JP2012116731A - Method for manufacturing optical fiber preform - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method for manufacturing an optical fiber perform, which can reduce surplus glass microparticles floating in a reaction vessel, and can reduce the adhesion of exfoliated scraps to a target.SOLUTION: One embodiment of the present invention includes a step of arranging a target 107 between an exhaust port 104a and a burner 103, and a step of feeding glass microparticles to the target 107 and depositing the glass microparticles while forming a flow of a clean air directing to the exhaust port 104a. In the deposition step, wind velocities of the clean air at positions of an upper stage α, a middle stage β and a lower stage γ are set such that the wind velocity of the clean air at the middle stage β is made ≥0.8 m/s; 1≤(a wind velocity of the clean air at the middle stage β)/(a larger wind velocity out of a wind velocity of the clean air at the lower stage γ and a wind velocity of the clean air at the upper stage α) and (a wind velocity of the clean air at the middle stage β)/(a smaller wind velocity out of a wind velocity of the clean air at the lower stage γ and a wind velocity of the clean air at the upper stage α)≤10 are satisfied.

Description

  The present invention relates to a method for manufacturing an optical fiber preform, and more specifically, while supplying a raw material gas to a starting preform (hereinafter also referred to as a “target”), a flame from a burner causes the surface of the starting preform to be formed. The present invention relates to a method for manufacturing an optical fiber preform forming soot.

  As a method for manufacturing an optical fiber preform, while supplying air as a cleaning gas from the periphery of the burner to the target, a flame, a raw material gas and a combustion gas are supplied from the burner to the target, and glass is supplied to the target. It has been proposed to deposit fine particles (see Patent Document 1). FIG. 1 is a schematic configuration diagram of a manufacturing apparatus that performs the method for manufacturing an optical fiber preform described in Patent Document 1. In FIG. 1, a manufacturing apparatus 1 includes a reaction vessel 3 that contains a rotating target 2, and a burner that sprays glass fine particles generated by a flame hydrolysis reaction of a glass raw material gas 4 a and a combustion gas 4 b toward the target 2. 5, a moving mechanism 6 that relatively moves the target 2 and the burner 5, and a clean air generator 8 for supplying clean air 7 that is a cleaning gas into the reaction vessel 3.

  A through hole is provided in the upper wall 3a of the reaction vessel 3, and the target 2 is disposed so as to be inserted through the through hole in the vertical direction. The target 2 is configured such that the upper end is gripped and rotated by the rotary chuck 9 and is reciprocated in the vertical direction by the moving mechanism 6. In this manner, the porous glass base material 10 is formed by uniformly depositing glass particles on the surface of the target 2 by reciprocating the target 2 along the axial direction while rotating the target 2.

  A clean air supply chamber 12 to which clean air 7 is supplied from a clean air generator 8 through a pipe 11 is provided on the side wall 3 b of the reaction vessel 3. The clean air supply chamber 12 has an opening 12 a, and the clean air 7 supplied from the clean air generator 8 to the clean air supply chamber 12 through the pipe 11 passes through the opening 12 a to the inside of the reaction vessel 3. To be supplied. Thereby, the clean air 7 can be sprayed with respect to the porous glass base material 10 under manufacture, and the excess glass fine particles floating in the reaction vessel 3 can be reduced.

  Further, a burner 5 is attached horizontally through the center of the clean air supply chamber 12, and the tip projects into the reaction vessel 3. The burner 5 has a port for blowing out gas formed concentrically with a port for blowing out flame. The burner 5 is connected to the gas supply device 14 by a pipe 13 (only one is shown in FIG. 1) provided for each port. The gas supply device 14 includes a combustion gas supply device and a raw material gas supply device, and is configured to supply the glass raw material gas 4 a and the combustion gas 4 b to each port of the burner 5.

  On the side wall 3c opposite to the side wall 3b provided with the burner 5 of the reaction vessel 3, an exhaust duct 15 for sucking and exhausting the gas in the reaction vessel 3 is provided to the outside. Thus, the air 7 and the glass fine particles in the reaction vessel 3 are exhausted.

  In Patent Document 1, in the manufacturing apparatus shown in FIG. 1, the supply flow rate of the clean air 7 is the average of all the gases blown out from the burner 5 including the supply flow rate of the glass raw material gas 4a and the glass raw material gas 4a and the combustion gas 4b. The excess glass fine particles floating in the reaction vessel 3 are reduced by controlling the flow rate to be at least 0.3 to 1.0 times the supply flow rate.

JP 2006-24884 A

If the excessive glass fine particles or the like adhere to the porous glass base material 10, the porous glass base material 10 may be damaged or the appearance may be deteriorated. Therefore, it is desired to reduce excess glass fine particles.
Now, the excess glass fine particles or the like adhere to the reaction vessel 3, and the adhering matter may be peeled off when the adhering amount exceeds a predetermined amount. In the present specification, such an exfoliated material (glass fine particles) once adhered to the reaction vessel is referred to as “peeling waste”. If the peeling waste adheres to the porous glass base material 10, it may cause damage to the porous glass base material 10 and poor appearance. Therefore, it is desired to reduce the generation of the above-mentioned peeling waste.

