WO2002036510A2 - Method of manufacturing an optical fiber preform - Google Patents
Method of manufacturing an optical fiber preform Download PDFInfo
- Publication number
- WO2002036510A2 WO2002036510A2 PCT/US2001/042464 US0142464W WO0236510A2 WO 2002036510 A2 WO2002036510 A2 WO 2002036510A2 US 0142464 W US0142464 W US 0142464W WO 0236510 A2 WO0236510 A2 WO 0236510A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- core layer
- tubular core
- tubular
- silica
- soot
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/012—Manufacture of preforms for drawing fibres or filaments
- C03B37/014—Manufacture of preforms for drawing fibres or filaments made entirely or partially by chemical means, e.g. vapour phase deposition of bulk porous glass either by outside vapour deposition [OVD], or by outside vapour phase oxidation [OVPO] or by vapour axial deposition [VAD]
- C03B37/01466—Means for changing or stabilising the diameter or form of tubes or rods
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/012—Manufacture of preforms for drawing fibres or filaments
- C03B37/01205—Manufacture of preforms for drawing fibres or filaments starting from tubes, rods, fibres or filaments
- C03B37/01225—Means for changing or stabilising the shape, e.g. diameter, of tubes or rods in general, e.g. collapsing
- C03B37/0124—Means for reducing the diameter of rods or tubes by drawing, e.g. for preform draw-down
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/012—Manufacture of preforms for drawing fibres or filaments
- C03B37/014—Manufacture of preforms for drawing fibres or filaments made entirely or partially by chemical means, e.g. vapour phase deposition of bulk porous glass either by outside vapour deposition [OVD], or by outside vapour phase oxidation [OVPO] or by vapour axial deposition [VAD]
- C03B37/01466—Means for changing or stabilising the diameter or form of tubes or rods
- C03B37/01473—Collapsing
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2201/00—Type of glass produced
- C03B2201/06—Doped silica-based glasses
- C03B2201/30—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi
- C03B2201/31—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi doped with germanium
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2201/00—Type of glass produced
- C03B2201/06—Doped silica-based glasses
- C03B2201/30—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi
- C03B2201/34—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi doped with rare earth metals, i.e. with Sc, Y or lanthanides, e.g. for laser-amplifiers
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2201/00—Type of glass produced
- C03B2201/06—Doped silica-based glasses
- C03B2201/30—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi
- C03B2201/34—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi doped with rare earth metals, i.e. with Sc, Y or lanthanides, e.g. for laser-amplifiers
- C03B2201/36—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi doped with rare earth metals, i.e. with Sc, Y or lanthanides, e.g. for laser-amplifiers doped with rare earth metals and aluminium, e.g. Er-Al co-doped
Definitions
- the present invention relates generally to methods for manufacturing an optical fiber preform, and more particularly to a method of manufacturing an optical fiber preform
- Processing of core cane traditionally includes depositing glass soot upon a rotating substrate to produce a soot tube.
- the soot tube is dried, consolidated and then drawn into a slender core cane. During the drawing process, the centerline hole is generally closed.
- Introducing various gases in predetermined amounts and times into a burner flame produces the desired refractive index profile of the core cane.
- This introduction produces oxides that may include, for example silicon oxide and germanium oxide. These oxides deposit on the rotating mandrel until the appropriate diameter of the core portion is reached.
- silica soot is deposited as the last step in the core cane making process. This layer of silica soot is termed "overcladding" and typically comprises about 95% of the volume of glass present in the soot blank.
- the mandrel is removed from the soot tube thereby leaving an aperture extending along its axial length and positioned at the blank's centerline (hereinafter referred to as the "aperture” or the “centerline aperture”).
- the centerline aperture has a silica plug-like member inserted in its lower end to restrict gas flow therethrough.
- the soot tube is inserted into and held in a consolidation furnace.
- Chlorine and helium gas are included within the furnace, passed through the centerline aperture, and held at a temperature between about 800
- °C -1200 °C to aid in hydrogen removal from the soot preform.
- chlorine permeates the interstices of the soot preform and flushes out any OH, H 2 or H 2 O contained therein.
- the cleaned and dried blank is then heated to a higher temperature, generally in the range of between about 1450 °C to about 1600 °C, (depending upon preform composition) until the deposited soot blank consolidates and transforms into a solid, high-purity glass having superior optical properties.
- the blank is subjected to gradient consolidation, a technique taught whereby the bottom tip is consolidated first; the consolidation continuing along the preform until completed.
- the preform is removed from the furnace and transferred to another furnace where the preform is drawn, under a vacuum, to close the centerline aperture and, in a controlled fashion, stretch the preform into a core cane of a desired diameter.
