JPH06211535A - Optical fiber drawing method - Google Patents

Abstract

PURPOSE:To draw a high-quality optical fiber having high strength, low transmission loss, etc., even when a large-diameter perform of optical glass fiber is drawn at a high speed. CONSTITUTION:When a carbon electric furnace 2 (drawing furnace) is used, the ratio of gaseous argon having a low heat-transfer coefficient to gaseous helium having a high heat-transfer coefficient in the gaseous mixture determined by the outer diameter and drawing speed of an optical fiber glass perform 8 is set in the gaseous argon feed controller 24 and gaseous helium feed controller 26 through an input controller 28. The gaseous mixture having a specified heat-transfer coefficient is formed in a mixer 22 and introduced into the furnace 2. The temp. of molten preform 8 is appropriately controlled at its meniscus by the heat-transfer coefficient of the gaseous mixture introduced into the furnace 2, and an optical fiber 10 is drawn while maintaining a specified length of the solidified part and an appropriate drawing tension.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for drawing an optical fiber, and more particularly, to strength and transmission even if an optical fiber is drawn by heating and melting a glass base material for an optical fiber having a large outer diameter in a short time. The present invention relates to an optical fiber drawing method capable of producing a high-quality optical fiber having excellent characteristics and the like.

[0002]

2. Description of the Related Art An optical fiber is manufactured by heating a glass base material for an optical fiber (preform) in a drawing furnace filled with an inert gas, melting the glass base material for an optical fiber by heating, and stretching it. And then pulling it out of the furnace. The single-mode optical fiber manufactured in this manner is, for example,
10 μm diameter core and diameter 12 formed around the core
It has a cladding of 5 μm. Recently, in order to reduce the manufacturing cost of optical fibers, attempts have been made to manufacture the optical fibers in a short time by increasing the outer diameter of the glass preform for optical fibers and increasing the drawing speed. In manufacturing such an optical fiber, it is necessary to manufacture the core and the clad with high quality such as the outer diameter shape, the transmission characteristics, and the strength.

The strength of the optical fiber is softened by heating, and dust adheres to the meniscus-shaped portion at the tip of the glass base material for an optical fiber, which is the tip where the optical fiber is drawn.
It is known to decline. For example, JP-A 1-2
Japanese Patent No. 75443 discloses a method of reducing fluctuations in the outer diameter of an optical fiber and preventing a decrease in strength. This method
As the drawing speed increases and the glass base material for optical fibers grows in size, the meniscus of the glass base material for optical fibers extends, and the drawn optical fiber is drawn out of the drawing furnace in a softened state. In order to prevent non-adhesion of dust in the outside air, a partition wall is provided below the drawing furnace to maintain a uniform and clean atmosphere gas flow up to a position where the temperature of the optical fiber falls below the softening point.

More specifically, as shown in FIG. 5, the drawing apparatus 71 has an electric heater 4 and a furnace core tube 6 provided in the drawing furnace body 2 and is provided above the drawing furnace body 2. The glass base material 8 for an optical fiber is inserted from the formed opening 2a, and the drawn optical fiber 10 is provided in the lower portion of the drawing furnace body 2 and the opening 12 of the partition 12 of about 300 mm to 500 mm is provided.
It is drawn from a. Argon gas is introduced into the partition wall 12 from the argon gas inflow controller 16 through the pipe 14. At this time, the glass base material 8 for an optical fiber having an outer diameter of 60 mm was drawn at a drawing speed of 300 to 500 m / mi.
In the case of drawing with n and tension of 2 kg, the temperature of the optical fiber at the outlet of the partition wall 12 is lowered to about 1000 to 1200 ° C., dust is not attached, and the probability of breaking the optical fiber is 4
It is reported that it is about once every 0 to 50 km, and the fracture probability when there is no partition wall is about once per 10 km, which is improved.

