WO2004108616A1 - Verfahren zum elongieren und kollabieren einer vorform aus quarzglas - Google Patents
Verfahren zum elongieren und kollabieren einer vorform aus quarzglas Download PDFInfo
- Publication number
- WO2004108616A1 WO2004108616A1 PCT/EP2004/005991 EP2004005991W WO2004108616A1 WO 2004108616 A1 WO2004108616 A1 WO 2004108616A1 EP 2004005991 W EP2004005991 W EP 2004005991W WO 2004108616 A1 WO2004108616 A1 WO 2004108616A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- hollow cylinder
- core rod
- core
- quartz glass
- optical component
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 59
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 31
- 230000003287 optical effect Effects 0.000 claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 claims abstract description 13
- 230000008569 process Effects 0.000 claims description 18
- 239000013307 optical fiber Substances 0.000 claims description 12
- 238000000227 grinding Methods 0.000 claims description 8
- 238000012545 processing Methods 0.000 claims description 8
- 238000013461 design Methods 0.000 claims description 6
- 238000005530 etching Methods 0.000 claims description 5
- 238000007920 subcutaneous administration Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000000835 fiber Substances 0.000 abstract description 17
- 239000004071 soot Substances 0.000 description 11
- 238000005253 cladding Methods 0.000 description 9
- 239000011521 glass Substances 0.000 description 9
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 8
- 238000002474 experimental method Methods 0.000 description 5
- 229910004298 SiO 2 Inorganic materials 0.000 description 4
- YBMRDBCBODYGJE-UHFFFAOYSA-N germanium dioxide Chemical compound O=[Ge]=O YBMRDBCBODYGJE-UHFFFAOYSA-N 0.000 description 4
- 208000005156 Dehydration Diseases 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000003746 surface roughness Effects 0.000 description 3
- 229910005793 GeO 2 Inorganic materials 0.000 description 2
- 229910003902 SiCl 4 Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 238000012681 fiber drawing Methods 0.000 description 2
- 239000005350 fused silica glass Substances 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 229940119177 germanium dioxide Drugs 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000003754 machining Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000010002 mechanical finishing Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 238000005498 polishing Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 238000004017 vitrification Methods 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000005137 deposition process Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000002019 doping agent Substances 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004439 roughness measurement Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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
- C03B37/01205—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
- C03B37/01242—Controlling or regulating the down-draw process
-
- 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
- C03B37/02—Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor
- C03B37/025—Manufacture of glass fibres or filaments by drawing or extruding, e.g. direct drawing of molten glass from nozzles; Cooling fins therefor from reheated softened tubes, rods, fibres or filaments, e.g. drawing fibres from preforms
- C03B37/0253—Controlling or regulating
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2205/00—Fibre drawing or extruding details
- C03B2205/44—Monotoring or regulating the preform feed rate
Definitions
- the invention relates to a method for producing a quartz glass optical component by elongating a coaxial assembly, comprising an inner bore having, mechanically machined to final gauge quartz glass hollow cylinder and disposed within the inner bore core rod, wherein the coaxial arrangement with a predetermined feed a Heating zone supplied and softened zone by zone and the optical component is subtracted from the softened area, wherein an existing between the core rod and hollow cylinder annular gap collapses.
- the invention relates to an optical component comprising a core and a cladding surrounding the core.
- preforms for optical fibers are usually produced. It is also known to collapse a jacket tube onto a core rod during fiber drawing, the latter method being referred to as "OverDrive-During-Drawing" (ODD).
- ODD OverDrive-During-Drawing
- EP-A 598 349 describes a thick-walled quartz glass cylinder for producing a large-volume preform for optical fibers.
- the thick-walled cylinder is alskollabiert when elongating on a core rod.
