Superhydrophobic Compositions And Coating Process For The Internal Surface Of Tubular Structures
US-2015337170-A1 · Nov 26, 2015 · US
US9884341B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9884341-B2 |
| Application number | US-201213571814-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 10, 2012 |
| Priority date | Aug 12, 2011 |
| Publication date | Feb 6, 2018 |
| Grant date | Feb 6, 2018 |
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Disclosed is an organic coating with a high degree of global planarization. Further disclosed is an iPECVD-based method of coating a substrate with an organic layer having a high degree of global planarization. Disclosed is a flexible, alternating organic and inorganic multi-layer coating with low water permeability, a high-degree of transparency, and a high-degree of global planarization. Also disclosed is an iPECVD-based method of coating a substrate with the alternating organic and inorganic multi-layer coating.
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What is claimed is: 1. A method of coating a substrate, comprising: (a) introducing into a partially evacuated vessel containing the substrate a gaseous initiator at a first flow rate, and a first gaseous monomer at a second flow rate, thereby forming a first mixture; (b) introducing energy from a microwave plasma power source into said first mixture at a first power, wherein the first power is about 10 W to about 100 W, thereby depositing a first layer on the substrate at a first deposition rate, wherein the first layer is organic; (c) introducing into the vessel a first auxiliary gas at a third flow rate, and a second gaseous monomer at a fourth flow rate, thereby forming a second mixture; and (d) introducing energy into said second mixture at a second power, wherein the second power is about 800 W to about 1000 W, thereby depositing a second layer over the first layer at a second deposition rate, wherein the second layer is inorganic, to form a multi-layered coating on the substrate; wherein the vessel further comprises a variable plasma source, a stage for holding the substrate, and the substrate positioned on said stage; the first gaseous monomer is a siloxane; the second gaseous monomer is a siloxane; the gaseous initiator is selected from a group consisting of peroxides, aryl ketones, and alkyl azo compounds; the first layer is deposited on the substrate by initiated plasma enhanced chemical vapor deposition (iPECVD); and a pressure in the partially evacuated vessel is in the range of about 0.01 Torr to about 0.45 Torr. 2. The method of claim 1 , further comprising repeating steps (a)-(d), wherein the multi-layer coating comprises alternating organic and inorganic layers. 3. The method of claim 1 , wherein the number of layers of the multi-layered coating is from about 2 to about 8. 4. The method of claim 1 , wherein the first gaseous monomer is 1,3,5-trivinyl-1,1,3,5,5-pentamethyltrisiloxane or trivinyltrimethyl cyclotrisiloxane. 5. The method of claim 1 , wherein the second gaseous monomer is 1,3,5-trivinyl-1,1,3,5,5-pentamethyltrisiloxane or trivinyltrimethyl cyclotrisiloxane. 6. The method of claim 1 , wherein the gaseous initiator is a peroxide. 7. The method of claim 1 , wherein the pressure in the partially evacuated vessel is from about 0.05 Torr to about 0.4 Torr. 8. The method of claim 1 , wherein the first flow rate is from about 30 sccm to about 0.01 sccm. 9. The method of claim 1 , wherein the second flow rate is from about 30 sccm to about 0.01 sccm. 10. The method of claim 1 , wherein the third flow rate is from about 5 sccm to about 750 sccm. 11. The method of claim 1 , wherein the fourth flow rate is from about 30 sccm to about 0.01 sccm. 12. The method of claim 1 , further comprising adjusting a temperature of the stage. 13. The method of claim 1 , wherein the stage is moveable. 14. The method of claim 1 , further comprising discharging in timed pulses the energy introduced into the first mixture at the first power, thereby creating a duty cycle. 15. The method of claim 14 , wherein each of the timed pulses t ON , is from about 1 ns to about 10 s. 16. The method of claim 1 , wherein the first deposition rate is from about 1 nm/minute to about 100 nm/minute. 17. The method of claim 1 , wherein the second deposition rate is from about 1 nm/minute to about 100 nm/minute. 18. The method of claim 1 , wherein the energy introduced into said second mixture is from a microwave power source. 19. The method of claim 1 , wherein the first gaseous monomer is 1,3,5-trivinyl-1,1,3,5,5-pentamethyltrisiloxane. 20. The method of claim 1 , wherein the second gaseous monomer is 1,3,5-trivinyl-1,1,3,5,5-pentamethyltrisiloxane. 21. The method of claim 1 , wherein the gaseous initiator is tert-butyl peroxide (TBPO). 22. The method of claim 1 , wherein the first gaseous monomer is 1,3,5-trivinyl-1,1,3,5,5-pentamethyltrisiloxane; the second gaseous monomer is 1,3,5-trivinyl-1,1,3,5,5-pentamethyltrisiloxane; and the gaseous initiator is tert-butyl peroxide (TBPO). 23. The method of claim 1 , further comprising discharging in timed pulses the energy introduced into the second mixture at the second power, thereby creating a duty cycle. 24. The method of claim 23 , wherein each of the timed pulses, t ON , is from about 1 ns to about 10 s.
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