Filter media with a multi-layer structure
US-10155187-B2 · Dec 18, 2018 · US
US11111614B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11111614-B2 |
| Application number | US-201916434918-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 7, 2019 |
| Priority date | Jun 8, 2018 |
| Publication date | Sep 7, 2021 |
| Grant date | Sep 7, 2021 |
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A method for tuning characteristics of a polyamide nanofiber nonwoven comprising the step of targeting a specific average nanofiber diameter and/or a specific relative viscosity for the polyamide nanofiber nonwoven. The specific average nanofiber diameter is within a range from 100 nm to 1000 nm and/or the specific relative viscosity is within a range from 5 to 75, e.g., from 15 to 50. The process further comprises the steps of extruding a polyamide composition having a moisture content with a pressurized gas through a fiber forming channel having a channel temperature to form the polyamide nanofiber nonwoven having the target average nanofiber diameter and/or relative viscosity and controlling the moisture content, the pressure of pressurized gas, and/or the channel temperature based on the specific average nanofiber diameter and/or the specific relative viscosity.
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What is claimed is: 1. A method for tuning characteristics of a polyamide nanofiber nonwoven comprising the steps of: targeting a specific average nanofiber diameter and/or a specific relative viscosity for the polyamide nanofiber nonwoven, wherein the specific average nanofiber diameter is within a range from 100 nm to 1000 nm and/or the specific relative viscosity is within a range from 5 to 75; extruding a polyamide composition having a moisture content with a pressurized gas through a fiber forming channel having a channel temperature to form the polyamide nanofiber nonwoven having the target average nanofiber diameter and/or relative viscosity; and controlling the moisture content by drying the polyamide composition to have a moisture content of less than 0.02 wt. %, and rehydrating the dried polyamide composition. 2. The method of claim 1 , wherein the specific average nanofiber diameter is within a range of 200 nm to 700 nm. 3. The method of claim 1 , wherein the specific relative viscosity is within a range from 15 to 50. 4. The method of claim 1 , wherein the moisture content is controlled from 0.005 wt. % to 1 wt. %. 5. The method of claim 1 , wherein the pressure of the pressurized gas is controlled to range from 160 kPa to 220 kPa. 6. The method of claim 1 , wherein the channel temperature is controlled to range from 270° C. to 330° C. 7. The method of claim 1 , wherein the fiber forming channel comprises a die and/or a capillary. 8. The method of claim 1 , wherein the polyamide nanofiber nonwoven is melt-blown and/or is free of solvent. 9. The method of claim 1 , wherein the polyamide composition comprises a catalyst. 10. A method for tuning the relative viscosity of a polyamide nanofiber nonwoven comprising the steps of: targeting a specific relative viscosity for the polyamide nanofiber nonwoven, wherein the specific relative viscosity is within a range from 5 to 75; extruding a polyamide composition having a moisture content to form the polyamide nanofiber nonwoven having the target relative viscosity; and controlling the moisture content based on the target relative viscosity. 11. The method of claim 10 , wherein the relative viscosity is targeted to a targeted relative viscosity within the range from 15 to 50. 12. The method of claim 10 , wherein the moisture content is controlled to range from 0.005 wt. % to 1 wt. %. 13. The method of claim 10 , wherein the moisture content is controlled to range from 0.02 wt. % to 0.3 wt. %. 14. The method of claim 10 , wherein the controlling comprises: drying the polyamide composition to have a moisture content of less than 0.02 wt. %; and rehydrating the dried polyamide composition. 15. The method of claim 10 , wherein the polyamide composition is extruded through a fiber forming channel having a channel temperature and the channel temperature is controlled to range from 270° C. to 330° C. 16. The method of claim 10 , wherein the polyamide nanofiber nonwoven is melt-blown and/or is free of solvent. 17. The method of claim 10 , wherein the polyamide composition comprises a catalyst. 18. The method of claim 1 , wherein the polyamide nanofiber nonwoven further comprises zinc oxide. 19. The method of claim 10 , wherein the polyamide nanofiber nonwoven further comprises zinc oxide.
Humidity control, or oiling, of filaments, threads or the like, leaving the spinnerettes · CPC title
by means of a flowing gas (e.g. melt-blowing) · CPC title
with bonds between thermoplastic filaments produced in association with filament formation, e.g. immediately following extrusion · CPC title
Pressure · CPC title
from polyamides (from polyamino acids or polypeptides D01F6/68) · CPC title
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