Japanese Patent Publication No. 62-4333 discloses that a wire drawing furnace made of a carbon material used for a wire drawing furnace is required for wire drawing.
Contamination of the surface of the optical fiber due to long-term exposure to a high temperature of 00 ° C or higher for oxidative consumption and generation of dust such as silicon carbide due to reaction between volatile components of quartz and carbon due to high temperature In order to prevent this, it is disclosed that a mixed gas of 0.05 to 0.6 helium gas mixed with argon gas is caused to flow into the core tube to keep the atmosphere in the drawing furnace clean. In other words, Japanese Examined Japanese Patent Sho 62-4333
The publication discloses that mixing helium gas with argon gas improves the cleanliness. However,
If the mixing ratio of the helium gas is too high, the outer diameter of the optical fiber fluctuates, so the mixing ratio is set to be in the range of 0.05 to 0.6.

Japanese Unexamined Patent Publication (Kokai) No. 60-231439 discloses a problem in the above-mentioned Japanese Patent Publication No. 62-4333, namely,
In order to avoid the problem of using a carbon material in the drawing furnace, and to avoid the occurrence of oxygen defects in the optical fiber when the optical fiber is drawn in an inert atmosphere, as a core tube,
It is disclosed that zirconia having a high melting point of about 2800 ° C. is used and a mixed gas of oxygen and helium gas is used as a heating atmosphere.

In Japanese Patent Laid-Open No. 3-153540, in order to reduce transmission loss of an optical fiber, a glass base material for an optical fiber is heated and melted into a meniscus shape, and a neck-down portion where the optical fiber is drawn is forcibly cooled. It is disclosed to do. As the cooling medium, helium having a large heat transfer coefficient but a small heat capacity is preferably water-cooled before use. Alternatively, for protection of the heating element, a mixed gas in which argon gas is mixed with helium gas can be used. The reason for forcibly cooling the neck-down part is that if the drawing tension is increased, the refractive index difference between the core and the clad cannot be maintained and the transmission loss increases, while the transmission loss increases even if the drawing tension is extremely lowered. It is presumed that this is due to heat fluctuations, and it is understood that the neck-down part that is most susceptible to heat is forcibly cooled to prevent heat fluctuations in that part.

[0008]

DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
The wire drawing device described in Japanese Patent No. 75443 discloses that the base material is heated and melted and the portion in the meniscus shape is stretched with an increase in the outer diameter of the glass base material for an optical fiber and an increase in drawing speed and speed. Since the distance (solidification length) from the tip of the meniscus-shaped portion to the position where the temperature of the optical fiber is below the softening point increases, the dust generated in the drawing furnace is essentially light in an unstable state before solidification. The problem of encouraging non-attachment to the fiber is still inherent. In order to prevent this dust from adhering, first, in order to maintain high cleanliness, a uniform flow of inert gas or air must be flown from the upper part of the drawing furnace. A partition wall having a length corresponding to the speed and the outer diameter of the glass base material for an optical fiber, for example, a length of 300 to 500 mm must be provided. Providing a partition increases the manufacturing cost of the drawing apparatus, and further increases the vertical length of the drawing furnace and the partition to increase the height of the drawing apparatus and accommodate the drawing apparatus. The problem arises that the height of the building is increased and the operability is reduced.

In the wire drawing apparatus described in Japanese Patent Publication No. 62-4333, the carbon wire drawing furnace (electric furnace) is prevented from oxidative wear and dust generated due to the reaction between quartz and carbon. In order to prevent this, it has been shown that helium gas is mixed with argon gas to clean the inside of the drawing furnace, but this method increases the outer diameter of the glass preform for optical fibers and increases the drawing speed. However, maintaining or improving the quality of the optical fiber is not suitable for the purpose.

The method disclosed in Japanese Patent Laid-Open No. 60-231439 mentioned above has a problem that the cost of the drawing apparatus becomes high because expensive zirconia is used for the core tube. In particular, zirconia simple substance causes cracks at about 1100 ° C. due to the difference in thermal expansion coefficient associated with phase transformation, so it is necessary to add yttria to zirconia, which makes production more difficult. Further, even in this method, the optical fiber of 10 km is broken about 9 times, and there is still a problem in strength.

Incidentally, the above-mentioned Japanese Patent Laid-Open No. 60-231439.
As a comparative example, Japanese Patent Publication discloses an example in which a carbon furnace tube is used and an argon gas and a helium gas are used as a heating atmosphere at a flow rate ratio of 4: 1. There are many problems with strength.

