Classifications

• • C—CHEMISTRY; METALLURGY
  • C03—GLASS; MINERAL OR SLAG WOOL
  • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
  • C03B23/00—Re-forming shaped glass
  • C03B23/04—Re-forming tubes or rods
  • C03B23/047—Re-forming tubes or rods by drawing

Definitions

• the present invention relates to a method for producing a tube made of vitreous material, in particular of quartz glass, in which a hollow cylindrical semifinished product made of vitreous material is fed essentially vertically to a heating zone, heated therein and tool-free to the tube with the formation of a transition region from the semifinished product to the tube downwards is subtracted, the diameter and wall thickness of the tube being measured continuously and the measured geometric data of the tube being used to generate a control signal, with the aid of which a pressure difference between the pressure P 1 in the interior of the semi-finished product, the transition region and the tube and the pressure P 2 in the boiler room, which is regulated in the heating zone at least in the transition area from the semi-finished product to the pipe and the pipe area adjacent to it.
• a method as stated above is known from EP-A1 394 640.
• quartz glass or high-silica glasses in the form of a hollow cylinder as semi-finished products are drawn into a tube in a vertical process, the pressure in the interior of the tube being higher than the external pressure, i.e. the pressure that acts in the heating zone on the outside of the semi-finished product and the pipe.
• This method can only be used to produce tubes in which the ratio of the outside diameter to the inside diameter of the tube corresponds at most to the ratio of the outside diameter to the inside diameter of the high-cylindrical semi-finished product; in general, however, tubes are obtained with the known method in which the ratio of outside diameter to
• capillary tubes are known from EP-A1 259 877, i.e. such pipes that have a very small inner diameter.
• the outside diameter of these capillary tubes is typically up to 5 times larger than the inside diameter.
• Such capillary tubes are produced by arranging several glass tubes with different diameters inside one another, the individual inside and outside diameters of these glass tubes being matched to one another. After these glass tubes have been inserted into one another, the arrangement is heated and the individual tubes are fused together in the longitudinal direction by pulling. However, this procedure means that extensive storage of glass tubes of different inside and outside diameters is required.
• the coaxial arrangement requires holding the tubes at both ends when pulling and fusing with high precision.
• the individual, prefabricated glass tubes, which are then inserted into one another have to be manufactured with very high precision in their geometric dimensions, in particular to ensure a uniform connection of the individual tubes.
• the present invention is based on the object of developing the method mentioned at the outset in such a way that it is possible to process a wide range of hollow cylindrical semifinished products into tubes with the desired internal and external dimensions.
• the above object is achieved on the basis of the method mentioned at the outset in that for the production of pipes in which the ratio of the outside diameter (D Ra ) to the inside diameter (D R
• the method according to the invention also allows the production of pipes in which the ratio of wall thickness to outer diameter is greater than in the semi-finished product.
• the pressure P 1 in the interior of the tube is then adjusted by supplying a gas stream which is introduced into the interior of the semi-finished product, the transition region and the tube and is kept at a pre-calculated value by means of a suction pump. This allows a defined vacuum in the pipe to be maintained and set.
• the quality of a tube can be greatly influenced by pressure fluctuations inside the tube, even if they are only slight.
• the gas stream is first fed to a container serving as a buffer, which is inserted between the suction pump and the interior of the tube, before it is introduced into the semi-finished product
• Inert gas has the advantage that when it comes into contact with hot parts, possibly also with hot furnace parts, oxidation is avoided.
• semi-finished products can be processed in which the ratio of the outside diameter of the semi-finished product (D Ha ) to the inside diameter of the semi-finished product (D Hi ) is in the range from 1.5 to 4.5, ie in a very wide range.
• a diameter measurement (outside and inside diameter) of the pipe is advantageously carried out directly, as seen in the drawing direction of the pipe, that is to say after the transition region still in the boiler room, and this geometric data is used to generate the control signal for regulating the pressure difference.
• the process indicated is particularly suitable for the production of pipes in which the ratio (D Ra / D Rl ) of the pipe outside diameter to the pipe inside diameter is greater than 1.5 ; this ratio (D Ra / D RI ) should preferably also be in the range from 1.8 to 5.0.
• the process can also be optimized for pipes in which the ratio of D Ra to D R
• the method according to the invention is particularly suitable for the production of capillary tubes which have a small inner diameter and have a high resistance to breakage, since tubes with relatively thick walls can be produced in one method operation.
• the method is also used to produce a tube for producing an optical waveguide.
• Semi-finished products made of high-purity quartz glass, in particular synthetic glass, are used for this purpose.
• the tubes produced therefrom serve as cladding tubes, for example in the production of optical waveguides using the known rod-in-tube technique, or as substrates in the known MCVD or PCVD processes.
• the arrangement for carrying out the method according to the invention comprises, as the figure shows, a vertically arranged furnace 1 with an upper furnace inlet 2 and a lower furnace outlet 3.
• the inner heating chamber 4 of the furnace 1 can be heated to temperatures above 2300 ° C.
• a quartz glass cylinder 5 which is closed on its upper side with a carrier 6, is introduced into the furnace interior 4 from the upper side via the furnace inlet 2 by means of a suitable guide device.
• the quartz glass hollow cylinder 5 is connected at its upper end, closed with the carrier 6, via a supply line 7 to a process container 8 which, on the one hand, via a shut-off valve 9 with an inert gas supply 10 and on the other hand with a controllable valve 11 with a vacuum pump 12 connected is.
• the interior 4 of the furnace 1 is supplied with a quartz glass hollow cylinder 5, softened in the area of a deformation zone 13, which is indicated by a dash-dotted circle approximately in the middle of the furnace interior 4, so that a pull onion moves in the direction of arrow 14 15 forms by tapering the wall cross section of the quartz glass cylinder 5.
• a pulling device 16 with guide rollers 17 is provided on the output side of the furnace 1.
• the tube interior 19 or the interior of the quartz glass cylinder 5 is closed in the region of the drawn-off tube 18 by means of a stopper 20, such as a silicone stopper.
• the pressure ratios in the interior 4 of the furnace 1 and in the tube interior 19 or in the interior of the quartz glass cylinder 5 can be set and changed in a defined manner.
• a pressure measuring device 21 for monitoring the pressure in the interior 19 and a further pressure measuring device 22 for measuring the pressure in the interior 4 of the furnace 1 are provided.
• a pressure regulator 23 which controls the controllable valve 11, a temperature regulator 24 for regulating the furnace temperature, a pyrometer 25 for measuring and monitoring the set furnace temperature, and a further pyrometer 26 for measuring the temperature in the region the onion 15, a diameter measuring device 27 for measuring the diameter of the drawn tube 18th immediately after the onion 15, ie inside the furnace chamber 4, another diameter measuring device 28 for measuring the diameter of the drawn tube 18 outside the furnace 1, a wall thickness measuring device 29 for measuring the wall thickness of the pulled tube 18 outside the furnace 1 , A speed measuring device 30 for measuring the drawing speed of the tube 18 in the direction of arrow 14, and a speed controller 31 which controls the pulling device 16 and thus adjusts the rotational speed of the guide rollers 17.
• All regulators, measuring devices and other devices, as stated above, are connected to a central process control and control device 32.
• Setpoints for example tube dimensions of both the quartz glass cylinder 5 and the desired tube 18 to be produced, the required mass throughput, etc., are entered via the central process regulation and control device, as indicated by the input arrow 33.
• the measuring points of the first diameter measurement, immediately below the onion 15, which is carried out by the diameter measuring device 27, is again indicated separately by the arrow 34, while the second measuring point for the drawn tube 18, outside the furnace 1, for the Diameter measuring device 28 is marked with an arrow 35.
• the manufacture of a tube 18 with the desired dimensions, starting from a quartz glass cylinder 5, can be continuously monitored and readjusted or adapted to the circumstances.
• a pipe 18 was manufactured with the construction as stated above, which had a pipe outer diameter of 50 mm, a pipe inner diameter of 12 mm, ie a diameter ratio D Ra / D Rl of 4.17, for which purpose as a semi-finished product a quartz glass hollow cylinder 5 was used, the ratio of the outer diameter D Ha to the inner diameter D Hl was 3.17.
• the throughput in this case was 34 kg / h.
• the drawing was carried out at a boiler room temperature (the temperature in the interior 4 of the furnace 1) of 2300 ° C. During the operation of furnace 1, P 2 in boiler room 4 was approximately 1120 mbar.
• a pressure P 1 of 1070 mbar had to be set in the tube interior 19 in order to generate the above-mentioned pipe ratio of 4.17.
• the interior 19 of the tube 18 was sealed by the seal, such as a silicone plug, 20 at the end of the tube 18 locked.
• the internal pressure was generated by means of the vacuum pump 12 via an extension piece, in the figure the carrier 6, at the upper end of the quartz glass cylinder 5.
• the process container 8 is interposed as a buffer between the vacuum pump 12 and the quartz glass cylinder 5.
• P 2 was 1090 mbar.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Materials Engineering (AREA)
• Organic Chemistry (AREA)
• Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)
• Manufacture, Treatment Of Glass Fibers (AREA)
• Glass Melting And Manufacturing (AREA)
• Glass Compositions (AREA)