  However, in Patent Document 1, only the ratio of the clean air 7 to at least one of the glass raw material gas 4a and the average supply flow velocity is defined, and the effect varies greatly depending on the wind speed of the clean air 7. For example, when the wind speed of the clean air 7 is low, excess glass fine particles that are not exhausted adhere to the walls of the reaction vessel 3 (the upper wall 3a, the side walls 3b, 3c, etc.) May be peeled off to form peeling waste, which may adhere to the porous glass base material 10 which is a product soot.

Moreover, in patent document 1, as FIG. 1 shows, the exhaust duct 15 (exhaust port through which the exhausted gas passes) provided facing the area | region (arrangement position of the burner 5) to which clean air 7 is supplied. 15a) is small, the wind speed distribution of the clean air 7 is very large in the direction of gravity in the reaction vessel 3. Specifically, the wind speed at the middle stage in the gravity direction P in the reaction vessel 3 located between the exhaust port 15a of the exhaust duct 15 and the opening 12a that is the supply port of the clean air 7 is the gravity direction P. The wind speed at the upper stage (the ceiling (upper wall 3a) side of the reaction vessel 3) and the lower stage (the bottom side of the reaction vessel 3) in FIG. That is, since the wind speed is very small (for example, a value close to 0) in the upper and lower stages, the glass fine particles floating in the middle stage are moved to the exhaust duct 15 by the action of the clean air 7. However, in the upper stage and the lower stage, since the wind speed of the clean air 7 is very low, the amount of glass particles exhausted to the exhaust duct 15 is reduced, and the amount of floating glass particles is reduced. It is difficult.
Therefore, conventionally, there is a limit in reducing the excessive glass fine particles, and there is also a limit in reducing the adhesion of peeling waste to the target.

  The present invention has been made in view of such problems, and the object of the present invention is to reduce the excess glass fine particles floating in the reaction vessel and to reduce the adhesion of peeling debris to the target. An object of the present invention is to provide a method for manufacturing a possible optical fiber preform.

  In order to achieve such an object, the present invention provides an optical fiber preform manufacturing method in which glass particulates are supplied to a starting preform disposed in a reaction vessel and the glass particulates are deposited on the starting preform. A step of disposing the starting base material between an exhaust port provided in a side wall other than a ceiling and a bottom of the reaction vessel and a supply unit of the glass fine particles, and the glass fine particles in the reaction vessel. Introducing a predetermined gas that does not react and supplying the glass fine particles to the starting base material while depositing the glass fine particles on the starting base material while forming the predetermined gas flow toward the exhaust port; And in the step of depositing, a position of 10% of the distance between the ceiling and the bottom of the reaction vessel in the direction from the ceiling of the reaction vessel to the bottom of the reaction vessel. The upper position, When the position of 10% of the distance from the bottom in the direction from the part toward the ceiling is the lower position, and the middle position between the ceiling and the bottom in the direction of gravity is the middle position, The wind speed of the predetermined gas at the middle position is 0.8 m / s or more, and 1 ≦ (wind speed of the predetermined gas at the middle position / wind speed of the predetermined gas at the lower position and The larger of the wind speeds at the upper position) ≦ 10 and 1 ≦ (wind speed at the middle position of the predetermined gas / wind speed at the lower position of the predetermined gas and the upper speed) The wind speed of the predetermined gas at the upper position, the middle position, and the lower position is set so as to satisfy the smaller one of the wind speeds at the position) ≦ 10. To do.

  According to the present invention, it is possible to reduce excess glass fine particles floating in the reaction vessel, and it is also possible to reduce adhesion of exfoliation waste to the target.

It is a schematic block diagram of the manufacturing apparatus of the conventional optical fiber preform. It is a top view of the manufacturing apparatus of the optical fiber preform which concerns on one Embodiment of this invention. FIG. 3 is a cross-sectional view taken along line A-A ′ in FIG. 2. It is a block diagram which shows schematic structure of the control system in the manufacturing apparatus of the optical fiber preform based on this invention. It is a top view of the manufacturing apparatus of the optical fiber preform which concerns on one Embodiment of this invention. FIG. 6 is a cross-sectional view taken along line B-B ′ of FIG. 5.

Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. In the drawings described below, components having the same function are denoted by the same reference numerals, and repeated description thereof is omitted.
(First embodiment)
FIG. 2 is a top view of the vertical optical fiber preform manufacturing apparatus according to this embodiment, and FIG. 3 is a cross-sectional view taken along line AA ′ of FIG.
2 and 3, the manufacturing apparatus 100 includes a reaction vessel 101, a clean air supply chamber 102 provided in communication with the reaction vessel 101 on the supply-side side wall 101 a of the reaction vessel 101, and the clean air supply. The burner 103 is disposed so as to protrude from the chamber 102 into the reaction vessel 101, and the exhaust port 104a provided on the side wall 101b (exhaust side side wall) of the reaction vessel 101 opposite to the side wall 101a. And an exhaust mechanism 104. The exhaust mechanism 104 has a pump, and by driving the pump in accordance with an instruction from the control unit 200 described later, the exhaust side (exhaust port 104a) of the reaction vessel 101 is supplied from the supply side (supply port 105). ) Can be formed, and the reaction vessel 101 can be evacuated. The clean air supply chamber 102 is provided with an air supply port 105. The clean air generator 116 and the air supply port 105 are connected by a clean air supply line 115, and the clean air supply chamber 102 is cleaned in accordance with an instruction from the control unit 200 described later. The air generator 116 supplies clean air to the clean air supply chamber 102 via the clean air supply line 115 and the air supply port 105.

  The manufacturing apparatus 100 further includes a spindle mechanism 106 provided on the ceiling 101c and the bottom 101d of the reaction vessel 101. The spindle mechanism 106 is coupled to a pair of chucks 109 that hold support members 108 connected to both ends of a target 107 as a starting base material. The spindle mechanism 106 reciprocates the target 107 in the longitudinal direction L in accordance with an instruction from the control unit 200 to be described later, and rotates the target 107 in the rotational direction R with the longitudinal direction of the target 107 as a rotational axis. That is, the spindle mechanism 106 is configured to reciprocate the target 107 with respect to the burner 103 and rotate the target 107 about the axis of the target 107 in order to deposit the soot 110 on the outer periphery of the target 107.

The manufacturing apparatus 100 discharges the flame 111 containing soot glass particles from the burner 103 on the outer periphery of the rotating target 107 while reciprocating the target 107 along the longitudinal direction inside the reaction vessel 101. As a result, the glass particles synthesized by the burner 103 are deposited on the outer periphery of the target 107 to form the soot 110.
The burner 103 is supplied with combustion gas from the combustion gas supply device 114a through the combustion gas supply line 112a, and from the glass raw material gas supply device 114b through the glass raw material gas supply line 112b. Gas which becomes glass fine particles by decomposition) is supplied. The combustion gas supply device 114 a supplies the burner 103 with at least one of combustion gas, for example, hydrogen (H ₂ ) and oxygen (O ₂ ), whose flow rate is controlled independently in accordance with an instruction from the control unit 200 described later. Further, the glass source gas supply device 114b supplies a glass source gas (for example, SiCl ₄ ) whose flow rate is controlled to the burner 103 as a raw material for synthesizing the optical fiber preform in accordance with an instruction from the control unit 200 described later.

  The burner 103 forms a flame with the combustion gas supplied from the combustion gas supply device 114a in accordance with an instruction from the control unit 200 described later, and hydrolyzes the glass raw material gas supplied from the glass raw material gas supply device 114b in the flame. Then, glass fine particles are formed, and a flame 111 containing these is blown onto the target 107 to deposit the glass fine particles to form the soot 110.

  In the reaction vessel 101 and the clean air supply chamber 102, a flow guide 113, which is a member for adjusting the wind speed of clean air from the clean air supply chamber 102 toward the exhaust mechanism 104, is provided. In the present embodiment, by designing the shape and arrangement position of the flow guide 113 according to the structure and shape of the manufacturing apparatus 100 such as the structure of the reaction container 101, the clean air supply chamber 102, and the exhaust mechanism 104, the reaction container 100 is designed. Inside, the wind speed in the direction of gravity can be set to a desired distribution.

  In the present embodiment, clean air (cleaned air) is used as a gas for reducing the exhaust of floating glass particles and the adhesion of exfoliation debris to the target. However, the present invention is not limited to this. . In the present invention, a gas is supplied separately from a gas for forming glass fine particles such as a glass raw material gas and a combustion gas, so that it does not affect soot formation and does not contribute to soot formation on the target, and floats excessively. It is important to guide the fine glass particles to the exhaust port, and any gas may be used as long as the function can be achieved. That is, any gas may be used as long as it is a gas that does not react with the glass fine particles or the soot 110 existing in the reaction vessel 101, such as nitrogen. Further, in the case where the glass raw material gas is supplied from the burner 103 as in this embodiment, in addition to the requirements, any gas may be used as long as it does not react with the glass raw material gas in the flame from the burner. May be.

In the present embodiment, as an example, the size of the exhaust port 104a (the diameter in the gravity direction in the reaction vessel 100 (hereinafter also referred to as “gravity direction diameter”)), the control of the exhaust amount of the exhaust mechanism 104, and the flow guide 113. The wind speed distribution of clean air is controlled by the arrangement of That is, in the present embodiment, the gravity direction diameter of the exhaust port 104a is increased as shown in FIG. 3 (for example, the gravity direction diameter is longer than the longitudinal direction of the target 107). By appropriately adjusting the amount of exhaust air, the clean air supplied from the clean air supply chamber 102 to the reaction vessel 101 is not only near the center in the gravity direction of the reaction vessel 100 but also on the ceiling side of the reaction vessel (near the ceiling 101c). ) And the bottom side (near the bottom 101d) can also establish a flow of clean air. At this time, by appropriately providing the flow guide 113, the wind velocity distribution in the gravity direction in the reaction vessel 101 can be more favorably formed.
In the present embodiment, for example, polycarbonate may be used as the flow guide 113 far from the burner 103. Further, as the flow guide 113 closer to the burner 103, for example, a heat-resistant black paint applied to aluminum may be used. Alternatively, stainless steel or titanium coated with heat-resistant black may be used.

