene, ethyl acetate, and a combination thereof. 10 . A method as claimed in claim 1 , wherein the weight ratio of said polyurethane in said first solution is 15-30%. 11 . A method as claimed in claim 10 , wherein the weight ratio of said salt in said second solution is 0.1-2%. 12 . A method as claimed in claim 11 , wherein the weight ratio of said first solution to said second solution ranges from 50:0 to 35:15. 13 . A method as claimed in claim 1 , wherein said third solvent is prepared by mixing said first solvent with water. 14 . A method as claimed in claim 13 , wherein said water is deionized water. 15 . A method as claimed in claim 1 , wherein step vi) in claim 1 is carried out at temperature 25-35° C. 16 . A method as claimed in claim 1 , wherein step vi) in claim 1 is carried out at humidity 30%-85% and/or the amount of said third solvent sprayed is 0.5 to 5 ml. 17 . A method as claimed in claim 1 , wherein step iv) in claim 1 is carried out in a single-needle electrospinning device, with at least one of the following parameters: applied voltage at 20-30 kV, the flow rate of syringe pump at 0.1-1.0 ml/h, the receiving distance at 10-20 cm, the ambient temperature at 23-35° C., the ambient humidity at 35%-85%, the receiving substrate is selected from aluminum foil, oil paper, fabric or non-woven fabric. 18 . A method as claimed in claim 1 , wherein step iv) in claim 1 is carried out in a needle-free electrospinning device, with at least one of the following parameters: applied voltage at 50-80 kV, the receiving distance at 20-50 cm, the ambient temperature at 23-35° C., the ambient humidity at 35%-85%, the receiving substrate is selected from aluminum foil, oil paper, fabric or non-woven fabric. 19 . A method as claimed in claim 18 , wherein said needle-free electrospinning device is a multi-channel needle-free electrospinning device.
Polycondensates having carboxylic or carbonic ester groups in the main chain · CPC title
the fibre formed by solvent evaporation, i.e. dry electro-spinning · CPC title
polyurethanes · CPC title
from polyesters · CPC title
Manufacture of films or sheets · CPC title
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