Glass manufacturing – Processes of manufacturing fibers – filaments – or preforms – Process of manufacturing optical fibers – waveguides – or...
Reexamination Certificate
2000-11-13
2002-11-05
Derrington, James (Department: 1731)
Glass manufacturing
Processes of manufacturing fibers, filaments, or preforms
Process of manufacturing optical fibers, waveguides, or...
C065S510000, C065S513000, C065S533000, C065S537000, C065S538000
Reexamination Certificate
active
06474109
ABSTRACT:
The present invention relates to a device for drawing optical fibres from a preform, comprising:
a furnace comprising a tube for heating one end of said preform to the drawing temperature thereof, which tube comprises:
i) a central tube,
ii) an upper extension tube connected to the lower part of said central tube so as to obtain a gas tight seal against an ambient atmosphere exterior said furnace, wherein the upper extension tube comprises an inlet for an inert gas in the top region of the upper extension tube, as a result of which the preform and the fibre to be drawn therefrom are surrounded by an inert gas,
iii) a lower extension tube connected to said upper extension tube in such a manner that a gas tight seal against an ambient atmosphere exterior said furnace is obtained,
iv) a tube outlet connected to said lower extension tube,
means for drawing the fibre,
means for supporting the preform in the furnace.
The present invention furthermore relates to a method for drawing optical fibres from a preform.
Such a device is known per se from U.S. Pat. No. 4,673,427, which was granted to the present applicants in 1987 already. According to this US patent, an optical fibre is drawn from the heated end of the preform in a furnace, with a gas being carried along heating means in the furnace. The gas is essentially heated to the temperature of the fibre at the end of the preform, after which the hot gas flows along the fibre at essentially the same speed as the drawing speed of the fibre. Although the specification makes mention of the fact that the gas flow is a laminar gas flow, in order to ensure that the temperature gradient in the fibre will be lower at all times than the value at which stresses are set up in the fibre that will increase the optical attenuation, it has become apparent that minor turbulence is produced in the gas flow, which results in undesirable fluctuations in the diameter of the drawn fibre.
Such a device is also known from European patent application No. 0 321 182, in which device the furnace includes a recovery chamber at its bottom side for cooling the fibre in a uniform manner under conditioned circumstances. The connection between the furnace and the recovery chamber is provided with a seal to prevent the ingress of ambient air. While the fibre is being drawn from the preheated preform, an inert gas, such as nitrogen or helium, is supplied via two separate manifolds disposed adjacent to the upper side of the furnace, in order to ensure a symmetrical temperature distribution for cooling the fibre symmetrically. A construction of this kind leads to disturbances in the flow behaviour of the inert gas at the preform already, so that it is difficult to form a stable boundary layer around the fibre. Another drawback of such a device is the fact that, although the length of the recovery chamber depends on the height of the draw tower and the draw speed, wherein the length of the recovery chamber in question is about 45 cm at a line speed of 2 m/s, in practice there will be undesirable ingress of ambient air into the end of the recovery chamber. Such ingress of ambient air leads to diameter fluctuations. In addition, the relatively cold ambient air may set up stresses in the fibre, which is not sufficiently stabilized yet at that point, resulting in a diminished optical performance of the fibre thus obtained.
Such a device is also known from European patent application No. 0 329 898, wherein an inert gas is supplied to inlet openings located at the upper side of the furnace, after which said inert gas is caused to exit the heated furnace, using a shutter disposed at the bottom side of the furnace, perpendicularly to the direction of flow of the inert gas, which shutter includes a number of holes. The drawn fibre is discharged via the central opening of the shutter, whilst the inert gas is discharged via the other holes of the shutter. Although the ingress of ambient air is significantly reduced when such a construction is used, it has become apparent that the special construction of the shutter opening may cause undesirable turbulence of the inert gas that is present in the furnace, especially near the shutter, which will lead to undesirable diameter fluctuations.
Such a device is also known from European patent application No. 0 567 961, wherein a flow isolator is disposed at the bottom side of the furnace for symmetrically cooling the fibre drawn from the heated preform, which flow isolator includes a single outlet opening at its bottom opening. When using a construction of this kind, the same problems, in particular turbulence, will occur as described above with reference to European patent application no. 0 329 898.
Japanese unexamined patent application no. 6-115972 relates to a method for drawing optical fibres from a preform wherein the lower end of the furnace is in direct communication with the ambient atmosphere, so that also in this case there is an ingress of ambient air, which may lead to undesirable fluctuations in the fibre diameter.
The object of the present invention is to provide a method and a device for drawing optical fibres from a preform, wherein the aforesaid problems of the prior art do no occur.
Another object of the present invention is to provide a device and a method for drawing optical fibres from a preform wherein the extent to which particles adhere to the fibre is minimized, which particles mainly originate from the inner wall of the tube through which the fibre is passed, or they are formed as a result of the evaporation of quartz from the preform at the high drawing temperature.
Another object of the present invention is to provide a device and a method for drawing optical fibres from a preform, wherein the boundary layer of an inert gas that forms around the fibre provides symmetrically cooling of the fibre during the drawing process, wherein disturbance of the boundary layer must be minimized.
Another object of the present invention is to provide a device and a method for drawing optical fibres from a preform, wherein turbulence as well as swirling are prevented during the drawing process.
According to the present invention the device referred to in the introduction is characterized in that the tube outlet is conical in shape, wherein the internal diameter of the end of the tube outlet is smaller than the internal diameter of the upper extension tube so as to prevent the ingress of ambient atmosphere and turbulence and swirling within the tube outlet, which tube outlet includes a number of outlet openings for inert gas disposed on the circumference of said conical shape.
The use of outlet openings for inert gas disposed on the circumference of the conical shape of the tube outlet, preferably at the end thereof, ensures that the boundary layer of inert gas that surrounds the fibre will flow along with the fibre in a laminar flow in the drawing direction thereof, so that the occurrence of fibre twisting or of oscillations in the fibre diameter is reduced to a minimum. The conical shape is in particular desirable in order to eliminate pressure fluctuations, which occur in particular at the end of the tube outlet, where the fibre is discharged via the central opening of the tube outlet. As a result of the presence of the additional outlet openings for inert gas, part of the gas that surrounds the fibre is discharged, thus reducing the amount of turbulence caused by the narrowing of the outlet opening. Although it has been stated above that the outlet openings are disposed at the end of the tube outlet, said outlet openings may be positioned close to the transition from the lower extension tube to the tube outlet in certain embodiments.
Furthermore it is preferable that the internal diameter of the lower extension tube is substantially the same as the internal diameter of the upper extension tube.
By matching the diameter of the lower extension tube with that of the upper extension tube it is ensured that the inert gas flowing along with the drawn fibre in a boundary layer surrounding said fibre will not encounter any obstacles,
Breuls Antonius Henricus Elisabeth
deFouw Marinus Jacob
Derrington James
Plasma Optical Fibre B.V.
SEED IP Law Group PLLC
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