- the core cane is then cut into segments, each of which is then again overclad with a significant amount of Si0 2 soot to an appropriate diameter and again consolidated thereby resulting in a glass preform which has no aperture and includes the desired amount of cladding surrounding the core.
- the resulting preform is then transferred to a drawing furnace where it is drawn into optical fiber.
- a method of manufacturing an optical fiber preform with lower centerline defects comprises providing a first tubular core layer including silica-containing glass or soot. Outside of the first tubular layer is deposited a doped silica soot thereby forming a second tubular core layer. At least the second tubular core layer is then consolidated (and preferably the first and second tubular layers), and at least part of the first tubular core layer is removed, preferably by exposing the layer to an etchant.
- the first core layer may be, for example, a thin deposited layer of silica soot, germania-doped silica soot, or a silica soot doped with any other glass former.
- the first layer may be a silica-glass containing tube, for example.
- the tube may also include suitable doping with a glass former.
- the soot may be deposited by any known deposition method, such as OVD for example.
- the second core layer preferably includes a rare earth dopant such as Er, Tm, Nd, Pm, Yb, or Sm, for example.
- the second tubular core layer is doped with alumina in an amount of about 1% to15% by weight.
- the second core layer is preferably deposited by an OVD method or the like on the outside of the first layer formed. Following deposition, at least the second layer is dried and consolidated through conventional.
- the etchant used to remove at least part of the first core layer is preferably SF 6 or NF 3 . Although other suitable etchants may be employed.
- the etchant is preferably provided by flowing it through the centerline aperture of the preform. Etching takes place at a temperature between about 1150 °C and 1400 °C. Upon completion of the etching step, preferably less than all of the first tubular layer is etched. away. Thus, it should be recognized that, in accordance with a preferred embodiment a small amount of the first core layer is left unetched.
- This small amount of sacrificial layer remaining prevents, for example, puddling of the rare earth dopants upon closure of the aperture when drawing the consolidated preform into a core cane due to a lesser reactivity of rare earth metals with fluorine.
- Puddling was found by the inventors to occur if the etching step were allowed to remove all the first core layer and some of the second layer.
- Puddling of such rare earth metals, such as Erbium may be detrimental to the optical properties of the resultant fiber drawn from the optical preform. Therefore, it should be recognized that because of the lack of puddling and other centerline defects, fibers produced from preforms manufactured in accordance with the present invention have excellent properties for use in amplifiers and other optical components.
- a method and apparatus wherein greater than 50% of the quantity of glass in the core cane comprises core material.
- greater than 50% of the quantity of glass in the core cane comprises core material. This is accomplished by depositing substantially less silica overcladding prior to the step of drawing into a core cane. More preferably yet, greater than 80% of the quantity of glass in the core cane comprises core material. Even more preferably, greater than 90% comprises core material.
- the first core layer acts as a sacrificial layer and prevents any alumina, preferably present in the second core layer, from coming into direct contact with the alumina bait rod, thus preventing the formation of any defect sites containing alumina resulting when the mandrel is removed.
- an optical fiber core cane having body of silica-containing glass material including a rare earth element having a length greater than 0.5 m and a diameter of greater than 7 mm and that includes greater than 50% core material by volume. This advantageously allows significantly more fiber to be drawn therefrom as compared to the prior art.
- Fig. 1 illustrates a perspective view of a first core soot segment formed on a bait rod.
- Fig. 2 illustrates a perspective view of a second core soot segment deposited on the first core segment.
- Fig. 3 is a cross-sectional end view of a soot preform in accordance with the invention taken along line 3-3 of Fig. 2.
- Fig. 4 illustrates a side cross-sectional view of a soot preform with the bait rod removed and the end plugged.
- Fig. 5 illustrates a partial cross-sectional side view of a soot preform during the drying step.
- Fig. 6 illustrates a partial cross-sectional side view of a vitrified preform during the consolidation step.
- Fig. 7 illustrates a partial cross-sectional side view of a vitrified preform with the bottom portion of the plug removed and whereby the etchant is provided through the centerline aperture.
- Fig. 8 illustrates a cross-sectional end view of an etched preform illustrating an unetched portion of the first layer still remaining.
- Fig. 9 illustrates a partial cross-sectional side view of a draw apparatus for producing a core cane.
- Fig. 10 illustrates a cross-sectional side view illustrating an alternate tubular silica-containing glass tube forming the first core layer.
- Fig. 11 illustrates a side view illustrating the step of depositing of silica- containing soot onto a core cane.