- This process is known as the "rod in cylinder" (RIC) process
- RIC rod in cylinder
- Several methods are proposed for producing the quartz glass cylinder, one of which provides a cylindrical silica glass ingot which is mechanically drilled using either a core drill
- porous silica soot is deposited on a refractory support by the known OVD method, the support is subsequently removed, and the resulting soot body is dewatered and vitrified.
- a method and an optical fiber of the type mentioned are known from DE 102 14 029 A1.
- a method is described in which a tube made of synthetic quartz glass is first prepared by producing a soot body by flame hydrolysis of SiCl 4 , vitrifying this into a quartz glass block and then boring the quartz glass block by means of a core drill.
- a honing machine for the purpose of a precise finishing of the tube thus obtained, it is proposed to finish the inner wall by means of a honing machine and finally to polish it with the use of an abrasive of fineness grade # 800.
- the machined tube is etched in hydrofluoric acid.
- a so-called core rod which has a core region of SiO 2 which is doped with germanium dioxide and has a cladding region surrounding the core region which consists of undoped SiO 2 .
- the core glass rod is inserted into the inner bore of the quartz glass hollow cylinder and fixed therein to form a coaxial arrangement.
- This arrangement is supplied with its lower end beginning of an electrically heated Faserziehofen from above with a predetermined feed rate and heated therein to a temperature around 2180 ° C and thereby softened zone by zone. From the softened area, an optical fiber having an outside diameter of 125 ⁇ m is drawn off at a predetermined pulling speed.
- the annular gap between the core rod and the quartz glass hollow cylinder closes, wherein in the gap a negative pressure is maintained.
- the preforms produced by the known processes often have bubbles at the interface between the core rod and the hollow cylinder.
- the fibers drawn from such preforms also often have poor qualities. Particular attention is paid to elongated bubbles along the interface between the core and the cladding, which can lead to low fiber strength and in particular to problems in splicing the fibers.
- the invention has for its object to provide an economical method by means of which by collapsing and elongating a coaxial arrangement of hollow cylinder and core rod, an optical component can be produced, which is characterized by a low breakage rate during fiber drawing.
- the invention has for its object to provide a manufactured by the method optical component with high quality, in particular with a defect-free interface between the core rod and the hollow cylinder.
- the object is achieved according to the invention in that the feed rate V [in mm / min], depending on the outside diameter of the hollow cylinder D [in mm], is kept within a range which satisfies the following design rule:
- V min 3000 x (2 / D) 2
- the result of the RIC process is an optical component in the form of a fiber or a preform, in which the initially existing annular gap is collapsed and closed.
- the feed rate (hereinafter also referred to as "feed rate”) determines the speed of the collapse process It has been shown that, especially in the case of rapid collapsing processes, which are frequently the goal for economic reasons, the quality of the interface is poor between hollow cylinder and core glass rod is obtained. Therefore, according to the invention, the feed rate when collapsing and elongating the coaxial assembly is sufficiently slow to select. This contributes to the fact that the inner surface of the hollow cylinder can sufficiently fuse before hitting the core rod. As a result, the surface of the mechanically machined to final dimension hollow cylinder is smoothed. On the other hand, not only economic considerations speak against the slow perform the collapse, but it has also been shown that it can lead to deformations of core rod and hollow cylinder and thus to geometric errors of the component produced therefrom in a long-lasting collapse.
- the appropriate range for the feed indicated on the basis of the above design rule is therefore characterized on the one hand by a lower limit (minimum feed V m in), below which a noticeable plastic deformation of the arrangement results due to a too slow collapsing process, and on the other hand by an upper limit (maximum feed V ma ⁇ ), which is low enough to ensure a sufficient fusion of the inner wall of the hollow cylinder, depending on the outer diameter of the hollow cylinder, and which includes a particularly low compared to the prior art feed rate.
- a lower limit minimum feed V m in
- maximum feed V ma ⁇ which is low enough to ensure a sufficient fusion of the inner wall of the hollow cylinder, depending on the outer diameter of the hollow cylinder, and which includes a particularly low compared to the prior art feed rate.
