# US 5,344,475 A · Manufacture of high proof-test optical fiber using sol-gel

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- Number: US 5,344,475 A
- Document ID: US5344475A
- Status: Granted
- Kind: A
- Application number: 08/029,750
- Filed: 1993-03-11
- Granted: 1994-09-06
- Earliest claimed: 1993-03-11
- Assignees: AT&T Bell Laboratories
- Inventors: Suhas D. Bhandarkar; Harish C. Chandan; David W. Johnson, Jr.; John B. MacChesney
- Web page: https://patentgrep.com/patent/US5344475A

## CPC

- C03B 37/016: by a liquid phase reaction process, e.g. through a gel phase
- Y10S 65/901: Liquid phase reaction process
- C03B: MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- Y10S: TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

## Abstract

Optical fiber drawn from preforms including sol-gel-derived glass is found to contain small refractory particles of the order of a micron in size. These particles initiate fiber breaks with the result that fiber may not meet proof-test tensile strength requirements. An effective separation method relies upon density and/or size difference from suspended sol particles for separation in the ungelled sol. A preferred separation procedure is centrifugation.

## Claims

### Claim 1

Process for fabrication of optical fiber in accordance with which fiber is drawn from a preform comprising a sol-gel body, in which the sol-gel body is prepared by gelation of a sol followed by drying to a porous body and finally by sintering, and in which the sol comprises suspension particles of SiO.sub.2 in water, in which suspension particles are primarily of size within the range of from 0.005 .mu.m to 0.2 .mu.m
CHARACTERIZED in that the sol is further processed to remove contaminant particles on the basis of at least one characteristic selected from the group consisting of density greater than that of such suspension particles and size larger than that of such suspension particles, in which further processing comprises centrifugation, settling, or filtration, and in which further processing results in substantial separation of refractory particles, in which refractory refers to particles which are not assimilated in resulting fiber.

### Claim 2 (depends on 1)

Process of claim 1 in which further processing comprises centrifugation.

### Claim 3 (depends on 2)

Process of claim 2 in which centrifugation results in substantial separation both of refractory particles and of any agglomerates of size.gtoreq.2 .mu.m of suspension particles.

### Claim 4 (depends on 3)

Process of claim 3 in which refractory particles include at least one composition selected from the group consisting of ZrO.sub.2, TiO.sub.2, and Cr.sub.2 O.sub.3.

### Claim 5 (depends on 1)

Process of claim 1 in which the sol-gel body is tubular, and in which the preform consists essentially of a rod-shaped body encompassed by such sol-gel body.

### Claim 6 (depends on 5)

Process of claim 5 in which such sol-gel body as sintered is a self-supporting tubular body into which such rod-shaped body is inserted to result in the preform.

### Claim 7 (depends on 6)

Process of claim 6 in which such rod-shaped body is prepared by a procedure selected from the group consisting of Modified Chemical Vapor Deposition and a soot process, further in which such soot process is selected from the group consisting of Vapor Axial Deposition and Outside Vapor Deposition.

### Claim 8 (depends on 5)

Process of claim 5 in which such sol-gel body is sintered in the presence of an inserted rod-shaped body.