- Fig. 12 illustrates a partial cross-sectional side view of a vitrified preform formed during a consolidation step.
- a first step in the method of manufacturing an optical fiber preform in accordance with the present invention is to provide a first tubular core layer 32 including silica-containing glass or silica-containing soot.
- a slightly tapered alumina bait rod 22 is rotated within a laydown apparatus including a lathe (not shown) for rotating the bait rod and one or more burners 24 (only one being shown).
- a handle 25 is typically provided on one end of the bait rod 22 to facilitate handling in later manufacturing processes to be discussed further herein.
- the handle and/or rod may be grasped by support and chuck portions of the lathe during laydown.
- the burners 24 are provided, for example, with a source 23 of fuel and combustion supporting gas, such as methane and oxygen, respectively.
- the furl is ignited in the presence of oxygen to form a flame 30.
- a first silicon-containing precursor 28 in liquid or vapor form is delivered to the burner 24 and introduced into the flame 30 to form silica-containing soot 26.
- the first precursor 28 may be mixed with other gasses, such as oxygen, or it may be separately provided to the burner 24 if a liquid-type delivery burner is utilized.
- the first tubular core layer 32 in this embodiment is deposited onto the bait rod 22 by an Outside Vapor Deposition (OVD) process.
- the first tubular core layer 32 is preferably less than about 3 mm thick and more preferably less than about 1.0 mm thick.
- the first layer is doped with a glass former, such as germania, such that the viscosity of the fist core layer is reduced to aid in hole closure.
- the first tubular core layer 32 may be alternately formed from a vitrified tubular silica-containing glass tube such as illustrated in Fig. 10.
- the tube comprises a germania doped silica glass.
- a doped silica soot 34 is deposited onto the outside of the first tubular core layer 32 to form a second tubular core layer 36. Similar to the first layer, fuel 23 is provided to burner 24 and ignited. Precursor 29 is provided to the flame 30 and oxidizes to form the doped silica soot 34.
- the composition of the second tubular core layer 36 is different from the first core layer 32.
- the doped silica soot of the second tubular core layer 36 is doped with a rare earth element.
- precursor 29 includes a rare earth element.
- the rare earth element is selected from a group consisting of Er, Tm, Nd, Pm, Yb, and Sm.
- Erbia in concentrations of between about 0.001% and 1.0% are desired in the soot, and more preferably between about 0.01 and 0.5%.
- Alumina in concentrations of 0%- 5% by weight is preferred, and more preferably between about 1.0% and 10% by weight.
- Alumina is added to the second core layer 36 to increase the solubility of the rare earths in glass thereby reducing clustering and also improving the spectroscopy of the rare earth ion.
- Germania is also preferably present in amounts ranging from about 0% to 25% by weight and more preferably in an amount between about 12% to 22% by weight.
- Figs. 2, 3 and 4 respectively, illustrate a cross-sectional views of the soot blank 38 manufactured in accordance with the invention.
- the blank 38 includes the first tubular core layer 32, the second tubular core layer 36 and the handle 25.
- the bait rod 22 is removed, as shown in the Fig. 4, and a plug 40 has been inserted in the end of the blank 38.
- the plug 40 is vitrified silica and includes a larger diameter recessed portion that is inserted into the centerline aperture 42 of the blank.
- the plug 40 also includes a smaller capillary tube 43 at the farthest outward end of the plug.
- the capillary tube 43 allows limited gas flow in the next step as will be described herein.
- the soot blank 38 is installed in a furnace 44.
- the furnace typically includes a muffle tube 46 manufactured from a ultra-pure silica material, insulation 48, and a heat source 50 such as induction coils shown.
- the blank 38 is first dried at a temperature between about 875°C and 950°C for about 2 hours in the presence of an atmosphere of drying gas 52 such as a mixture of helium and chlorine gasses.
- the gasses are present in about 94%-100% helium and 0%-5% chlorine.
- the gasses are passed into the centerline aperture 42 where they disperse out through the soot interstices.
- the drying gasses may be provided between the soot blank 38 in the muffle tube 46 thereby surrounding the blank, if desired.
- the blank 38 is suitably dried, it is consolidated into a solid vitrified glass mass; preferably in the same furnace 44 as shown in Fig. 5.
- the second tubular core layer 36 (Fig. 4) of the blank 38 is consolidated.
- both the first and second tubular layers 32, 36 are consolidated in the furnace 44 as shown in Fig. 6.
