Nanoparticle additives for silica soot compacts and methods for strengthening silica soot compacts
US-2016251252-A1 · Sep 1, 2016 · US
US10562804B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10562804-B2 |
| Application number | US-201715455776-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 10, 2017 |
| Priority date | Mar 18, 2016 |
| Publication date | Feb 18, 2020 |
| Grant date | Feb 18, 2020 |
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A method of producing bi-modal particles includes the steps of igniting a first precursor gas using a primary burner thereby producing a first plurality of particles of a first size, fluidly transporting the first plurality of particles down a particle tube, igniting a second precursor gas using a secondary burner thereby producing a second plurality of particles of a second size, flowing the second plurality of particles into the first plurality of particles, and capturing the first and second plurality of particles.
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What is claimed is: 1. A method of producing bi-modal particles, comprising the steps: igniting a first precursor gas using a primary burner coupled to a first particle tube thereby producing a first plurality of particles of a first size; fluidly transporting the first plurality of particles down the first particle tube; igniting a second precursor gas using a secondary burner positioned within a second particle tube thereby producing a second plurality of particles of a second size, smaller than the first size; fluidly transporting the second plurality of particles down the second particle tube; flowing the second plurality of particles into the first plurality of particles in the first particle tube; and capturing the first and second plurality of particles. 2. The method of claim 1 , wherein the first plurality of particles comprise SiO 2 and exhibit a particle D50 diameter of greater than about 25 nm and the second plurality of particles comprise SiO 2 and exhibit a particle D50 diameter of less than about 25 nm. 3. The method of claim 1 , wherein the second precursor gas comprises diatomic hydrogen and an organic siloxane. 4. The method of claim 1 , wherein the step of igniting the first precursor gas results in the first plurality of particles being formed at a higher temperature than the ignition of the second precursor gas forms the second plurality of particles at. 5. The method of claim 4 , wherein the first plurality of particles is formed at a temperature greater than about 1800° C. and the second plurality of particles is formed at a temperature of less than about 1500° C. 6. The method of claim 1 , further comprising the steps: controlling the flow rate of the second precursor gas using a controller in electrical communication with a sensor; and supplying the second precursor gas to the secondary burner. 7. The method of claim 1 , further comprising the steps: passing a carrier gas through the primary burner; and generating gas turbulence to the carrier gas. 8. The method of claim 1 , further comprising the steps: supplying the second precursor gas to a precursor tube; and passing an inert gas around the precursor tube to form a shield around the second precursor gas. 9. A method of forming an optical fiber, comprising the steps: igniting a first gas using a primary burner coupled to a first particle tube thereby producing a first plurality of particles of a first size; igniting a second gas using a secondary burner positioned within a second particle tube thereby producing a second plurality of particles of a second size, smaller than the first size; flowing the second plurality of particles from the second particle tube into the first plurality of particles in the first particle tube; capturing the first and second plurality of particles; and pressing the first and second plurality of particles into an optical fiber preform. 10. The method of claim 1 , further comprising the steps: consolidating the optical fiber preform; and drawing an optical fiber from the optical fiber preform. 11. The method of claim 2 , wherein a flow rate of the second gas to a precursor tube is controlled using a gas flow restrictor such that the second plurality of particles spend less than about 10 seconds above a temperature of about 1300° C. 12. The method of claim 3 , wherein the second plurality of particles exhibit a surface area of at least about 225 m 2 /g. 13. The method of claim 4 , wherein the second plurality of particles exhibit a surface area of at least about 350 m 2 /g. 14. The method of claim 5 , wherein the second gas comprises a combustible gas and an organic siloxane.
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