  In the present invention, it is important to form a wind speed distribution characteristic of the present invention as described later in the direction of gravity in the reaction vessel 101. Therefore, if the wind speed distribution characteristic of the present invention can be formed, the wind speed distribution by controlling the size of the exhaust port 104a, the exhaust amount of the exhaust mechanism 104, and the arrangement of the flow guide 113 as in this embodiment. The wind speed distribution adjustment may be performed not only by the formation but also by an arbitrary combination of the three parties, or only by controlling the exhaust amount of the exhaust mechanism 104 or only by the arrangement of the flow guide 113. Also good.

The above-described manufacturing apparatus 100 can incorporate the control unit 200 shown in FIG. Further, the control unit may be connected through an interface.
FIG. 4 is a block diagram showing a schematic configuration of the control system according to the present embodiment.
In FIG. 4, reference numeral 200 denotes a control unit as control means for controlling the entire apparatus 100. The control unit 200 includes a CPU 201 that executes processing operations such as various calculations, controls, and determinations, and a ROM 202 that stores various control programs executed by the CPU 201. In addition, the control unit 200 includes a RAM 203 that temporarily stores data during processing operations of the CPU 201, input data, and the like, and a nonvolatile memory 204 such as a flash memory and an SRAM.

  The control unit 200 includes a keyboard for inputting predetermined commands or data, an input operation unit 205 including various switches, and a display unit for performing various displays including the input / setting state of the manufacturing apparatus 100. 206 (for example, a display) is connected. Further, the clean air generator 116, the spindle mechanism 106, the combustion gas supply device 114a, the glass raw material gas supply device 114b, the exhaust mechanism 104, and the burner 103 are connected to the control unit 200 via drive circuits 207a to 207f, respectively. Has been.

  In such a configuration, the present embodiment particularly reduces the adhesion of glass particles to the ceiling 101c and the bottom 101d of the reaction vessel 101, and prevents the debris generated from the ceiling 101c and the bottom 101d from adhering to the soot 110. In the direction of gravity of the reaction vessel 101, appropriate cleanliness is achieved at a predetermined upper position, a predetermined middle position, and a predetermined lower position. It is characterized by forming a wind speed distribution of air. That is, the upper part in the reaction vessel 101 has both the effects of reducing the adhesion of the glass particles to the ceiling 101c and the bottom 101d and reducing the adhesion of the debris generated from the ceiling 101c and the bottom 101d to the soot 110. A wind speed distribution of clean air is formed in (the position of the upper stage and its vicinity), the middle part (the position of the middle stage and its vicinity), and the lower part (the position of the lower stage and its vicinity).

  In the present specification, the “upper position of the reaction vessel 101 in the direction of gravity (hereinafter sometimes simply referred to as“ upper stage ”)” means from the ceiling 101c in the direction from the ceiling 101c to the bottom 101d. , 10% of the distance between the ceiling 101c and the bottom 101d, and “the lower position in the direction of gravity of the reaction vessel 101 (hereinafter sometimes simply referred to as“ lower stage ”)” refers to the bottom 101d. 10% of the distance between the ceiling 101c and the bottom 101d in the direction of gravity from the bottom 101d in the direction from the bottom to the ceiling 101c. In addition, “the middle position of the reaction vessel 101 in the gravity direction (hereinafter sometimes simply referred to as“ middle stage ”)” refers to the middle position between the ceiling 101c and the bottom 101d in the gravity direction.

  Usually, the target 107 is arranged so that a part of the target 107 is located in the middle stage of the reaction vessel 101. Therefore, the burner 103 is also often arranged near the middle stage, and the flame 111 containing glass particles is often blown out near the middle stage. Accordingly, there are a lot of surplus glass fine particles floating around the middle stage. Therefore, in this embodiment, in the wind speed distribution in the direction of gravity, the wind speed of the clean air at the middle stage is set to 0.8 m / s or more, and the wind speed of the clean air is set so that the wind speed at the middle stage is the strongest.

  Furthermore, in this embodiment, in order to reduce the attachment of surplus glass particles floating on both the ceiling 101c and the bottom 101d, both the upper side in the gravitational direction in the reaction vessel 101 and the lower side in the gravitational direction. The technical idea is to form a wind speed distribution in the direction of gravity so that a flow of clean air with a predetermined wind speed is formed. In order to realize the technical idea, in the present embodiment, 1 ≦ a (a: the wind speed at the middle stage of the clean air / the wind speed at the lower stage of the clean air and the wind speed at the upper stage) ≦ 10, And 1 ≦ b (b: wind speed at the middle stage of clean air / wind speed at the lower stage of the clean air and wind speed at the lower stage of the upper stage) ≦ 10 so that the upper, middle, and lower stage clean air Set the wind speed.