- Consolidation takes place at about between 1350 °C and 1500 °C, and most preferably at about 1430 °C for about 4 hours in the presence of an inert consolidation gas 54 such as helium or argon. Consolidation is preferably carried out by a gradient consolidation method where the blank is lowered through a hot zone. The now consolidated preform 55 is quickly withdrawn from the furnace
- plug portion 40a This leaves a larger diameter through hole and removes the capillary tube on the lower end of the preform 55 for better etchant flow and access as shown in Fig. 7.
- the preform 55 is quickly lowered back into the furnace 44 and then a supply of etchant 56 is directed into and through the centerline aperture 42 as shown by the arrows labeled "A" to expose the surface of the first tubular layer
- the etchant 56 is preferably a gas with a high degree of reactivity with oxide based glasses.
- the etchant 56 most preferably is a gas selected from a group consisting of SF 6 and NF 3 .
- the most preferred etchant is SF ⁇ and is supplied at the centerline at a flow rate of about 75 standard cubic centimeters per minute.
- the etchant gas is included with a carrier gas 58, such as helium.
- the etchant 56 is included in a range of amounts between about 5.0 % and about 25%, and most preferably about 18%, and helium is provided in a range between about 75 % to about 95%, and most preferably in about 82% by volume.
- the etchant 56 is included in a range of amounts between about 5.0 % and about 25%, and most preferably about 18%, and helium is provided in a range between about 75 % to about 95%, and most preferably in about 82% by volume.
- the layer 56 performs the function of etching away at least part of the first tubular core layer 32.
- the layer is about 40 microns thick. It is preferable to etch away between about 80% and 95% of the first tubular layer 32, i.e., less than the entire layer 32 upon completion of the etching step.
- part of the first core layer preferably remains after etching.
- the first layer 32 includes germania
- a portion of a germania doped glass of the first .tubular core layer remains after etching. This remaining layer prevents inconsistent etching of the constituents in the second tubular core layer.
- the step of etching preferably occurs at an etching temperature between about 1150 °C and 1400 °C, and most preferably between about 1150 °C and 1250 °C within the furnace 44.
- Fig. 8 illustrates a cross section of the consolidated preform
- the consolidated core blank 55 is transferred to a draw furnace 64 wherein a step of drawing the consolidated core blank 55 into a core cane 62 takes place. Drawing takes place at a temperature between about 1600 °C and 1800 °C in an atmosphere of an inert gas, such as helium.
- a vacuum may be applied while drawing, preferably about 100 Torr, to close the centerline aperture 42.
- Tension capstans 67 one or both of which are motor driven (motor not shown), provide a suitable tension force to draw from the core preform 55, a core cane to a desired dimension "d" of about 9 mm.
- Suitable controls 72 receive a signal indicative of the diameter "d" via a non- contact sensor 68 and control the capstan rate and down feed rate 70 of the core blank 55 such that the desired diameter is maintained.
- a cutter mechanism 72 such as a flame burner, cuts the canes to the desired length.
- greater than 50% of the quantity of glass in the core cane comprises core material. This is accomplished by depositing significantly less silica overcladding prior to the step of drawing into a core cane.
- core material what is referred to herein is the physical core, i.e., that portion of the core cane that, when drawn into a fiber, will be the light carrying region. More preferably yet, greater than 80% of the quantity of glass in the core cane comprises core material and most preferably, greater than 90% of the quantity of glass in the core cane comprises core material.
- a method of manufacturing an optical fiber preform comprising the steps of forming a body of silica-containing soot 38 including a tubular core layer 36 of doped silica soot, the tubular core layer being doped with a rare earth element, the body having a centerline aperture 42, consolidating at least the tubular core layer to form a consolidated core blank 55, and drawing the consolidated core blank and closing the centerline aperture to form a core cane 62 that includes greater than 50% core material by volume.
- an optical fiber core cane is provided that comprises a body of silica containing glass material including a rare earth element. The length of the core cane 62 is greater than 0.5 m and has a diameter of greater than 7.0 mm. The resultant core cane includes greater than 50% core material by volume.
- silica-containing cladding soot 76 is formed by passing a precursor 82, such as SiCI , into a flame of a burner 24.
- a precursor 82 such as SiCI
- the oxidized soot 76 is deposited onto the core cane 62 to form a soot preform 80 having a cladding layer 78.
- a handle 25 may be included on one end of the preform 80 as heretofore described.
- the soot is preferably dried as described with reference to the method of Fig. 5 and an additional step of consolidating the soot preform 80 preferably takes place.
- the preferably previously dried soot preform is placed into a consolidation furnace 44.
- Consolidation gas 54 such as helium, is provided to the soot preform.