The method disclosed in Japanese Unexamined Patent Publication (Kokai) No. 3-153540 merely cools the helium gas and forcibly cools it in order to prevent thermal fluctuations in the neck-down portion in order to improve the transmission loss of the optical fiber. However, it does not disclose the improvement measures for increasing the outer diameter of the glass preform for optical fibers and increasing the drawing speed, which are the problems of the present invention.

The present invention solves the various problems of the prior art described above, and the strength of the optical fiber, the fluctuation of the outer diameter, and the transmission can be achieved even if the glass base material for an optical fiber having a large outer diameter is drawn at a high drawing speed. An object of the present invention is to provide an optical fiber drawing method capable of producing a high-quality optical fiber excellent in terms of loss and the like.

[0014]

Means and Solution for Solving the Problems A first aspect of the optical fiber drawing method of the present invention will be described. The inventor of the present invention changes the heat transfer coefficient of the inert gas introduced into the drawing furnace according to the outer diameter of the glass preform for optical fiber and the drawing speed, thereby melting the glass preform for optical fiber. It has been found that the shape of or the solidification length of the optical fiber immediately after drawing can be adjusted. Therefore, the relationship between the outer diameter and the drawing speed of the glass preform for optical fiber, the shape of the fused part of the glass preform for optical fiber, or the solidification length of the optical fiber immediately after drawing is desired and obtained. The heat transfer coefficient of the inert gas is controlled in a feed-forward manner so that the shape of the melted portion of the glass preform for optical fiber or the solidified length of the optical fiber immediately after drawing becomes a desired length. as a result,
Even if the outer diameter of the glass base material for optical fibers becomes large and the drawing speed becomes high, the solidification length can be maintained at an appropriate length, and it is not necessary to provide partition walls, etc. Can be manufactured.

As a method for changing the heat transfer coefficient, it is preferable to use a plurality of inert mixed gases having different heat transfer coefficients and change the mixing ratio of these inert gases. When this mixed gas is introduced toward the heating and melting part of the glass preform for optical fibers, the drawing conditions can be controlled efficiently. When a carbon electric furnace is used as the drawing furnace, it is preferable to use argon and helium as the inert mixed gas and change the mixing ratio of argon and helium to change the heat transfer coefficient.

A second aspect of the optical fiber drawing method of the present invention will be described. The present inventor has also found that the temperature of the tip of the optical fiber drawn from the heated and melted portion of the glass preform for optical fiber defines the drawing condition of the optical fiber. Therefore, the temperature of the tip of the optical fiber is measured, and the inert gas introduced into the drawing furnace is adjusted so that the measured value is substantially below the softening temperature of the optical fiber.
Since this feedback control directly monitors the softening condition of the optical fiber, the optical fiber can be manufactured with high quality and the solidified length of the optical fiber is maintained at a predetermined length. Even if the outer diameter becomes large and the drawing speed becomes high, a high-quality optical fiber can be manufactured without increasing the solidification length. For this adjustment, it is preferable to use a plurality of gases having different heat transfer coefficients such as argon gas and helium gas as the inert gas, and change the mixing ratio of these mixed gases according to the deviation of the measured temperature from the softening temperature. Let Also in this case, similarly to the above, it is preferable to introduce the mixed gas toward the heating and melting portion of the glass preform for optical fibers.

A third aspect of the optical fiber drawing method of the present invention will be described. The outer diameter of the drawn optical fiber outside the drawing furnace is one factor indicating the final quality of the optical fiber. Therefore, using the conventionally used outer diameter measuring device, the outer diameter of the optical fiber drawn out from the drawing furnace is measured, and the fluctuation per unit time of the measured outer diameter is kept within a set value. The feedback adjustment of the inert gas introduced into the drawing furnace is performed. Feedback control of the inert gas introduced into the drawing furnace can guarantee the quality in the final product stage. Also in this case, it is preferable to use a plurality of inert gases having different heat transfer rates as the inert gas, change the mixing ratio of the mixed gas according to the deviation of the measured outer diameter from the reference outer diameter, and mix the mixed gas with the light. It is introduced toward the heating and melting part of the glass preform for fibers.