Thus, in the direction of gravity in the reaction vessel 101, the clean wind is set to have the highest wind speed at the middle stage, the upper and lower wind speeds are set within a predetermined range below the middle wind speed, and the middle stage wind speed is set to 0. The following effects can be acquired by setting it as 8 m / s or more.
That is, in a form in which a part of the target 107 is located in the normally used middle stage, the wind speed in a region where the surplus of surplus glass fine particles are present (for example, a region within 10% above and below the middle stage) is present. Is set to be the largest and is set to 0.8 m / s or more, so that the flow of clean air from the air supply port 105 to the exhaust port 104a is strongest in the region, and surplus glass fine particles are floating. The flow can be formed so as to be exhausted sufficiently. Therefore, even in the middle stage where the most surplus surplus glass particles are present, the surplus surplus glass particles can be satisfactorily sent to the exhaust port 104a.
Furthermore, by setting the lower and upper wind speeds of clean air so as to satisfy 1 ≦ a ≦ 10 and 1 ≦ b ≦ 10, the flow of clean air with an appropriate wind speed below the middle stage is set at the upper and lower stages. The excess glass particles that can be formed and are scattered toward the ceiling 101c and the bottom 101d can be guided to the exhaust port 104a by the flow of the clean air. That is, since an appropriate flow of clean air is established in the upper stage and the lower stage, it is possible to establish a flow of clean air also in an area between the upper stage and the ceiling 101c and an area between the lower stage and the bottom 101d. In addition, it is possible to reduce the floating of the glass particles in the vicinity of the ceiling 101c and the bottom 101d, and it is possible to reduce the adhesion of the glass particles to the ceiling 101c and the bottom 101d. Furthermore, even if the glass particles adhere to the ceiling 101c and the bottom 101d and the adhered glass particles are peeled off (that is, even if separation debris is generated), the upper and lower stages, and further, the upper and ceiling 101c Since the flow of the clean air is formed between the lower portion and the bottom portion 101d, the generated separation dust is sent to the exhaust port 104a along the flow of the clean air. Therefore, the target 107 is positioned in the air stream of clean air, and even if peeling waste is generated, the adhesion of the peeling waste to the target 107 can be reduced.

  Further, even in a form in which a part of the target 107 is not located in the middle stage, in the gravity direction in the reaction vessel 101, the middle stage has the highest wind speed, and the upper stage and the lower stage have appropriate wind speeds that are lower than the middle stage. Since the wind speed distribution is formed, there is no change in the flow of clean air in the vicinity of the ceiling 101c and the bottom 101d, and the glass fine particles floating in the vicinity of the ceiling 101c and the bottom 101d can be reduced. In addition, even if peeling debris is generated, adhesion to the target 107 can be reduced by the flow of clean air near the ceiling 101c and the bottom 101d.

In addition, a (wind speed at the middle stage of clean air / wind speed at the lower stage of clean air and wind speed at the upper stage), b (wind speed at the middle stage of clean air / wind speed at the lower stage of clean air, and If the value of each of the lower wind speeds in the upper stage is too large, a density distribution is likely to be formed in the longitudinal direction of the soot 110 formed on the target 107. When the density distribution occurs, the outer diameter of the longitudinal length of the preform becomes large and causes deterioration due to drawing. Therefore, adjustment in vitrification is necessary. Furthermore, if a and b are further increased, a large density difference occurs, which affects the longitudinal characteristics of the soot 110 and causes defects. Therefore, it is preferable that a and b are not too large (the difference in wind speed between the middle stage, the upper stage, and the lower stage is not too large). That is, when a and b are 10 or more, a density difference more than expected occurs in the longitudinal direction of the soot 110, and there is a concern about the occurrence of cracks or the like due to distortion during vitrification, making it difficult to form a preform. Accordingly, a ≦ 10 and b ≦ 10 are preferable. When a and b are 5 or more, the longitudinal characteristics of the soot 110 may be affected, and a defect may occur in some of the strands. Therefore, it is more preferable that a ≦ 5 and b ≦ 5.
Furthermore, in consideration of the reduction in the generation of exfoliation debris, it is preferable to prevent the glass particles accumulated on the ceiling 101c and the bottom 101d from being swung by the clean air flowing near the ceiling 101c and the bottom 101d. In addition, it is desirable to suppress the upper and lower wind speeds. Thus, in consideration of preventing the glass fine particles (adhered matter) deposited on the ceiling 101c and the vicinity of the bottom 101d from moving as much as possible, it is preferable that the wind speed of the upper stage and the lower stage be at most the middle stage. . That is, it is preferable that 1 ≦ a and 1 ≦ b.
Considering the above, it is preferable to satisfy 1 ≦ a ≦ 10 and 1 ≦ b ≦ 10, and it is more preferable to satisfy 1 ≦ a ≦ 5 and 1 ≦ b ≦ 5.