- Preforms made by the RIC process show the above-mentioned bubbles at the interface between the core rod and hollow cylinder, even if a hollow cylinder is used with particularly low roughness.
- a clear correlation between the roughness of the inner wall of the hollow cylinder and the quality of the resulting interface in a preform obtained by the RIC process or the quality of the fiber drawn therefrom could not be determined.
- Such surface defects of the mechanically machined hollow cylinder are eliminated in the method according to the invention in that the feed is adjusted according to the above design rule to a value below the specified maximum feed rate V ma ⁇ . This ensures that the machined surface has enough time to fuse so that the existing cracks can close.
- the suitable feed for the melting of the inner surface of the hollow cylinder depends on the wall thickness of the hollow cylinder or of the total effetzuraceenden volume, which is composed in the radial cross section of the core rod plus the wall of the hollow cylinder. In the above formula, in which the suitable range for the feed is approximated by the outer diameter of the hollow cylinder, the annular gap remaining between the core rod and the hollow cylinder is omitted for the sake of simplicity. Taking into account the physical units, the above design rule is:
- a cylinder machined to a final dimension in the sense of this invention also means a cylinder whose inner surface has been mechanically machined to final gauge and which is optionally cleaned by chemical treatment (by etching), since etching processes do not change the geometric final shape of the hollow cylinder (for example, a bend or an ovality in cross section).
- the inventive method does not exclude that the core rod is overlapped in addition to the mechanically finished to final dimension hollow cylinder with other casing pipes, which are preferably casing pipes, which were also machined to final gauge.
- the feed rate is set as low as possible, but as large as necessary in order to prevent deformation of the hollow cylinder and the core rod. avoid.
- V ma ⁇ is set on the basis of the design rule:
- V max 8000 x (2 / D) 2
- a hollow cylinder having an outer diameter D of at least 150 mm is used, the feed being set to a value below 2.5 mm / min, preferably below 1.5 mm / min.
- a large-volume hollow cylinder is used with an outer diameter of at least 150 mm, there is a cost advantage and an improvement in dimensional accuracy.
- the cost advantage is based on the larger volume and the resulting larger preform or fiber length, so that a cost-effective mass production can be realized.
- the improvement in dimensional stability results from the fact that deviations of the hollow cylinder from the ideal cylinder symmetry during elongation are scaled down to the scale of the smaller component diameter, and thereby less significant, than with a smaller scale reduction.
- a prerequisite for a high-quality interface between the core rod and the hollow cylinder is that the collapse takes place with a slow advance of not more than 2.5 mm / min, preferably less than 1.5 mm / min.
- a method variant in which the mechanical processing of the hollow cylinder comprises grinding the inner wall of the inner bore and a subsequent etching treatment has proven particularly useful, subcutaneous cracks remaining after the grinding having a crack depth of not more than 2 mm.
- the mechanical processing of the inner wall of the inner bore by grinding (which also includes honing) inevitably causes cracks.
- the crack depth can be successively reduced by repeated grinding honing and polishing steps, but this is associated with a high expenditure of time and materials.
- the method according to the invention tolerates such cracks, if the crack depth is less than 2 mm and thus allows the use of hollow cylinders, which can be produced relatively inexpensively due to a less complex mechanical machining of its inner wall.
- the annular gap between the core rod and the hollow cylinder is on average greater than 2 mm, preferably greater than 5 mm.
- the annular gap between the core rod and the hollow cylinder is on average less than 1 mm, preferably less than 0.7 mm.
- a small annular gap width during collapse causes a comparatively small flow of material in the radial direction, which facilitates compliance with a given geometry with regard to the fiber core eccentricity.
- This variant of the method is to be preferred in particular when high demands are placed on the geometry of the component and when the cylinder surfaces have only small cracks which fuse together easily.
