Method for producing a large quartz-glass tube
US-2016168005-A1 · Jun 16, 2016 · US
US11299417B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11299417-B2 |
| Application number | US-201616062658-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 16, 2016 |
| Priority date | Dec 18, 2015 |
| Publication date | Apr 12, 2022 |
| Grant date | Apr 12, 2022 |
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The invention relates to a process for preparing a quartz glass body comprising the process steps i.) Providing a silicon dioxide granulate, ii.) Making a glass melt from the silicon dioxide granulate in a melting crucible, and iii.) Making a quartz glass body from at least a part of the glass melt, wherein the melting crucible is comprised in an oven and is made of at least one material comprising tungsten or molybdenum or a combination thereof. The invention further relates to a quartz glass body which can be obtained by this process. Further, the invention relates to a light guide, an illuminant and a formed body, each of which can be obtained by processing the quartz glass body further.
Opening claim text (preview).
The invention claimed is: 1. A process for preparing a quartz glass body comprising pyrogenic silicon dioxide, comprising: providing a silicon dioxide granulate comprising: providing a pyrogenic silicon dioxide powder; and processing the silicon dioxide powder to give a silicon dioxide granulate, wherein the silicon dioxide granulate has a larger particle diameter than the silicon dioxide powder; making a glass melt from the silicon dioxide granulate in a melting crucible; and making a quartz glass body from at least a part of the glass melt; wherein the melting crucible is comprised in an oven, wherein the melting crucible is made of at least one material comprising tungsten or molybdenum or a combination thereof, and wherein the quartz glass body comprises: an OH content of less than 500 ppm; a chlorine content of less than 60 ppm; a tungsten content of less than 1000 ppb; a molybdenum content of less than 1000 ppb; wherein the ppb and ppm are based on the total weight of the quartz glass body in each case. 2. The process according to claim 1 , wherein the oven has at least one gas inlet and one gas outlet, wherein a gas which is removed through the gas outlet has a dew point of less than 0° C. on exiting the oven through the gas outlet. 3. The process according to claim 1 , wherein the melting crucible does not have a coating selected from a material comprising rhenium, iridium, osmium or a combination thereof on the surface facing the glass melt. 4. The process according to claim 1 , wherein the quartz glass body comprises at least one of: an aluminium content of less than 200 ppb; an ODC content of less than 5·10 15 /cm 3 ; a metal content of metals which are different from aluminium of less than 1 ppm; a viscosity (p=1013 hPa) in a range from log 10 (η (1250° C.)/dPas)=11.4 to log 10 (η (1250° C.)/dPas)=12.9, or log 10 (η (1300° C.)/dPas)=11.1 to log 10 (1300° C.)/dPas)=12.2, or log 10 (η (1350° C.)/dPas)=10.5 to log 10 (η (1350° C.)/dPas)=11.5; a standard deviation of the OH content of not more than 10%, based on the OH content of the quartz glass body; a standard deviation of the Cl content of not more than 10%, based on the Cl content of the quartz glass body; a standard deviation of the Al content of not more than 10%, based on the Al content of the quartz glass body; a refractive index homogeneity of less than 1*10 −4 ; and a cylindrical form, wherein the ppb and ppm are based on the total weight of the quartz glass body in each case. 5. The process according to claim 1 , wherein the silicon dioxide powder comprises at least one of: a BET surface area in a range from 20 to 60 m 2 /g; a bulk density in a range from 0.01 to 0.3 g/cm 3 ; a carbon content of less than 50 ppm; a chlorine content of less than 200 ppm; an aluminium content of less than 200 ppb; a total content of metals which are different from aluminium of less than 5 ppm; at least 70 wt.-% of the powder particles have a primary particle size in a range from 10 to 100 nm; a tamped density in a range from 0.001 to 0.3 g/cm 3 ; a residual moisture content of less than 5 wt.-%; a particle size distribution D 10 in a range from 1 to 7 μm; a particle size distribution D 50 in a range from 6 to 15 μm; and a particle size distribution D 90 in a range from 10 to 40 μm; wherein the wt.-%, ppm and ppb are based on the total weight of the silicon dioxide powder in each case. 6. The process according to claim 1 , wherein the silicon dioxide powder is prepared from a compound selected from the group consisting of siloxanes, silicon alkoxides and silicon halides. 7. The process according to claim 1 , further comprising making a hollow body with at least one opening from the quartz glass body. 8. A process for preparing a light guide, comprising: providing a hollow body with at least one opening obtained by a process according to claim 7 ; introducing one or more core rods into the quartz glass body through the at least one opening to obtain a precursor; and drawing the precursor from in the warm to obtain a light guide with one or more cores and a jacket. 9. A process for preparing a light guide, comprising: providing a hollow body obtained by a process according to claim 7 ; optionally fitting the hollow body with electrodes; and filling the hollow body with a gas. 10. A process for preparing a formed body comprising: providing a quartz glass body according to claim 7 ; and forming a formed body from the quartz glass body.
Processes specially adapted for the production of quartz or fused silica articles {, not otherwise provided for (C03B19/01, C03B19/066, C03B19/106, C03B19/12, C03B19/14, C03B37/00 take precedence)} · CPC title
doped with hydroxyl groups · CPC title
Melting processes · CPC title
Assembly details; Material or dimensions of burner; Manifolds or supports · CPC title
Pure silica glass, e.g. pure fused quartz · CPC title
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