EP0169237A1

EP0169237A1 - Glass fiber splicing by flame fusion

Info

Publication number: EP0169237A1
Application number: EP19850900883
Authority: EP
Inventors: John Thorvald Krause
Original assignee: American Telephone and Telegraph Co Inc; AT&T Corp
Current assignee: AT&T Corp
Priority date: 1984-01-24
Filing date: 1985-01-15
Publication date: 1986-01-29
Also published as: DE3562136D1; EP0150095B1; JPS61501172A; EP0150095A3; EP0150095A2; WO1985003283A1

Abstract

Dans le but d'obtenir des connexions d'épissure de haute résistance entre des fibres de verre à base de silice, un procédé d'utilisation d'un écoulement tripartite de gaz pour une fusion à la flamme est décrit. Un écoulement d'oxygène externe de vitesse relativement élevée (5) entoure un écoulement de chlore ou d'oxygène intermédiaire de vitesse plus lente (3) qui à son tour entoure un écoulement central de H2, D2, NH3, ou ND3 (1). En particulier, des résistances élevées sont obtenues lorsqu'un écoulement central d'hydrogène ou de deutérium et un écoulement intermédiaire de chlore sont utilisés de sorte que les extrémités des fibres à épisser sont chauffées à des températures de 500oC et au delà uniquement après avoir enveloppé ces extrémités par du chlore.In order to obtain high strength splice connections between silica-based glass fibers, a method of using a tripartite gas flow for flame fusion is described. A relatively high velocity external oxygen flow (5) surrounds a slower velocity intermediate chlorine or oxygen flow (3) which in turn surrounds a central flow of H2, D2, NH3, or ND3 (1) . In particular, high resistances are obtained when a central flow of hydrogen or deuterium and an intermediate flow of chlorine are used so that the ends of the fibers to be spliced are heated to temperatures of 500oC and beyond only after having wrapped these ends by chlorine.

Description

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GLASS FIBER SPLICING BY FLAME FUSION

1. Field of the Invention

The invention is concerned with connecting glass fibers and, more particularly, with producing high-strength splice connections of lightguide glass fibers by heat fusion. Background of the Invention

Lightwave communications via lightguide glass fibers is widely considered as virtually certain to replace most of current electrical communications over copper wire, and the manufacture of optical fibers has reached a high level of perfection. Fabrication aspects such as the making of preforms, the drawing of fibers, their coating and sheathing, and their interconnection are highly advanced.

Still, certain areas of manufacture are open to further improvement; e.g., it has been realized that tensile strength of a glass fiber is adversely affected by exposure to water-derived species at elevated temperatures as disclosed in U. S. patent application Serial No. 300,108, filed September 8, 1981 and in continuation application Serial No. 558,995, filed December 7, 1983.

Particular attention is due, therefore, the way glass fibers are connected by splicing such as, in particular, by heat fusion splicing. Summary of the Invention

The invention is a method for splicing glass fibers by heat fusion. The method involves the use of a tri-partite flow of gases, namely, an outer, relatively high-velocity oxygen flow, an intermediate, lower-velocity chlorine or oxygen flow, and a central flow of H2, D2, H3 or ND3. Resulting spliced fibers have a yield strength which is at least 60 percent of pristine strength.

Brief Description of the Drawing

The Figure is a schematic cross-sectional view of a triple-orifice nozzle of a torch as may be conveniently used to practice the invention. Detailed Description

The Figure shows central orifice 1 , intermediate orifice 3, and outer orifice 5 of a triple nozzle having coaxial cylindrical nozzles 2, 4, and 6. Each of the orifices 1, 3, and 5 can be connected to a gas supply to produce a corresponding flow out of each respective orifice. The outer diameter of the outermost nozzle 6 is typically of the order of 0.5 centimeter.

The invention is aimed at producing high-strengt splice connections between glass fibers, as are being used, e.g., in optical communications. Such fibers have a surface glass portion which preferably comprises at least 95 weight percent silica, and their diameter is of the order of 100 micrometers. Optical fibers typically comprise a core portion having a refractive index which is slightly greater than the refractive index of a surrounding claddi-ng portion; in the case of fibers for th transmission of a single optical mode the diameter of the core portion may be of the order of 10 micrometers. Raise refractive index of a core portion is conveniently achieve by doping such as, e.g., by the addition of germanium to silica. Processing in accordance with the invention call for bringing essentially coaxially aligned glass fibers into end-to-end contact and heating in a flame which is produced upon combustion in a flow of gases. This flow preferably comprises three portions as produced, e.g., by nozzle as shown in the Figure and as may be designated outer, intermediate, and central portions. The outer flow portion preferably is at least 50 volume percent oxygen, the intermediate flow portion is preferably at least 50 volume percent chlorine, oxygen, or a mixture of chlorine and oxygen, and the central flow portion is preferably at least 50 volume percent hydrogen, ammonia, deuterium, deuterated ammonia, or a mixture thereof. (Chlorine is essentially precluded as a constituent of th intermediate flow portion when the central flow portion comprises appreciable amounts of H3 or D3. ) Preferred are 90 volume percent in each of the three flow portions. Characteristically, velocity of flow in the oute flow portion is greater than velocity in the intermediate flow portion, preferred velocity being at least twice and preferably ten times the velocity in the intermediate flow. Such velocity differential is considered to be beneficial in that it serves to make the flame more narrow. Also, rapidly flowing outer oxygen results in desirable cooling of the fiber away from the ends of the fibers being spliced.