Next, a method for producing soot as an optical fiber preform according to the present embodiment will be described.
In this embodiment, prior to the soot formation step, the wind speed of the upper, middle, and lower stages of clean air is such that the wind speed of the middle stage is 0.8 m / s or more, and 1 ≦ a ≦ 10, 1 ≦ b ≦ 10. A measurement step for obtaining in advance parameters (in this case, the supply amount of the clean air supplied from the clean air generator 116 to the clean air supply chamber 102 and the exhaust amount of the exhaust mechanism 104) so as to satisfy an appropriate wind speed satisfying Do.

  First, for example, a target 107 having a core and a clad is manufactured by a normal manufacturing method, and the target 107 is attached to a chuck 109 provided in the reaction vessel 101.

<Measurement process>
Next, the position α (corresponding to the upper stage, also referred to as “upper stage α”), the position β (corresponding to the middle stage, also referred to as “middle stage β”), and the lower stage γ (corresponding to the lower stage, “lower stage γ” in FIG. 3) Anemometers are also installed in each. In this specification, the anemometer installed in the upper stage α is called the upper stage anemometer, the anemometer installed in the middle stage β is called the middle stage anemometer, and the anemometer installed in the lower stage γ is called the lower stage anemometer. I will call it. In the present embodiment, the display unit 206 is configured to display the measurement results of the upper stage anemometer, the middle stage anemometer, and the lower stage anemometer.

  Next, when the user inputs a wind speed measurement instruction via the input operation unit 205, the control unit 200 controls the clean air generator 116 so that a predetermined amount of clean air is supplied based on the input wind speed measurement instruction. The exhaust mechanism 104 is controlled so that a predetermined amount of exhaust is controlled. Thereby, the flow of clean air is established in the reaction vessel 101, and the wind speed of the clean air in each of the upper stage α, the middle stage β, and the lower stage γ is measured by the upper stage anemometer, the middle stage anemometer, and the lower stage anemometer. The measurement result is displayed on the display unit 206.

  The measurement result displayed on the display unit 206 is a desired value in which the wind speed of the middle stage of clean air is 0.8 m / s or more, and satisfies the desired relationship of 1 ≦ a ≦ 10 and 1 ≦ b ≦ 10. For example, the user inputs this via the input operation unit 205, and the control unit 200 stores the current supply amount of clean air from the clean air generator and the exhaust amount of the exhaust mechanism 104 in the RAM 203 as set values. To do.

  On the other hand, the measurement result displayed on the display unit 206 indicates that the wind speed of the middle stage of clean air is not a desired value of 0.8 m / s or more and / or a desired value of 1 ≦ a ≦ 10, 1 ≦ b ≦ 10. When the relationship is not satisfied, the user performs an input for adjusting at least one of the supply amount and the exhaust amount of the clean air via the input operation unit 205, and the control unit 200 performs the input of the clean air supply amount and the exhaust amount according to the input. Adjust at least one of the displacements. In this way, the wind speed is measured again with the adjusted supply amount and the exhaust amount of clean air, and the measurement result is a desired value in which the wind speed of the middle stage of clean air is 0.8 m / s or more, and 1 ≦ a The above adjustment is repeated until the desired relationship of ≦ 10 and 1 ≦ b ≦ 10 is satisfied. If the measurement result after adjustment is the desired value of the wind speed of the middle stage of clean air of 0.8 m / s or more, and satisfies the desired relationship of 1 ≦ a ≦ 10, 1 ≦ b ≦ 10, that effect Is input via the input operation unit 205, and the control unit 200 stores the adjusted clean air supply amount from the clean air generating device and the exhaust amount of the exhaust mechanism 104 in the RAM 203 as set values.

  As described above, when the conditions for achieving the appropriate upper, middle, and lower wind speeds for clean air are finished, the upper, middle, and lower anemometers provided in the reaction vessel 101 And move to the soot formation process.

<Soot formation process>
In the soot formation operation step, the control unit 200 reads the clean air supply amount and the exhaust amount stored in the RAM 203, which are obtained by the above-described condition determination, and operates according to the read values. The clean air generator 116 and the exhaust mechanism 104 are operated. Thus, when the soot is formed, the wind speed distribution of the clean air satisfying a desired value of 0.8 m / s or more and 1 ≦ a ≦ 10 and 1 ≦ b ≦ 10 in the middle stage of the clean air is reacted. It can be formed in the direction of gravity in the container 101. Further, the control unit 200 controls the combustion gas supply device 114a and the glass raw material gas supply device 114b to supply the combustion gas and the glass raw material gas to the burner 103, and controls the burner 103 to emit a flame, soot, A flame 111 containing glass fine particles is discharged from the burner 103. At this time, the spindle mechanism 106 is driven by the control unit 200 to rotate the target 107 in the rotation direction R and move along the longitudinal direction L, thereby forming a flow of clean air toward the exhaust port 104a. The soot 110 is formed on the surface of the target 107.