The above first to third aspects of the optical fiber drawing method of the present invention are different methods.
While these can be carried out independently, they can also be combined appropriately.

[0019]

EXAMPLE A first example of the optical fiber drawing method of the present invention will be described. FIG. 1 shows a configuration diagram of an optical fiber drawing apparatus for carrying out the optical fiber drawing method of the present invention. As shown in FIG. 1, the optical fiber drawing apparatus 1 includes a drawing furnace body 2
A heater 4 and a core tube 6 are provided inside, and a glass preform 8 for an optical fiber is inserted from an upper opening 2a formed in an upper part of a drawing furnace body 2 and heated and melted into a meniscus-shaped optical fiber. For example, an optical fiber 10 is drawn from the lower end of the glass base material 8 and has a core with a diameter of 10 μm and a clad with a diameter of 125 μm formed around the core.
Are drawn out from the lower opening 2b.

The argon gas inflow controller 24 and the helium gas inflow controller 26 respectively control the flow rates of the argon gas and the helium gas flowing from the argon gas cylinder (not shown) and the helium gas cylinder (not shown) to the pipeline 24a and the pipeline 26b, respectively. Control. The pipeline 24 a and the pipeline 26 b are connected to the mixer 22, and the argon gas and the helium gas are mixed in the mixer 22 and introduced into the lower part of the drawing furnace body 2 via the gas pipeline 20. It The mixed gas that has flowed into the drawing furnace body 2 from the pipe 20 diffuses into the core tube 6. Argon gas inflow controller 24 and helium gas inflow controller 26
Are electrically connected to the input controller 28.

The input controller 28 is the optical fiber drawing device 1
The operator (operator) inputs the drawing speed of the optical fiber 10 and the outer diameter of the glass preform 8 for an optical fiber, and the inert mixed gas defined according to these set values, that is, in this example, A signal S28a indicating the flow rate of the argon gas and a signal S28b indicating the flow rate of the helium gas are output to the argon gas inflow controller 24 and the helium gas inflow controller 26, respectively, based on the mixing ratio of the argon gas and the helium gas. As a result, the pipeline 2
4a and the conduit 26b, a signal S28a indicating the flow rate of the argon gas and a signal S2 indicating the flow rate of the helium gas.
The argon gas and the helium gas corresponding to 8b are mixed in the flow mixer 22 and introduced as an inert mixed gas through the gas pipe 20 to the lower part of the drawing furnace body 2 and diffused into the core tube 6. In particular, since the above inert gas mixture is directly introduced into the lower part of the furnace core tube 6, that is, in the vicinity of the heated and molten meniscus shaped portion of the glass preform 8 for optical fiber, the influence of the high temperature atmosphere in the drawing furnace body 2 is reduced. At a minimum, the inert gas mixture can be applied to the vicinity of the heated and molten meniscus shaped portion of the glass preform 8 for optical fiber, that is, the drawing start portion of the optical fiber.

As the inert mixed gas, a mixed gas of argon gas and helium gas is suitable when the drawing furnace body 2 is an electric furnace made of carbon. In other words, the heat transfer coefficient of helium gas is high, and the heat transfer coefficient of argon gas is low,
It is suitable for mixing and adjusting the heat transfer rate.
When a carbon electric furnace is used as the drawing furnace body 2, mixing of argon gas and helium gas is preferable from the viewpoint of reaction with carbon.

Example 1 A glass preform 8 for an optical fiber having an outer diameter of 60 mm was drawn at a drawing speed of 5
When drawing at 00 m / min, from the input controller 28,
Output signals S28a and S28b for causing the argon gas and the helium gas to flow out to the mixer 22 at a mixing ratio of 10: 1 (helium gas mixing ratio of about 0.1) to the argon gas inflow controller 24 and the helium gas inflow controller 26. did. The outer diameter variation of the drawn optical fiber 10 under this condition is good, and the drawn optical fiber 1
The breakage probability and the transmission loss of 0 are described, for example, in JP-A-1-
As disclosed in Japanese Laid-Open Patent Publication No. 275443, it was almost the same as when an optical fiber glass preform having an outer diameter of 50 mm was drawn at 300 m / min with a conventional optical fiber drawing apparatus.

