Process for producing synthetic quartz glass using a cleaning device
US-2017341967-A1 · Nov 30, 2017 · US
US9481597B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9481597-B2 |
| Application number | US-201214365944-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 13, 2012 |
| Priority date | Dec 16, 2011 |
| Publication date | Nov 1, 2016 |
| Grant date | Nov 1, 2016 |
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The invention relates to a method for producing synthetic quartz glass by vaporizing a polyalkylsiloxane as a liquid SiO 2 feedstock ( 105 ), converting the vaporized SiO 2 feedstock ( 107 ) into SiO 2 particles, separating the SiO 2 particles, forming a soot body ( 200 ) and vitrifying the soot body ( 200 ). According to the invention, the vaporizing of the heated SiO 2 feedstock ( 105 ) comprises an injection phase in an expansion chamber ( 125 ), in which the SiO 2 feedstock ( 105 ) is atomized into fine droplets, wherein the droplets have an average diameter of less than 5 pm, and wherein the atomizing of the droplets takes place in a preheated carrier gas stream which has a temperature of more than 180° C.
Opening claim text (preview).
The invention claimed is: 1. A method for producing synthetic quartz glass, said method comprising: (A) providing a liquid SiO 2 feedstock having more than 70% by wt. of octamethylcyclotetrasiloxane, (B) vaporizing the liquid SiO 2 feedstock into a gaseous SiO 2 feedstock vapor, (C) converting the SiO 2 feedstock vapor into SiO 2 particles, (D) depositing the SiO 2 particles on a deposition surface so as to form a SiO 2 soot body, (E) vitrifying the SiO 2 soot body so as to form the synthetic quartz glass, wherein the vaporizing of the SiO 2 feedstock comprises injection of the liquid SiO 2 feedstock into an expansion chamber such that the SiO 2 feedstock is atomized into fine droplets, wherein the droplets have a mean diameter of less than 5 μm, and wherein the droplets are atomized in a preheated carrier gas stream that has a temperature of more than 180° C. and wherein a molar ratio of carrier gas to siloxane is greater than or equal to 1.5. 2. The method according to claim 1 , wherein the droplets have a mean diameter of less than 2 μm and wherein the carrier gas stream is supplied at a pressure of 1.5 to 5 bar.
Improving the yield, e-g- reduction of reject rates · CPC title
Pure silica glass, e.g. pure fused quartz · CPC title
Non-halide · CPC title
with vapour generated from liquid glass precursors, e.g. directly by heating the liquid · CPC title
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