- the inventive method proves to be particularly advantageous especially for thick-walled hollow cylinders. Because the wall thickness of the hollow cylinder plays with regard to a sufficient melting an important role. As the wall thickness of the quartz glass cylinder increases, the feed to be adjusted decreases rather than increases. For economic reasons, a hollow cylinder with an inner diameter of at most 70 mm, preferably a maximum of 50 mm, is preferably used.
- the wall thickness of the hollow cylinder plays an essential role in terms of the deformation and the economy of the method according to the invention.
- hollow cylinder and core rod are used in which the ratio CSA (o / CSA (R) of the radial cross-sectional area CSA (C) of the hollow cylinder and the radial cross-sectional area CSA ( R) of the core rod is in the range between 5 and 100, preferably between 10 and 80 lies.
- a large wall thickness requires more "heating" to ensure sufficient fusion of the inner wall of the hollow cylinder, which is more likely to slow down the feed rate, and the manufacturing accuracy of the optical component increases with increasing wall thickness because of absolute geometry errors (independent of wall thickness) and the outer diameter of the quartz glass cylinder) are scaled down more during elongation.
- FIG. 1 shows a diagram with results of RIC experiments using hollow cylinders with different outer diameters and with variation of the feed.
- preforms and optical fibers were prepared by the RIC process by overlaying a core rod with a quartz glass hollow cylinder and elongating this composite.
- the preforms and fibers have a core region that is separated from an inner cladding layer and an outer cladding glass layer is surrounded.
- the core region consists of quartz glass, which is homogeneously doped with 5% by weight of germanium dioxide.
- the cladding glass layers consist of undoped quartz glass, part of which is provided by the jacket of the core rod and a part by a mechanically processed quartz glass hollow cylinder.
- the core rod was produced by the OVD method by layered soot particles are deposited on a carrier rotating about its longitudinal axis by reciprocating a Abscheidebrenners, the Abscheidebrenner SiCI 4 and GeCI 4 fed and in a burner flame in the presence of oxygen to SiO 2 and GeO 2 were hydrolyzed.
- the ratio of SiCl 4 and GeCl was set in the deposition of the inner layers so that over this part of the wall thickness of the soot tube a predetermined homogeneous GeO 2 concentration of 5 wt .-% was found.
- a soot tube was obtained, which was subjected to a dehydration treatment to remove the hydroxyl groups introduced by the preparation.
- the soot tube was placed in a vertical orientation in a dehydration furnace and initially treated at a temperature in the range of 850 ° C to about 1000 ° C in a chlorine-containing atmosphere. The treatment duration was about six hours. As a result, a hydroxyl group concentration of less than 100 parts by weight ppb was achieved.
- the thus treated soot tube was vitrified in a vitrification furnace at a temperature in the range of 1350 ° C and thereby collapsed the inner bore, so that a core rod having the desired refractive index profile was obtained.
- the core rods were made with the dimensions shown in Table 1, wherein the respective core diameters were adapted to the associated hollow cylinder so that in the optical fiber with an outer diameter of 125 microns each have a central "core area" with a Diameter of about 8.5 microns results.
- porous soot bodies were produced by external deposition by means of an OVD method, but without the addition of a dopant.
- the soot tube was subjected to the above-described dehydration treatment and then vitrified.
- the two end portions of the fused quartz glass fused quartz glass ingot thus obtained were cut off, and the outer wall was roughly ground by means of a peripheral sander equipped with a # 80 whetstone, whereby the predetermined target outer diameter was substantially obtained.
- the outer surface of the tube was then ground by means of an NC peripheral sander.
