Process for producing water-absorbing polymer fibers
US-2015292117-A1 · Oct 15, 2015 · US
US2017306528A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017306528-A1 |
| Application number | US-201615518291-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 2, 2016 |
| Priority date | Sep 4, 2015 |
| Publication date | Oct 26, 2017 |
| 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.
This invention relates to a method of manufacturing a superabsorbent polymer fiber and a superabsorbent polymer fiber manufactured thereby.
Opening claim text (preview).
1 . A method of manufacturing a superabsorbent polymer fiber, comprising steps of: 1) preparing a neutralization solution by dissolving a water-soluble ethylenic unsaturated monomer in a sodium hydroxide aqueous solution; 2) preparing a spinning solution by adding the neutralization solution with a crosslinking agent and then performing stirring; and 3) producing a superabsorbent polymer fiber by subjecting the spinning solution to centrifugal spinning using a spinneret and then performing drying, wherein the neutralization solution has a neutralization degree of 40 to 90 mol %. 2 . The method of claim 1 , wherein the neutralization solution has a neutralization degree of 50 to 80 mol %. 3 . The method of claim 1 , wherein the water-soluble ethylenic unsaturated monomer is at least one selected from the group consisting of anionic monomers and salts thereof, including isobutylene, acrylic acid, polyacrylic acid, methacrylic acid, maleic anhydride, fumaric acid, crotonic acid, itaconic acid, 2-acryloyl ethanesulfonic acid, 2-methacryloyl ethanesulfonic acid, 2-(meth)acryloyl propanesulfonic acid, and 2-(meth)acrylamide-2-methylpropanesulfonic acid; nonionic hydrophilic monomers, including (meth)acrylamide, N-substituted (meth)acrylate, 2-hydroxyethyl(meth)acrylate, 2-hydroxypropyl(meth)acrylate, methylacrylate, hydroxypropyl methacrylate, methoxypolyethyleneglycol (meth)acrylate, and polyethyleneglycol (meth)acrylate; and amino group-containing unsaturated monomers and quaternary salts thereof, including (N,N)-dimethylaminoethyl (meth)acrylate and (N,N)-dimethylaminopropyl (meth)acrylamide. 4 . The method of claim 1 , wherein the water-soluble ethylenic unsaturated monomer is at least one selected from the group consisting of isobutylene, maleic anhydride, polyacrylic acid, acrylic acid, methylacrylate, hydroxypropyl methacrylate. 5 . The method of claim 1 , wherein the crosslinking agent is at least one selected from the group consisting of a polyhydric alcohol compound, an acrylate-based compound, an epoxy compound, a polyamine compound, a haloepoxy compound, a haloepoxy compound condensed product, an oxazoline compound, a mono-, di- or poly-oxazolidinone compound, a cyclic urea compound, a multivalent metal salt, and an alkylene carbonate compound. 6 . The method of claim 1 , wherein the crosslinking agent is an epoxy compound. 7 . The method of claim 1 , wherein the centrifugal spinning is performed at a rotation speed of 3,000 rpm to 15,000 rpm. 8 . The method of claim 1 , wherein in the preparing the neutralization solution of step 1), the water-soluble ethylenic unsaturated monomer is used in an amount of 10 to 50 wt % based on a total weight of the sodium hydroxide aqueous solution. 9 . The method of claim 1 , wherein in the preparing the spinning solution of step 2), the crosslinking agent is used in an amount of 0.001 to 5 wt % based on a total weight of the water-soluble ethylenic unsaturated monomer. 10 . The method of claim 1 , wherein in step 3), the drying is performed at a temperature of 100 to 250° C. for 10 min to 120 min. 11 . The method of claim 1 , wherein the fiber is a nonwoven fabric. 12 . The method of claim 1 , wherein the superabsorbent polymer fiber is used for manufacturing a hygiene material.
Olefin series · CPC title
used for fibers · CPC title
forming webs during fibre formation, e.g. flash-spinning · CPC title
characterised by the absorbing medium (A61F13/20 takes precedence) · CPC title
by means of rotating spinnerets · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.