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US4640699A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing glass product having gradient of refractive index

Assignee: Hoya Corp
•
Filing: 1985-04-03
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Granted: 1987-02-03
•
Expires: 2005-04-03
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Abstract

Abstract A process for producing a glass product having Δn, the difference between the central and peripheral portions of the glass, greater than 0.04. This process utilizes a porous glass body which is produced via a phase separation technique. A dopant selected from the group consisting of (1) TlNO 3 , (2) TlNO 3 and an alkali metal compound and (3) TlNO 3 , Pb(NO 3 ) 2 and an alkali metal compound is then permeated into the micropores of the porous glass product. A concentration gradient of the dopant is then formed by leaching out a portion of the dopant from the micropores. After the dopant is solidified in the mircopores, the porous glass product is dried. A heat-treatment step then serves to collapse the micropores. A glass product having a gradient of refractive indices is therby obtained.

Inventors

  • 👤 Shigeaki Ohmi
  • 👤 Seiichi Shingaki
  • 👤 Hiroyuki Sakai
  • 👤 Yoshiyuki Asahara

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 08:53
CPC Classifications
C; C03; C03C; C03C23/00; C03C23/0095; C03B; C03B19/00; C03B19/12; C03B37/00; C03B37/01; C03B37/012; C03B37/014; C03B37/016; C03C13/00; C03C13/04; C03B2201/00; C03B2201/06; C03B2201/30; C03B2201/50

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 246 words
A process for producing a glass product having a gradient of refractive indices and transparent without turbidity which comprises: (a) producing a porous glass body by: (1) heating a glass body to effectuate a phase separation; (2) leaching out the acid-soluble phase from said glass body; and then (3) recovering therefrom the porous glass body; (b) premeating a solution of dopant into the micropores of said porous glass product wherein said dopant is selected from the group consistin of (1) TlNO 3 , the concentration of TlNO 3 in the dopant solution being about 80 g/100 ml of H 2 O or less, (2) TlNO 3 and an alkali metal compound, the concentration of TlNO 3 in the dopant solution being about 100 to 400 g/100 ml of H 2 O, and (3) TlNO 3 , Pb(NO 3 ) 2 and an alkali metal compound, the concentration of TlNO 3 in the dopant solution being about 100 to 400 g/100 ml of H 2 O, (c) leaching out a portion of the dopant from the micropores with or without solidifying the dopant in the micropores to form a concentration gradient of the dopant in said porous glass product; (d) solidifying the dopant in the micropores, (e) drying the porous glass product, (f) heat treating said porous glass product to collapse the micropores, and (g) recovering a glass having Δn greater than 0.04 wherein Δn is the difference between the central and peripheral portions of the glass.
Claim 2
Dependent Claim 246 words
A process for producing a glass product having a gradient of refractive indices and transparent without turbidity which comprises: (a) producing a porous glass body by: (1) heating a glass body to effectuate a phase separation; (2) leaching out the acid-soluble phase from said glass body; and then (3) recovering therefrom the porous glass body; (b) premeating a solution of dopant into the micropores of said porous glass product wherein said dopant is selected from the group consistin of (1) TlNO 3 , the concentration of TlNO 3 in the dopant solution being about 80 g/100 ml of H 2 O or less, (2) TlNO 3 and an alkali metal compound, the concentration of TlNO 3 in the dopant solution being about 100 to 400 g/100 ml of H 2 O, and (3) TlNO 3 , Pb(NO 3 ) 2 and an alkali metal compound, the concentration of TlNO 3 in the dopant solution being about 100 to 400 g/100 ml of H 2 O, (c) leaching out a portion of the dopant from the micropores with or without solidifying the dopant in the micropores to form a concentration gradient of the dopant in said porous glass product; (d) solidifying the dopant in the micropores, (e) drying the porous glass product, (f) heat treating said porous glass product to collapse the micropores, and (g) recovering a glass having Δn greater than 0.04 wherein Δn is the difference between the central and peripheral portions of the glass.
Claim 3
Dependent Claim 14 words
The process of claim 1, wherein the alkali metal compound is CsNO 3 .
Claim 4
Dependent Claim 30 words
The process of claim 1, wherein a solvent for the dopant is selected from the group consisting of water, an organic solvent, and a mixture of water and organic solvent.
Claim 5
Dependent Claim 34 words
The process of claim 3, wherein when the dopant is (1) TlNO 3 , the concentration of TlNO 3 in the dopant solution is about 80 g/100 ml of H 2 O or less.
Claim 6
Dependent Claim 26 words
The process of claim 1, wherein the concentration of TlNO 3 in the dopant solution is about 60 to 80 g/100 ml of H 2 O.
Claim 7
Dependent Claim 57 words
The process of claim 3, wherein when the dopant is (2) TlNO 3 and an alkali metal compound, the concentration of TlNO 3 in the dopant solution is about 100 to 400 g/100 ml of H 2 O and the concentration of said alkali metal compound is about 20 g/100 ml of H 2 O or greater.
Claim 8
Dependent Claim 24 words
The process of claim 6, wherein the concentration of said alkali metal compound is about 100 to 200 g/100 ml of H 2 O.
Claim 9
Dependent Claim 81 words
The process of claim 3, wherein when the dopant is (3) TlNO 3 , Pb(NO 3 ) 2 and an alkali metal compound, the concentration of TlNO 3 in the dopant solution is about 100 to 400 g/100 ml of H 2 O, the concentration of said Pb(NO 3 ) 2 is about 20 g/100 ml of H 2 O or greater, and the concentration of said alkali metal compound is about 20 g/100 ml of H 2 O or greater.
Claim 10
Dependent Claim 44 words
The process of claim 8, wherein the concentration of said Pb(NO 3 ) 2 is about 80 to 120 g/100 ml of H 2 O, and the concentration of said alkali metal compound is about 100 to 200 g/100 ml of H 2 O.

References Cited (Backward Citations)

US4225330A Cited
US4528010A Cited
US4389233A Cited
US4525189A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-02-02 1990-08-04 1991-02-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-02-02 1994-08-04 1995-02-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-02-02 1998-08-04 1999-02-03 $7700.00 Window Closed / Lapsed

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