A splice connection is produced in accordance with the invention by heating in a flame produced upon combustion in a flow having portions as described above. The temperature of fiber ends being joined preferably does not exceed 1800 degrees C or, more favorably, does not exceed 1700 degrees C. Temperature control is most readil achieved by regulating flow through the central orifice. Fusion time depends indirectly on fusion temperature and directly on fiber diameter; fusion times in the range of from 15 seconds to 2 minutes are typical.

Splice connections made in accordance with the invention produce a spliced fiber having a preferred tensile strength which is greater than or equal to 60 percent of pristine fiber strength (the tensile strengt of fibers or the lesser of the tensile strengths of fibers being joined). Particularly high strengths of at least 95 percent of pristine strength are achieved when the inne flow is essentially hydrogen or. deuterium and the intermediate flow is essentially chlorine and if care is taken to prevent excessive heating of fiber ends prior to their being inside of the chlorine flow. This is conveniently achieved by initially keeping central hydroge flow at a low rate so that a preferred temperature of 500 degrees C is not exceeded until after fiber ends are within the chlorine flow. For fibers consisting essentially of fused silica (typically doped at least in part for optical purposes), resulting fiber strengths are greater than or equal to 800 kpsi. Example. Two essentially identical single-mode optical fibers were spliced by heat fusing in accordance with the invention. The fibers had Ge-doped cores having a diamete of approximately 10 micrometers and essentially pure silic claddings. Overall fiber diameter was 125 micrometers. The ends of the fibers were placed end-to-end and exposed to a flame produced by a torch having three concentric orifices. Essentially pure oxygen flowing at a rate resulting in a velocity of flow of approximately 10 meters per second was fed to the outer orifice, essentially pure chlorine flowing at a rate resulting in a velocity of flow of approximately 0.6 meters per second was fed to the intermediate orifice, and essentially pure hydrogen was fe to the central orifice. Initial hydrogen flow was adjuste just sufficient to maintain a flame and, after placing the fibers in the flame, hydrogen flow was increased for fusing. A temperature of approximately 1700 degrees C was maintained for approximately 90 seconds, and the spliced fiber was removed from the flame. Tensile strength of the resulting combined fiber was determined to be approximatel (800 kpsi).

Claims

1. Method for making a glass fiber which here is designated as a spliced fiber, said method comprising a step of connecting at least a first glass fiber and a second glass fiber, said first and said second glass fibers comprising respective surface portions which consist of at least 95 weight percent silica, said step of connecting comprising heating an end portion of said first fiber and an end portion of said second fiber while said end portion of said first fiber is in contact and essentially aligned with said end portion of said second fiber, said heating being in a flame which results upon combustion in a flow of gases, CHARACTERIZED BY said flow comprising an outer flow portion, an intermediate flow portion which is interior to said outer flow portion, and a central flow portion which is interior to said intermediate flow portion, said outer flow portion comprising at least 50 percent by volume oxygen, said intermediate flow portion comprising at least 50 percent by volume of a gas selected from the group consisting of chlorine, oxygen, and a mixture of chlorine and oxygen, said central flow portion comprising at least 50 percent by volume of a gas or mixture of gases selected from the group of hydrogen, deuterium, NH3, and ND3, and the velocity of the flow of said outer flow portion being greater than the velocity of the flow of said intermediate flow portion, whereby said spliced fiber has a tensile strength which is at least 60 percent of pristine strength.

2. Method according to claim 1, CHARACTERIZED IN THAT the velocity of the flow of said outer flow portion is at least twice the velocity of the flow of said intermediate flow portion.

3. Method according to claim 1 or 2, CHARACTERIZED BY '^' adjusting a flow rate in said outer flow portion to result in a velocity of the flow greater than or equal to 5 meters per second.

4. Method according to claim 1 or 2 or 3, CHARACTERIZED BY adjusting a flow rate in said intermediate flow portion to result in a velocity of the flow greater than or equal to 0.1 meters per second.

5. Method according to claim 4, CHARACTERIZED BY said flow rate in said intermediate flow portion results in a velocity of the flow which is less than or equal to 1 meter per second.

6. Method according to any one of preceding claims 1-5

CHARACTERIZED BY adjusting a flow rate in said central flow portion such that the temperature of said first end portion and said second end portion is less than or equal to 1800 degrees C.

7. Method according to claim 6, CHARACTERIZED BY adjusting said flow rate in said central flow portion first to result in the temperature sufficient to maintain a temperature not exceeding about 500°C until the fiber ends are within the intermediate, chlorine flow, and then increasing the flow rate of said central flow portion to fuse the fiber ends.

8. Method according any one of preceding claims 1-7

CHARACTERIZED IN THAT said inner flow portion is essentially hydrogen or deuterium, said intermediate flow portion is essentially chlorine, and said tensile strength is at least 95 percent f of pristine strength.

9. Method according to claim 8, 5 CHARACTERIZED IN THAT said fiber consists essentially of fused silica and said tensile strength is at least 5,515,816 Pa (800 kpsi) .

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