Priority Applications (7)

Applications Claiming Priority (2)

Publications (1)

Family

ID=7890559

Family Applications (1)

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Cited By (2)

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Citations (3)

Family Cites Families (10)

• 1998
  • 1998-12-10 DE DE19856892A patent/DE19856892C2/de not_active Expired - Fee Related
• 1999
  • 1999-12-06 CA CA002320358A patent/CA2320358A1/en not_active Abandoned
  • 1999-12-06 WO PCT/EP1999/009513 patent/WO2000034193A1/de not_active Ceased
  • 1999-12-06 EP EP99965440A patent/EP1054841B1/de not_active Expired - Lifetime
  • 1999-12-06 CN CNB998028371A patent/CN1160264C/zh not_active Expired - Lifetime
  • 1999-12-06 AT AT99965440T patent/ATE325082T1/de not_active IP Right Cessation
  • 1999-12-06 BR BR9907813-9A patent/BR9907813A/pt not_active Application Discontinuation
  • 1999-12-06 DE DE59913387T patent/DE59913387D1/de not_active Expired - Lifetime
  • 1999-12-06 JP JP2000586646A patent/JP4397008B2/ja not_active Expired - Fee Related
  • 1999-12-06 KR KR1020007008570A patent/KR100632756B1/ko not_active Expired - Lifetime
  • 1999-12-06 US US09/601,460 patent/US6516636B1/en not_active Expired - Lifetime
• 2000
  • 2000-08-08 ZA ZA200004039A patent/ZA200004039B/xx unknown

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