That is, according to this embodiment, the outer diameter of the glass preform for optical fibers is increased, and even if the drawing speed is increased, there is no problem in transmission loss, and a high-quality optical fiber can be manufactured. There is. Therefore, as in this embodiment, the argon gas and the helium gas are used.
The number of breaks in the optical fiber according to the present embodiment is significantly improved as compared with the method disclosed in Japanese Patent No. 231439 as the prior art. Further, this embodiment means that the mixing ratio of expensive helium gas is lower than that of argon gas, and the optical fiber 10 can be manufactured at a low cost.
Further, in this embodiment, even if the outer diameter of the glass preform 8 for optical fiber becomes large and the drawing speed becomes high, the method disclosed in Japanese Patent Laid-Open No.
As described in JP-A-275443, the solidification length does not increase and it is not necessary to provide partition walls. Therefore, unlike the drawing apparatus described in Japanese Patent Laid-Open No. 1-275443, the drawing apparatus of this embodiment does not become large. From this point as well, according to this embodiment, the manufacturing cost of the optical fiber does not soar. As described above, Japanese Patent Publication No. 62-4333 discloses that argon gas and helium gas are used in order to keep the inside of the drawing furnace clean from the viewpoint of preventing oxidation wear of the drawing furnace and generation of dust. Although only disclosed, no consideration is given to the increase of the outer diameter of the glass preform 8 for an optical fiber and the speeding up of the drawing speed, which is the object of the present invention. However, it is described in Japanese Patent Publication No. 62-4333. Even with this method, as shown in this example, it is not possible to prevent the solidification length from increasing. This embodiment is further described in JP-A-60
As disclosed in Japanese Patent No. 231439, it is not necessary to construct a drawing furnace using zirconia, and a normal carbon electric furnace can be used. In addition, this embodiment is described in JP-A-30-
As disclosed in Japanese Patent No. 15340, it is not necessary to forcibly cool the helium gas, and a cooling device is unnecessary.

Example 2 A glass preform 8 for an optical fiber having an outer diameter of 80 mm was drawn at a drawing speed of 8
When the line drawing is performed at 00 m / min, a signal S28a that causes the input controller 28 to flow the argon gas and the helium gas to the mixer 12 at a flow rate ratio of 4: 1 (helium gas mixing ratio is 0.2), S28b is an argon gas inflow controller 24 and a helium gas inflow controller 2
Output to 6. Optical fiber 10 drawn under this condition
As in Example 1, the outer diameter variation was good, and the breakage probability and transmission loss of the optical fiber 10 were almost the same as those in Example 1. That is, this Example 2 shows that the quality of the optical fiber is high even when the glass base material 8 for an optical fiber has a large outer diameter and is drawn at a high speed.

Comparing Example 1 and Example 2, when a carbon electric furnace is used for the drawing furnace body 2 and a mixed gas of argon gas and helium gas is used, the glass base material 8 for optical fiber is It can be seen that there is an appropriate mixing ratio of helium gas depending on the size of the outer diameter depending on the drawing speed. As described above, in the optical fiber drawing device 1 of the present embodiment, the argon gas and the helium gas are mixed at the mixing ratio determined according to the outer diameter of the glass preform 8 for optical fiber and the drawing speed of the optical fiber 10. The heat transfer coefficient of the inert gas is changed by mixing, and the inert gas mixture is introduced so as to hit the meniscus portion from the lower portion of the drawing furnace body 2. As a result, it is possible to keep the temperature of the drawn optical fiber 10 below the softening point while maintaining the temperature of the meniscus portion of the optical fiber glass preform 8 at an appropriate level. The solidified length of the fiber 10 can be adjusted appropriately to manufacture a high quality drawn optical fiber 10.