- the inner bore of the tube thus obtained was honed altogether by means of a honing machine equipped with a # 80 honing stone, whereby the polishing wheel was continuously refined and the finishing treatment was carried out with a # 800 honing stone. After making sure that the tube was made to a wall thickness within a given tolerance range, it was briefly etched in a 30% hydrofluoric acid etching solution. The maximum surface roughness R ma ⁇ was thereafter
- the hollow cylinder / core rod assembly was then fed to an electrically heated furnace at a given feed rate (see Table 1) and heated therein to a temperature in the range of 2000 ° C to 2400 ° C, drawing an optical fiber from the softened area , The take-off speed was adjusted to the feed rate so that the nominal fiber diameter of 125 ⁇ m + 0.5 ⁇ m was obtained. The remaining process parameters were not changed, in particular the drawing temperature is mentioned. In each case, a vacuum in the range between 2 kPa and 10 kPa was maintained in the annular gap between the core rod and the hollow cylinder.
- the take-off speed was adapted to the feed so that a nominal diameter of the preform of 85.0 mm + - 0.5 mm was obtained.
- the quality of the interface between the core region of the fiber and the cladding glass contributed by the hollow cylinder was examined microscopically. Particular attention was paid to so-called elongated bubbles at the interface.
- the width of the annular gap between the hollow cylinder and core rod in the RIC process is less drastic. It can be seen that a further annular gap has an advantageous effect on the quality of the interface, while a narrow annular gap favors the dimensional accuracy of the preform and of the fiber drawn therefrom.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
- Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/559,481 US20060150685A1 (en) | 2003-06-04 | 2004-06-03 | Method for elongating and collapsing a blank made of quartz glass |
DE112004000594T DE112004000594B4 (de) | 2003-06-04 | 2004-06-03 | Verfahren zum Elongieren und Kollabieren einer Vorform aus Quarzglas |
JP2006508259A JP4625448B2 (ja) | 2003-06-04 | 2004-06-03 | 石英ガラスからなる予備成形物を延伸および萎縮する方法 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10325538.9 | 2003-06-04 | ||
DE10325538A DE10325538A1 (de) | 2003-06-04 | 2003-06-04 | Verfahren für die Herstellung eines optischen Bauteils aus Quarzglas durch Elongieren einer koaxialen Anordnung sowie nach dem Verfahren hergestelltes optisches Bauteil |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2004108616A1 true WO2004108616A1 (de) | 2004-12-16 |
Family
ID=29762202
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2004/005991 WO2004108616A1 (de) | 2003-06-04 | 2004-06-03 | Verfahren zum elongieren und kollabieren einer vorform aus quarzglas |
Country Status (5)
Country | Link |
---|---|
US (1) | US20060150685A1 (de) |
JP (1) | JP4625448B2 (de) |
CN (1) | CN100491279C (de) |
DE (2) | DE10325538A1 (de) |
WO (1) | WO2004108616A1 (de) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102004035086B4 (de) * | 2004-07-20 | 2008-07-03 | Heraeus Quarzglas Gmbh & Co. Kg | Verfahren zur Herstellung eines Hohlzylinders aus Quarzglas mit kleinem Innendurchmesser sowie zur Durchführung des Verfahrens geeignete Vorrichtung |
EP3088370B1 (de) * | 2015-04-28 | 2018-09-26 | Heraeus Quarzglas GmbH & Co. KG | Verfahren und vorrichtung zur herstellung eines rohres aus glas |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4820322A (en) * | 1986-04-28 | 1989-04-11 | American Telephone And Telegraph Company At&T Bell Laboratories | Method of and apparatus for overcladding a glass rod |