- the temperature inside the furnace is increased to between about 1400 °C and 1550 °C for about 4 hours. After this period, the soot has vitrified into a high-purity glassy mass including the core 62 and cladding 78 and collectively referred to herein as the consolidated preform 84.
- This preform 84 is ultimately placed in a draw furnace and optical fiber is drawn therefrom.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
- Glass Compositions (AREA)
Abstract
Description
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP01977897A EP1337484A2 (en) | 2000-11-01 | 2001-10-05 | Method of manufacturing an optical fiber preform |
| AU2001296980A AU2001296980A1 (en) | 2000-11-01 | 2001-10-05 | Method of manufacturing an optical fiber preform |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US70400600A | 2000-11-01 | 2000-11-01 | |
| US09/704,006 | 2000-11-01 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2002036510A2 true WO2002036510A2 (en) | 2002-05-10 |
| WO2002036510A3 WO2002036510A3 (en) | 2002-07-11 |
Family
ID=24827683
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2001/042464 Ceased WO2002036510A2 (en) | 2000-11-01 | 2001-10-05 | Method of manufacturing an optical fiber preform |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP1337484A2 (en) |
| AU (1) | AU2001296980A1 (en) |
| WO (1) | WO2002036510A2 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006071865A3 (en) * | 2004-12-23 | 2006-08-24 | Nextrom Holding Sa | Method and apparatus for manufacturing an optical fiber core rod |
| WO2009134385A1 (en) * | 2008-04-30 | 2009-11-05 | Corning Incorporated | Process for preparing an optical preform |
| EP3450409A1 (en) * | 2017-08-29 | 2019-03-06 | Corning Incorporated | Method and furnace for preparing an optical fiber preform using etchant and neutralizing gases |
| NL2019811B1 (en) * | 2017-08-29 | 2019-03-11 | Corning Inc | Gas system for furnace |
| US11072560B2 (en) | 2017-08-29 | 2021-07-27 | Corning Incorporated | Neutralizing gas system for furnace |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1187291A (en) * | 1982-07-26 | 1985-05-21 | George E. Berkey | Method of making glass optical fiber |
| CA1263807A (en) * | 1985-03-19 | 1989-12-12 | Richard James Pilon | Optical waveguide manufacture |
| US4810276A (en) * | 1987-08-05 | 1989-03-07 | Corning Glass Works | Forming optical fiber having abrupt index change |
| US5152818A (en) * | 1990-11-09 | 1992-10-06 | Corning Incorporated | Method of making polarization retaining fiber |
| EP1061055A4 (en) * | 1998-02-03 | 2006-11-15 | Sumitomo Electric Industries | METHOD FOR MANUFACTURING BASIC MATERIAL FOR OPTICAL FIBERS |
| DE60025823T2 (en) * | 1999-04-26 | 2006-08-03 | Corning Incorporated | OPTICAL WAVEGUIDE FIBER WITH LOW WATER PEAK AND METHOD FOR THE PRODUCTION THEREOF |
-
2001
- 2001-10-05 WO PCT/US2001/042464 patent/WO2002036510A2/en not_active Ceased
- 2001-10-05 AU AU2001296980A patent/AU2001296980A1/en not_active Abandoned
- 2001-10-05 EP EP01977897A patent/EP1337484A2/en not_active Withdrawn
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006071865A3 (en) * | 2004-12-23 | 2006-08-24 | Nextrom Holding Sa | Method and apparatus for manufacturing an optical fiber core rod |
| GB2435589A (en) * | 2004-12-23 | 2007-08-29 | Nextrom Holding Sa | Method and apparatus for manufacturing an optical fiber core rod |
| GB2435589B (en) * | 2004-12-23 | 2010-08-25 | Nextrom Holding Sa | Method and apparatus for manufacturing an optical fiber core rod |
| WO2009134385A1 (en) * | 2008-04-30 | 2009-11-05 | Corning Incorporated | Process for preparing an optical preform |
| US8815103B2 (en) | 2008-04-30 | 2014-08-26 | Corning Incorporated | Process for preparing an optical preform |
| EP3450409A1 (en) * | 2017-08-29 | 2019-03-06 | Corning Incorporated | Method and furnace for preparing an optical fiber preform using etchant and neutralizing gases |
| NL2019811B1 (en) * | 2017-08-29 | 2019-03-11 | Corning Inc | Gas system for furnace |
| US11072560B2 (en) | 2017-08-29 | 2021-07-27 | Corning Incorporated | Neutralizing gas system for furnace |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2001296980A1 (en) | 2002-05-15 |
| WO2002036510A3 (en) | 2002-07-11 |
| EP1337484A2 (en) | 2003-08-27 |
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