A second embodiment of the optical fiber drawing method of the present invention will be described. The second embodiment uses the optical fiber 10
In order to reduce the fluctuation of the outer diameter of the optical fiber, the details will be described with reference to a drawing apparatus for carrying out the optical fiber drawing method shown in FIG. Of the components shown in FIG. 2, FIG.
The components with the same numbers as are the same as those described in the first embodiment. As shown in FIG. 2, the drawing device 31 includes a radiation thermometer 36 as a non-contact temperature measuring device for measuring the temperature of the optical fiber 10 below the lower opening 2b of the drawing furnace body 2.
Is provided. A signal S36 corresponding to the measured temperature is output from the radiation thermometer 36 to the calculator 38. Calculator 38
Compares the measured temperature indicated by the signal S36 with a predetermined reference temperature, and based on the comparison result (deviation),
The mixing ratio of the argon gas and the helium gas introduced into the drawing furnace body 2 which is a carbon electric furnace is determined.

When the temperature measured by the radiation thermometer 36 is higher than the reference temperature, the mixing ratio is determined by increasing the mixing ratio of the helium gas in order to increase the heat transfer coefficient of the gas mixture. When the measured temperature is lower than the reference temperature, conversely, the mixing ratio of the helium gas is reduced to reduce the heat transfer coefficient of the mixed gas. As the reference temperature,
For example, the temperature is the softening point of the optical fiber 10.

The calculator 38 outputs a signal S38a indicating the flow rate of the argon gas according to the mixing ratio thus determined.
And a signal S38b indicating the flow rate of helium gas are output to the argon gas inflow controller 24 and the helium gas inflow controller 26, respectively.

Example 3 A glass preform 8 for an optical fiber having an outer diameter of 80 mm was drawn at a drawing speed of 3.
The mixing ratio of the argon gas and the helium gas was controlled via the calculator 38 so that the temperature measured by the radiation thermometer 36 was 1400 ° C., which is the softening point temperature, drawn by drawing from 00 to 800 m / min. As a result, the drawn optical fiber 10
The fluctuation of the outer diameter was good as in the above-mentioned examples. Also,
As shown in FIG. 3, as the drawing speed becomes higher, the length of the drawn optical fiber that is not cooled becomes longer, so that the temperature measured by the radiation thermometer 36 rises, and accordingly the helium gas in the mixed gas is mixed. The ratio is increased to facilitate cooling of the optical fiber 10 and maintain the solidified length of the optical fiber 10 at a predetermined length. Therefore, also in this embodiment,
Solidification length does not increase.

As described above, this embodiment uses the radiation thermometer 3
6 is used to measure the temperature of the optical fiber 10 in the vicinity of the lower opening 2b of the drawing furnace body 2, and the measured temperature is used as the measured temperature.
The heat transfer coefficient of the mixed gas flowing into the drawing furnace body 2 is adjusted so as to be equal to or lower than the softening point. As a result,
Also, the solidified length of the optical fiber 10 from the tip of the meniscus portion of the optical fiber glass preform 8 is appropriately maintained, and the transmission loss of the optical fiber 10 and the outer diameter fluctuation of the drawn optical fiber 10 are suppressed. It was possible to manufacture a high-quality optical fiber 10 having excellent transmission characteristics and strength. Further, in this embodiment, the radiation thermometer 36 is used to measure the temperature of the optical fiber 10 in the vicinity of the lower opening 2b of the drawing furnace body 2 and feedback control is performed to control the flow rate of the mixed gas, so that process fluctuations, etc. Even if this occurs, an optical fiber with high quality and high accuracy can be manufactured.