DE3913907A1 (de) * | 1989-04-27 | 1990-10-31 | Standard Elektrik Lorenz Ag | Verfahren zur herstellung von lichtwellenleitern mit vorstrecken einer roh-vorform vor aufschmelzen eines ueberwurfrohres |
JPH1148725A (ja) * | 1997-08-08 | 1999-02-23 | Yokohama Rubber Co Ltd:The | 空気入りタイヤ |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL261074A (de) * | 1958-08-11 | |||
US3887485A (en) * | 1969-10-31 | 1975-06-03 | Jenaer Glaswerk Schott & Gen | Solid optical filter having selective wavelength permeability |
US3737292A (en) * | 1972-01-03 | 1973-06-05 | Corning Glass Works | Method of forming optical waveguide fibers |
DE3447082A1 (de) * | 1984-05-26 | 1985-12-19 | AEG-Telefunken Kabelwerke AG, Rheydt, 4050 Mönchengladbach | Verfahren zum herstellen einer vorform zum ziehen von lichtleitfasern |
CA1317464C (en) * | 1986-04-28 | 1993-05-11 | William Malcolm Flegal | Method of and apparatus for overcladding an optical preform rod |
US4880759A (en) * | 1986-08-12 | 1989-11-14 | H. C. Spinks Clay Company Inc. | Ball clay slurry |
DE3731604A1 (de) * | 1987-09-19 | 1989-03-30 | Philips Patentverwaltung | Verfahren zur herstellung einer monomode-lichtleitfaser |
JPH0818842B2 (ja) * | 1987-12-03 | 1996-02-28 | 住友電気工業株式会社 | 光フアイバ用母材の製造方法 |
ES2120467T3 (es) * | 1992-11-19 | 1998-11-01 | Shinetsu Quartz Prod | Procedimiento para fabricar un tubo de vidrio de cuarzo de gran tamaño, una preforma y una fibra optica. |
DE60137770D1 (de) * | 2000-05-01 | 2009-04-09 | Sumitomo Electric Industries | Lichtwellenleiterfaser und verfahren zu ihrer herstellung |
AU2003210420A1 (en) * | 2002-03-22 | 2003-10-08 | Heraeus Tenevo Ag | Method for producing an optical fiber and optical fiber |
DE10214029C2 (de) * | 2002-03-22 | 2003-09-18 | Heraeus Tenevo Ag | Verfahren zur Herstellung einer optischen Faser sowie nach dem Verfahren hergestellte optische Faser |
-
2003
- 2003-06-04 DE DE10325538A patent/DE10325538A1/de not_active Withdrawn
-
2004
- 2004-06-03 WO PCT/EP2004/005991 patent/WO2004108616A1/de active Application Filing
- 2004-06-03 CN CNB2004800155011A patent/CN100491279C/zh not_active Expired - Lifetime
- 2004-06-03 JP JP2006508259A patent/JP4625448B2/ja not_active Expired - Lifetime
- 2004-06-03 DE DE112004000594T patent/DE112004000594B4/de not_active Expired - Fee Related
- 2004-06-03 US US10/559,481 patent/US20060150685A1/en not_active Abandoned
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4820322A (en) * | 1986-04-28 | 1989-04-11 | American Telephone And Telegraph Company At&T Bell Laboratories | Method of and apparatus for overcladding a glass rod |
DE3913907A1 (de) * | 1989-04-27 | 1990-10-31 | Standard Elektrik Lorenz Ag | Verfahren zur herstellung von lichtwellenleitern mit vorstrecken einer roh-vorform vor aufschmelzen eines ueberwurfrohres |
JPH1148725A (ja) * | 1997-08-08 | 1999-02-23 | Yokohama Rubber Co Ltd:The | 空気入りタイヤ |
Non-Patent Citations (1)
Title |
---|
PATENT ABSTRACTS OF JAPAN vol. 0134, no. 08 (C - 634) 8 September 1989 (1989-09-08) * |
Also Published As
Publication number | Publication date |
---|---|
JP4625448B2 (ja) | 2011-02-02 |
US20060150685A1 (en) | 2006-07-13 |
DE10325538A1 (de) | 2004-01-22 |
CN100491279C (zh) | 2009-05-27 |
DE112004000594B4 (de) | 2007-10-18 |
CN1798707A (zh) | 2006-07-05 |
DE112004000594D2 (de) | 2006-02-23 |
JP2006526561A (ja) | 2006-11-24 |
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