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US4681615A Expired / Lapsed US ⏱️ 0.0 years remaining

Silica glass formation process

Assignee: A Co OF JAPAN KK
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Filing: 1983-12-22
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Granted: 1987-07-21
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Expires: 2003-12-22
📄 Original PDF 🌐 Google Patents

Abstract

Abstract PCT No. PCT/JP83/00450 Sec. 371 Date Aug. 20, 1984 Sec. 102(e) Date Aug. 20, 1984 PCT Filed Dec. 22, 1983 PCT Pub. No. WO84/02519 PCT Pub. Date Jul. 5, 1984.A process for forming monolithic silica glass articles is provided. The process includes the steps of hydrolyzing silicon alkoxide to form a hydrolyzed solution, adding fumed silica to the hydrolyzed silicon alkoxide solution to yield a sol solution, gelling the sol solution to a gel, and drying and sintering the gel to obtain the monolithic silica glass articles.

Inventors

  • 👤 Motoyuki Toki
  • 👤 Sadao Kanbe
  • 👤 Satoru Miyashita
  • 👤 Tetsuhiko Takeuchi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 23:25
CPC Classifications
C; C03; C03C; C03C1/00; C03C1/006; C03B; C03B19/00; C03B19/12; C03C3/00; C03C3/04; C03C3/06; C03C2201/00; C03C2201/02; C03C2203/00; C03C2203/20; C03C2203/26; C03C2203/34; Y; Y02; Y02P; Y02P40/00; Y02P40/50; Y02P40/57; Y10; Y10S; Y10S65/00; Y10S65/901

Claims Analysis

Total Claims: 22
Claim 1
Independent Claim 89 words
A process for forming a monolithic silica glass article, comprising; hydrolyzing a silicon alkoxide in solution to form a hydrolyzed solution; adding fumed silica to the hydrolyzed solution in an amount between about 0.2 to 5 mols of silica per mol of silicon alkoxide to form a sol solution; gelling the sol solution to form a gel; drying the gel to a dry gel; and sintering the dry gel at a temperature effective to form a glass in order to form a large monolithic silica glass article without cracking.
Claim 2
Dependent Claim 89 words
A process for forming a monolithic silica glass article, comprising; hydrolyzing a silicon alkoxide in solution to form a hydrolyzed solution; adding fumed silica to the hydrolyzed solution in an amount between about 0.2 to 5 mols of silica per mol of silicon alkoxide to form a sol solution; gelling the sol solution to form a gel; drying the gel to a dry gel; and sintering the dry gel at a temperature effective to form a glass in order to form a large monolithic silica glass article without cracking.
Claim 3
Dependent Claim 19 words
The process of claim 1, wherein the fumed silica is formed by hydrolyzing SiCl 4 with an oxy-hydrogen flame.
Claim 4
Dependent Claim 16 words
The process of claim 1, wherein said fumed silica is derived from a sodium silicate solution.
Claim 5
Dependent Claim 18 words
The process of claim 1, wherein said fumed silica is obtained by hydrolyzing a silicon alkoxide with ammonia.
Claim 6
Dependent Claim 22 words
The process of claim 1, further including the step of uniformly dispersing the fumed silica in the sol solution by ultrasonic vibration.
Claim 7
Dependent Claim 28 words
The process of claim 1, further including the step of dispersing the fumed silica in the sol solution by centrifugal separation to insure uniform dispersion of fumed silica.
Claim 8
Dependent Claim 12 words
The process of claim 1, wherein the silicon alkoxide is silicon ethoxide.
Claim 9
Dependent Claim 17 words
The process of claim 1, wherein the hydrolyzed silicon alkoxide is silicon ethoxide hydrolyzed with hydrochloric acid.
Claim 10
Dependent Claim 27 words
The process of claim 1, including the step of adjusting the pH of the sol solution to between about 3 and 6 by addition of a base.
Claim 11
Dependent Claim 25 words
The process of claim 1, wherein the pH of the sol solution is adjusted to between about 4 to 4.5 by addition of a base.
Claim 12
Dependent Claim 17 words
The process of claim 9, wherein the base is any one of ammonia and an organic base.
Claim 13
Dependent Claim 22 words
The process of claim 11, wherein the ammonia is selected from the group of ammonia water, ammonia gas and an ammonia solution.
Claim 14
Dependent Claim 33 words
The process of claim 11, wherein the organic base is selected from the group of triethylamine, an aqueous solution of triethylamine, pyridine, an aqueous solution of pyridine, aniline or an aqueous aniline solution.
Claim 15
Dependent Claim 50 words
The process of claim 1, further including the step of drying the sol solution to a gel, and drying the gel to a dry gel in a mold having a lid covering the mold, said lid formed with aperatures comprising less than 50% of the surface area of the lid.
Claim 16
Dependent Claim 36 words
The process of claim 9, wherein the sol solution is gelled in a mold having a lid covering the mold and formed with openings comprising less than about 20% of the surface area of the lid.
Claim 17
Dependent Claim 37 words
The process of claim 1, wherein the gel is formed at temperatures between about 5° to 60° C. and the gel is dried to a dry gel at a drying temperature between about 20° to 120° C.
Claim 18
Dependent Claim 24 words
The process of claim 16, wherein the gel is heated to the drying temperature at a rate less than about 120° C. per hour.
Claim 19
Dependent Claim 30 words
The process of claim 1, wherein the sintering of the dry gel includes the steps of (a) removing absorbed water; (b) removing carbon and (c) making the dry gel non-porous.
Claim 20
Dependent Claim 57 words
The process of claim 18, including at least one heating step of removing absorbed water by heating the dry gel to a first selected temperature between about 20° and 400° C. at a heating rate of less than 400° C. per hour and maintaining the dried gel at the selected temperature for at least about one hour.
Claim 21
Dependent Claim 60 words
The process of claim 19, further including at least one heating step of removing carbon by heating the dry gel to a second selected temperature between about 400° and 1200° C. at a heating rate of between about 30° to 400° C. per hour and maintaining the second selected temperature for a period of more than at least 3 hours.
Claim 22
Dependent Claim 47 words
The process of claim 20, further including at least one heating step of making the dry gel non-porous by heating the dry gel to a third selected temperature between about 1000° and 1400° C. at a heating rate of between about 30° and 400° C. per hour.

References Cited (Backward Citations)

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US4317668A Cited
GB2075003A Cited
JPS5722130A Cited
JPS5722129A Cited
GB2103202A Cited
JPS5826048A Cited
US4419115A Cited
US4472510A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-07-20 1991-01-19 1991-07-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-07-20 1995-01-19 1995-07-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-07-20 1999-01-19 1999-07-21 $7700.00 Window Closed / Lapsed

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