Microfluidic devices and systems, and methods for operating microfluidic devices and systems
US-2024408596-A1 · Dec 12, 2024 · US
US12196660B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12196660-B2 |
| Application number | US-201916968225-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 18, 2019 |
| Priority date | Feb 26, 2018 |
| Publication date | Jan 14, 2025 |
| Grant date | Jan 14, 2025 |
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.
A method of measuring indices in superabsorbents, by initially charging excess aqueous solution or dispersion, swelling the superabsorbent in the initially charged aqueous solution or dispersion while stirring, dissolving or dispersing a component A in the aqueous solution or dispersion, measuring the enrichment of component A in the aqueous solution or dispersion during the swelling of the superabsorbent, using the enrichment of component A in the aqueous solution or dispersion to measure the time-dependent swelling characteristics and using these to determine the swelling constant k or the characteristic swell time τ, the index being dependent on the permeability of the superabsorbent, and ascertaining the index by means of a correlation measured beforehand between swelling constant k and index or characteristic swell time τ and index.
Opening claim text (preview).
The invention claimed is: 1. A method of measuring an index in a superabsorbent comprising initially charging excess aqueous solution or dispersion, swelling the superabsorbent in the initially charged aqueous solution or dispersion while stirring, dissolving or dispersing at least one component A in the aqueous solution or dispersion and measuring an enrichment of the at least one component A in the aqueous solution or dispersion during the swelling of the superabsorbent, wherein the enrichment of component A in the aqueous solution or dispersion is used to measure the time-dependent swelling characteristics and these are used to determine the swelling constant k or the characteristic swell time τ, the index is dependent on the permeability of the superabsorbent, and the index is ascertained by a correlation measured beforehand between swelling constant k and index or characteristic swell time τ and index. 2. The method according to claim 1 , wherein component A is a soluble salt and the enrichment of component A is measured via a rise in electrical conductivity of the solution. 3. The method according to claim 1 , wherein component A is a soluble dye and the enrichment of component A is measured via a rise in light absorption of the solution. 4. The method according to claim 1 , wherein the amount of aqueous solution or dispersion used is from 10 to 200 ml. 5. The method according to claim 1 , wherein the amount of superabsorbent used is from 0.5 to 5 g. 6. The method according to claim 1 , wherein a quotient of amount of aqueous solution or dispersion used and total swelling capacity of the superabsorbent used in the aqueous solution or dispersion is in a range from 2.5 to 5. 7. The method according to claim 1 , wherein the index is a time taken for a layer of superabsorbent particles to swell by a particular value. 8. The method according to claim 7 , wherein the layer of superabsorbents consists of 0.5 to 5 g of the superabsorbent and covers a circular area having a diameter of 5 to 7 cm. 9. The method according to claim 1 , wherein the correlation is measured by calculating the swelling constant k or the characteristic swell time τ and measuring the index of at least three superabsorbents having different permeability. 10. The method according to claim 9 , wherein the superabsorbents of different permeability are produced by changing an amount of crosslinker in a polymerization and/or by changing an amount of surface postcrosslinker in a surface postcrosslinking operation. 11. The method according to claim 1 , wherein the superabsorbent has an average particle size of 200 to 600 μm. 12. The method according to claim 1 , wherein the superabsorbent has a saline flow conductivity of at least 10×10 −7 cm 3 s/g. 13. The method according to claim 1 , wherein the superabsorbent has a centrifuge retention capacity of at least 10 g/g. 14. The method according to claim 1 for quality control in the continuous production of superabsorbents.
by use of radiation, e.g. transmitted or reflected light · CPC title
Measuring the absorption by excited molecules · CPC title
Sorption · CPC title
by using centrifugal effects · CPC title
Details, e.g. sample holders, mounting samples for testing · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.