A third embodiment of the optical fiber drawing method of the present invention will be described. FIG. 4 shows a block diagram of a wire drawing apparatus for carrying out the third embodiment. FIG. 1 among the components shown in FIG.
The components with the same numbers as are the same as those described in the first embodiment. The drawing device 41 shown in FIG. 4 measures the outer diameter of the optical fiber 10 drawn from the glass preform 8 for optical fiber by using an outer diameter measuring device 42 that is usually provided, and The diameter is used as the feedback signal S42,
Output to the calculator 44. The calculator 44 is the outer diameter measuring device 42.
Continuously input the outer diameter measurement signal S42 from the
In the drawing furnace body 2, the fluctuation of the measurement outer diameter per unit time is calculated based on the measurement outer diameter shown by 2, and the calculated fluctuation per unit time is equal to or less than a preset set value. The mixing ratio of the argon gas and the helium gas to be flown into is determined. For example, when the fluctuation of the outer diameter of the optical fiber 10 is large, the mixing ratio of the helium gas is increased according to the fluctuation and the heat transfer coefficient of the inert mixed gas is increased. First, the cooling of the optical fiber 10 is promoted to maintain the outer diameter of the optical fiber 10 at a predetermined value. Further, the solidification length is maintained at a predetermined value. The calculator 44 outputs the signal S44a indicating the flow rate of the argon gas according to the determined mixing ratio and the S signal 4 indicating the flow rate of the helium gas.
4b is output to the argon gas inflow controller 24 and the helium gas inflow controller 26, respectively.

Also in this embodiment, even if the outer diameter of the optical fiber glass preform 8 is large and the drawing speed is high, the outer diameter fluctuation of the optical fiber 10 can be suppressed, and the transmission characteristics and the strength can be improved. It is possible to manufacture an excellent high-quality optical fiber 10. In the optical fiber drawing device 41, the outer diameter variation of the optical fiber 10 is measured online and the measurement result is used as a feedback signal, as in the second embodiment. An optical fiber with high quality and high precision can be manufactured.

As described above, the first to third embodiments based on different points of view have been described independently as the optical fiber drawing method of the present invention. However, in carrying out the present invention, the first to third embodiments are described. It can be appropriately combined. With these combinations, the respective effects of the above-described embodiments can be obtained. Even if these examples are combined, it is not necessary to provide a partition wall or the like at the bottom of the drawing furnace, and it is not necessary to upsize the drawing apparatus. Further, when realizing each embodiment, existing simple control technology and existing low-priced member or existing low-priced component can be applied, and expensive member or advanced control technology can be used for the implementation. It is easy to implement because it is not needed.

Further, in the above embodiment, as the inert mixed gas, an example using argon gas and helium gas, which is suitable when the drawing furnace body 2 is an electric furnace made of carbon, is described. The gas is not limited to argon gas and helium gas, and an appropriate inert gas that does not oxidize and wear the drawing furnace body 2 and does not generate dust depending on the constituent material of the drawing furnace body 2 can be used. . Furthermore, in the above embodiment, an example using a mixed gas as the inert gas was described, but similarly to the above, means for changing the heat transfer coefficient, for example, a device capable of cooling gas cooling and adjusting the flow rate thereof is provided. If used, only a single inert gas, eg, argon gas, can be used.

[0036]

As described above, according to the optical fiber drawing method of the present invention, the drawing apparatus is complicated by adjusting the heat transfer coefficient of the inert mixed gas flowing into the drawing furnace body. Alternatively, even if the optical fiber glass preform having a large outer diameter is drawn at a high drawing speed, a high-quality optical fiber having excellent strength and transmission characteristics can be manufactured.

[Brief description of drawings]

FIG. 1 is a first embodiment of the optical fiber drawing method of the present invention.
It is a block diagram of the optical fiber drawing apparatus as an Example of.

FIG. 2 is a second embodiment for carrying out the optical fiber drawing method of the present invention.
It is a block diagram of the optical fiber drawing apparatus as an Example of.

FIG. 3 is a graph showing the relationship between the drawing speed and the mixing ratio of helium in the optical fiber drawing device according to the second embodiment.

FIG. 4 is a third embodiment for carrying out the optical fiber drawing method of the present invention.
It is a block diagram of the optical fiber drawing apparatus as an Example of.

FIG. 5 is a configuration diagram showing an example of a conventional optical fiber drawing device.

[Explanation of symbols]

 1, 31, 41 ... Optical fiber drawing device 2 ... Drawing furnace body 2a, 2b, 12a ... Opening part 4 ... Heater 6 ... Reactor tube 8 ... Glass for optical fiber Base material 10 ... Optical fiber 12 ... Partition wall 14, 20, 24a, 26a ... Pipe line 24, 16 ... Argon gas inflow controller 26 ... Helium gas inflow controller 28 ... Input controller 36 ... Radiation thermometer 38,44 ... Calculator 42 ... Outer diameter measuring instrument

 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Tamotsu Kamiya 2-6-1, Marunouchi, Chiyoda-ku, Tokyo Furukawa Electric Co., Ltd.