  In the present embodiment, parameters (in this case, the supply amount of clean air and the exhaust amount) for forming an appropriate speed distribution in the measurement process are stored in the RAM 203, but are stored in the nonvolatile memory 204. Also good. As described above, if stored in the non-volatile memory 204, the configuration of the manufacturing apparatus 100 (for example, the shape and arrangement of the flow guide 113) corresponding to the stored parameters is not changed even in the next soot formation. The appropriate clean air velocity distribution can be realized. Therefore, if the configuration of the manufacturing apparatus 100 is not changed, there is no need to perform a measurement process for each soot formation.

  Further, in this embodiment, after the measurement process is completed, the upper anemometer, the middle anemometer, and the lower anemometer are removed to perform the soot formation process, but the soot formation process is performed with the respective anemometers installed. May be. In this case, also in the soot formation process, the wind speed of the clean air can always be confirmed in the upper stage α, the middle stage β, and the lower stage γ, and each wind speed can be adjusted as desired.

  Further, the upper, middle, and lower air speeds of the clean air when the exhaust amount and the supply amount of clean air are changed with respect to a predetermined configuration of the manufacturing apparatus 100 (for example, a predetermined flow guide installation state). The measurement results may be measured in advance, the measurement results may be tabulated, and the table may be stored in the ROM 202 or the nonvolatile memory 204. In this case, the user can set each desired speed of the clean air through the input operation unit 205 such that the middle wind speed is 0.8 m / s or more and satisfies 1 ≦ a ≦ 10 and 1 ≦ b ≦ 10. When the wind speed (upper, middle, and lower wind speeds) is input, the control unit 200 refers to the table stored in the ROM 202 or the nonvolatile memory 204 and corresponds to the input upper, middle, and lower wind speeds. The clean air supply amount and the exhaust amount may be extracted, and the clean air generator 116 and the exhaust mechanism 104 may be controlled so that the extracted clean air supply amount and exhaust amount are realized in the soot formation step.

(Example)
Examples of the present invention will be described below.
In Examples 1-1 to 2-4 and Comparative Examples 1 to 3, the production conditions were as follows.
Target: A cylinder having a core portion and a small number of cladding portions and a diameter of about 50 mm and a total length of about 2500 mm. As a constituent material, the core part is mainly SiO ₂ and the cladding part is doped with Ge in the core part.
Combustion gas: oxygen, hydrogen
Glass raw material: SiCl ₄
Clean air: air from which dust has been removed through a filter. Examples 1-1 and 1-2 are examples in which the flow guide 113 is not installed in the manufacturing apparatus 100 of FIGS. -1 to 2-4 are embodiments when the flow guide 113 is installed in the manufacturing apparatus 100 of FIGS. Moreover, the flow guide 113 is not installed also in Comparative Examples 1-3.

  In each of Examples 1-1 to 2-4, the soot formation process was performed with the wind speeds of the upper, middle, and lower stages of clean air, and the values a and b shown in Table 1 below. Similarly, in each of Comparative Examples 1 to 3, the soot formation step was performed with the wind speeds of the upper, middle, and lower stages of clean air, and a and b at the values shown in Table 2 below.

As can be seen from Tables 1 and 2, in Examples 1-1 to 2-4, as compared with Comparative Examples 1 to 3, the generation rate of soot (the ratio of soot in which 50 out of soot were produced) ) Can be reduced. In particular, in Examples 2-1 to 2-4 in which the flow guide 113 was provided, the occurrence rate of fluff when 50 soots were produced could be reduced to zero. In addition, in Examples 1-1 and 1-2 in which the flow guide 113 is not provided, the occurrence rate of shading can be reduced.
In the present specification, “butsu” is an abnormal appearance portion formed by surplus glass fine particles and peeling debris adhering to a target and growing from that point.

  On the other hand, in Comparative Examples 1 to 3 in which the wind speed of the middle stage of clean air is less than 0.8 m / s and a <1, b <1, the occurrence rate of sag was a high value of 8% or more. .

(Second Embodiment)
In the first embodiment, the manufacturing apparatus (vertical manufacturing apparatus) in which the target 107 is arranged so that the longitudinal direction of the target 107 is parallel to the gravity direction of the reaction vessel 101 has been described. The present invention can also be applied to a manufacturing apparatus (horizontal manufacturing apparatus) in which the target 107 is arranged so as to be perpendicular to the gravity direction of the reaction vessel 101.

FIG. 5 is a top view of the vertical optical fiber preform manufacturing apparatus according to the present embodiment, and FIG. 6 is a cross-sectional view taken along line AA ′ of FIG.
In this embodiment, since the manufacturing apparatus 100 is a horizontal type, the spindle mechanism 106 is provided on the side wall 101e of the reaction vessel 101 and the side wall 101f facing the side wall 101e. Therefore, in this embodiment, the soot 110 is formed on the target 107 while moving the target 107 in a direction (horizontal direction) perpendicular to the gravity direction of the reaction vessel 101.

