IP Library Granted Patent US 8,240,172
Granted Patent B2
US 8,240,172 · App. 13/080,704 · Granted Aug 14, 2012

Process for production of synthetic quartz glass

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Quick Facts
Patent No.
US 8,240,172
App. No.
13/080,704
Granted
Aug 14, 2012
Kind
B2
Abstract

The present invention relates to a process for production of a synthetic quartz glass having a fluorine concentration of 1,000 mass ppm or more, the process comprising: (a) a step of depositing and growing quartz glass fine particles obtained by flame hydrolysis of a glass forming raw material onto a substrate, to thereby form a porous glass body; (b) a step of keeping the porous glass body in a reaction vessel that is filled with elemental fluorine (F 2 ) or a mixed gas comprising elemental fluorine (F 2 ) diluted with an inert gas and contains a solid metal fluoride, to thereby obtain a fluorine-containing porous glass body; and (c) a step of heating the fluorine-containing porous glass body to a transparent vitrification temperature, to thereby obtain a fluorine-containing transparent glass body.

Claims (24)

1. A process for production of a synthetic quartz glass having a fluorine concentration of 1,000 mass ppm or more, the process comprising:

(a) depositing and growing quartz glass fine particles obtained by flame hydrolysis of a glass forming raw material onto a substrate, to thereby form a porous glass body;

(b) keeping the porous glass body in a reaction vessel that is filled with elemental fluorine (F 2 ) or a mixed gas comprising elemental fluorine (F 2 ) diluted with an inert gas and contains a solid metal fluoride, to thereby obtain a fluorine-containing porous glass body; and

(c) heating the fluorine-containing porous glass body to a transparent vitrification temperature, to thereby obtain a fluorine-containing transparent glass body.

2. The production process according to claim 1 , wherein the solid metal fluoride is sodium fluoride.

3. The production process according to claim 1 , further comprising subjecting the inside of the reaction vessel to a degassing treatment before filling the inside of the reaction vessel with elemental fluorine (F 2 ) or a mixed gas obtained by diluting elemental fluorine (F 2 ) with an inert gas in (b).

4. The production process according to claim 1 , further comprising presintering the porous glass body at from 1,100 to 1,350° C. between (a) and (b).

5. The production process according to claim 1 , wherein (b) is carried out a temperature of 200° C. or less.

6. The production process according to claim 1 , wherein (b) is carried out a temperature of 150° C. or less.

7. The production process according to claim 1 , wherein the inert gas comprises nitrogen, helium or argon.

8. The production process according to claim 1 , wherein the transparent vitrification temperature is within the range of from 1,350 to 1,800° C.

9. The production process according to claim 1 , wherein the transparent glass body has a fluorine concentration of 3,000 ppm or more.

10. A process for production of a TiO 2 -containing synthetic quartz glass (TiO 2 —SiO 2 glass) having a fluorine concentration of 1,000 mass ppm or more, the process comprising:

(a) depositing and growing TiO 2 —SiO 2 glass fine particles obtained by flame hydrolysis of an Si precursor and a Ti precursor each serving as a glass forming raw material onto a substrate, to thereby form a porous TiO 2 —SiO 2 glass body;

(b) keeping the porous TiO 2 —SiO 2 glass body in a reaction vessel that is filled with elemental fluorine (F 2 ) or a mixed gas comprising elemental fluorine (F 2 ) diluted with an inert gas and contains a solid metal fluoride, to thereby obtain a fluorine-containing porous TiO 2 —SiO 2 glass body; and

(c) heating the fluorine-containing porous TiO 2 —SiO 2 glass body to a transparent vitrification temperature, to thereby obtain a fluorine-containing transparent TiO 2 —SiO 2 glass body.

11. The production process according to claim 10 , wherein the solid metal fluoride is sodium fluoride.

12. The production process according to claim 10 , further comprising subjecting the inside of the reaction vessel to a degassing treatment before filling the inside of the reaction vessel with elemental fluorine (F 2 ) or a mixed gas obtained by diluting elemental fluorine (F 2 ) with an inert gas in (b).

13. The production process according to claim 10 , further comprising presintering the porous glass body at from 1,100 to 1,350° C. between (a) and (b).

14. The production process according to claim 10 , wherein (b) is carried out a temperature of 200° C. or less.

15. The production process according to claim 10 , wherein (b) is carried out a temperature of 150° C. or less.

16. The production process according to claim 10 , wherein the inert gas comprises nitrogen, helium or argon.

17. The production process according to claim 10 , wherein the transparent vitrification temperature is within the range of from 1,350 to 1,800° C.

18. The production process according to claim 10 , wherein the transparent TiO 2 —SiO 2 glass body has a fluorine concentration of 3,000 ppm or more.

Assignments (3)
CHANGE OF NAME Recorded Aug 7, 2018
From: ASAHI GLASS COMPANY, LIMITED
To: AGC INC.
Reel/Frame 046730/0786 →
CORPORATE ADDRESS CHANGE Recorded Nov 9, 2011
From: ASAHI GLASS COMPANY, LIMITED
To: ASAHI GLASS COMPANY, LIMITED
Reel/Frame 027197/0541 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 6, 2011
From: TAMITSUJI, CHIKAYA; WATANABE, KUNIO; KOIKE, AKIO
To: ASAHI GLASS COMPANY, LIMITED
Reel/Frame 026081/0296 →