Claims (13)

[Claims] 1. A method for drawing an optical fiber by heating and drawing an optical fiber glass preform, wherein the heat transfer coefficient of an inert gas introduced into a drawing furnace is set to the outer diameter of the optical fiber glass preform and The shape of the molten portion of the glass base material for an optical fiber, which is changed according to the drawing speed, or
A method for drawing an optical fiber, which comprises adjusting the solidification length of the optical fiber immediately after drawing. 2. A plurality of inert mixed gases having different heat transfer coefficients are used as the inert gas, and the heat transfer coefficient is changed by changing a mixing ratio of these inert gases, and the mixed gas is supplied to the optical fiber. The optical fiber drawing method according to claim 1, wherein the glass base material is introduced toward the heating and melting portion of the glass base material. 3. A carbon electric furnace is used as the drawing furnace, argon and helium are used as the inert gas mixture, and the heat transfer coefficient is changed by changing the mixing ratio of the argon and helium. 2. The optical fiber drawing method described in 2. 4. A method of drawing an optical fiber by heating and drawing an optical fiber glass preform, wherein the temperature of the tip of the optical fiber drawn from the heated and melted portion of the optical fiber glass preform is measured. A method for drawing an optical fiber, wherein the inert gas introduced into the drawing furnace is adjusted so that the measured value is substantially equal to or lower than the softening temperature of the optical fiber. 5. A plurality of gases having different heat transfer coefficients are used as the inert gas, and a mixing ratio of the mixed gas is changed according to a deviation of the measured temperature from the softening temperature, and the mixed gas is mixed with the optical fiber. The optical fiber drawing method according to claim 4, wherein the optical glass fiber is introduced toward the heating and melting portion of the glass preform. 6. The optical fiber drawing method according to claim 5, wherein a carbon electric furnace is used as the drawing furnace, and argon and helium are used as the inert mixed gas. 7. A method for drawing an optical fiber by heating and drawing a glass preform for an optical fiber, wherein the outside diameter of the drawn optical fiber outside the drawing furnace is measured, and the measured outside diameter per unit time. The method for drawing an optical fiber is characterized in that the inert gas introduced into the drawing furnace is adjusted so that the fluctuation of the above is within a set value. 8. A plurality of inert gases having different heat transfer coefficients are used as the inert gas, and a mixing ratio of the mixed gas is changed according to a deviation of the measured outer diameter from a reference outer diameter. The method for drawing an optical fiber according to claim 7, wherein the glass base material for an optical fiber is introduced toward a heating and melting portion. 9. The method of drawing an optical fiber according to claim 8, wherein a carbon electric furnace is used as the drawing furnace, and argon and helium are used as the inert mixed gas. 10. The temperature of the tip portion of the optical fiber drawn from the heated and melted portion of the glass base material for optical fiber is measured, and the measured value is kept within the softening temperature of the optical fiber in the drawing furnace. The method for drawing an optical fiber according to any one of claims 1 to 3, wherein an inert gas to be introduced into the device is adjusted. 11. A plurality of gases having different heat transfer coefficients are used as the inert gas, and a mixing ratio of the mixed gas is changed according to a deviation of the measured temperature from the softening temperature, and the mixed gas is mixed with the optical fiber. The optical fiber drawing method according to claim 10, wherein the glass base material is introduced toward the heating and melting portion. 12. An optical fiber outside the drawing furnace, which has been drawn, is measured, and an optical fiber is introduced into the drawing furnace so that the fluctuation of the measured outside diameter per unit time is within a set value. The method for drawing an optical fiber according to claim 10, wherein the active gas is adjusted. 13. A plurality of inert gases having different heat transfer coefficients are used as the inert gas, and a mixing ratio of the mixed gas is changed according to a deviation of the measured outer diameter from a reference outer diameter. The optical fiber drawing method according to claim 12, wherein the glass base material for an optical fiber is introduced toward a heating and melting portion.