  Also in the present embodiment, the wind speed of the clean air at the middle stage (for example, position β) is 0.8 m / s or higher, and the upper stage (for example, position α) so as to satisfy 1 ≦ a ≦ 10 and 1 ≦ b ≦ 10. And the wind speed of the clean air in the lower stage (for example, position γ) is set. Accordingly, excess glass fine particles that have not adhered to the target 107 out of the glass fine particles blown to the target 107 by the flame 111 are blown off to the exhaust port 104a side with clean air having a wind speed of 0.8 m / s or more. At this time, since it is difficult to completely send the surplus glass particles floating in the middle stage due to the flow of clean air to the exhaust port 104a, the surplus glass particles diffuse to the ceiling 101c and the bottom 101d side. However, due to the wind speed distribution in the direction of gravity, which is characteristic of the present invention, clean air flows are also formed in the upper and lower stages, and also in the vicinity of the ceiling 101c and the bottom 101d. Therefore, the glass particulates diffused toward the ceiling 101c and the bottom 101d are guided to the exhaust port 104a in the flow of clean air on the ceiling and bottom sides, and the adhesion of the glass particulates to the ceiling 101c and the bottom 101d is reduced. can do. Furthermore, even if the above-mentioned peeling debris is generated from the ceiling 101c and the bottom 101d, a flow of clean air is appropriately formed near the ceiling 101c and the bottom 101d. Therefore, it is possible to reduce peeling debris adhering to the target 107.

(Third embodiment)
In the first and second embodiments, the form in which the soot is formed by fixing the burner 103 and moving the target 107 in the vertical and horizontal manufacturing apparatuses has been described. However, the present invention is not limited to this form. For example, the soot may be formed while fixing the target 107 and moving the burner 103 along the longitudinal direction of the target 107. Furthermore, the form which moves both the target 107 and the burner 103 may be sufficient. That is, in one embodiment of the present invention, at the time of soot formation, the target 107 and the burner 103 are relatively moved so that the flame 111 from the burner 103 acts on the entire area of the soot formation region of the target 107.
However, in the present invention, it is not essential to move the target 107 and the burner 103 relatively, and the soot 110 is formed in the soot formation region of the target 107 by the action of the flame 111 containing the glass fine particles emitted from the burner 103. It is important to. Therefore, as long as the soot 110 can be appropriately formed on the target 107, any form such as a form in which a plurality of burners 103 are provided along the longitudinal direction of the target 107 without relatively moving the target 107 and the burner 103 can be adopted. good.

DESCRIPTION OF SYMBOLS 100 Manufacturing apparatus 101 Reaction container 101c Ceiling 101d Bottom 102 Clean air supply chamber 103 Burner 104 Exhaust mechanism 104a Exhaust port 105 Supply port 106 Spindle mechanism 107 Target 110 Soot 113 Flow guide

Claims (3)

A method for producing an optical fiber preform in which glass particulates are supplied to a starting preform disposed in a reaction vessel, and the glass particulates are deposited on the starting preform,
Disposing the starting base material between an exhaust port provided in a side wall other than the ceiling and the bottom of the reaction vessel and the glass fine particle supply unit;
Introducing a predetermined gas that does not react with the glass fine particles into the reaction vessel and forming a flow of the predetermined gas toward the exhaust port, supplying the glass fine particles to the starting base material to the starting base material Depositing the glass particles,
In the depositing step,
A position of 10% of the distance between the ceiling and the bottom of the reaction vessel in the direction from the ceiling of the reaction vessel to the bottom of the reaction vessel is defined as an upper position, and If the position of 10% of the distance from the bottom in the direction toward the ceiling is the lower position, and the middle position between the ceiling and the bottom in the direction of gravity is the middle position,
The wind speed of the predetermined gas at the middle position is 0.8 m / s or more, and 1 ≦ (wind speed of the predetermined gas at the middle position / wind speed of the predetermined gas at the lower position and The larger of the wind speeds at the upper position) ≦ 10 and 1 ≦ (wind speed at the middle position of the predetermined gas / wind speed at the lower position of the predetermined gas and the upper speed) The wind speed of the predetermined gas at the upper position, the middle position, and the lower position is set so as to satisfy the smaller one of the wind speeds at the position) ≦ 10. An optical fiber preform manufacturing method. The reaction vessel is provided with an inlet for introducing the predetermined gas,
The method of manufacturing an optical fiber preform according to claim 1, wherein the starting preform is provided between the introduction port and the exhaust port. In the reaction vessel, a member for adjusting the wind speed of the predetermined gas is provided,
3. The wind speed of the predetermined gas at the upper position, the middle position, and the lower position of the predetermined gas is adjusted by at least one of the shape and arrangement position of the member. The manufacturing method of the optical fiber preform of description.

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