OPTICAL FIBER PREFORM

Abstract

The present invention provides an optical fiber with improved optical properties such as zero dispersion wavelength by suppressing the volatilization of dopant materials such as germanium dioxide and optimizing the refractive index distribution by adjusting the setting position of the core portion burner for deposition in a larger optical fiber preform. An optical fiber preform includes a core portion with a relatively high refractive index and a clad portion with a relatively low refractive index, wherein a position having a value of 45% of a refractive index difference between a center of the core portion and the clad portion is a boundary rcore (mm) between the core portion and the clad portion; and when a radius position r at which a refractive index difference with the clad portion being a maximum value is rside (mm), r.sub.side/rcore is 0.745 to 1.

Claims

1. An optical fiber preform, comprising a core portion with a relatively high refractive index and a clad portion with a relatively low refractive index, wherein a position having a value of 45% of a refractive index difference between a center of the core portion and the clad portion is a boundary reore (mm) between the core portion and the clad portion; and when a radius position r at which a refractive index difference with the clad portion being a maximum value is rside (mm), r.sub.side/r.sub.core is 0.745 to 1.

2. The optical fiber preform according to claim 1, wherein an outer diameter is 103 mm or more.

3. The optical fiber preform according to claim 1, wherein a difference between a refractive index difference between the center and the clad portion, and a refractive index difference between rside and the clad portion is 4.6% or less of a refractive index difference between the center and the clad portion.

4. The optical fiber preform according to claim 1, wherein a refractive index of the clad portion is a refractive index at a position of 47.5% of an outer diameter of the optical fiber preform.

5. An optical fiber made by wire drawing from the optical fiber preform according to claim 1.

6. The optical fiber according to claim 5, wherein a zero dispersion wavelength is 1318.9 nm or less.

7. A producing method of an optical fiber preform, comprising: forming a core portion by depositing a material containing silicon tetrachloride and dopant materials on a starting material with a core portion burner for deposition; and forming a clad portion by depositing a material containing silicon tetrachloride to cover the core portion with a clad portion burner for deposition arranged above the core portion burner for deposition; wherein a flow rate ratio of carrier gas and silicon tetrachloride flowing to the core portion burner for deposition is adjusted to 0.39 to 0.73, and a flow rate ratio of sealing gas and silicon tetrachloride is adjusted to 1.5 to 2.5.

8. The producing method of an optical fiber preform according to claim 7, wherein the optical fiber preform is formed to have an outer diameter of 107 mm or more.

9. A producing method of an optical fiber for forming an optical fiber by wire drawing from an optical fiber preform produced by the producing method of an optical fiber preform according to claim 7.

10. The producing method of an optical fiber according to claim 9, wherein the optical fiber is formed so that a zero dispersion wavelength is 1318.9 nm or less.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0013] FIG. 1 illustrates a schematic view schematically showing the production of glass fine particulate deposits using a total of three burners.

[0014] FIG. 2 illustrates a schematic view showing a cross-sectional structure of the first clad portion depositing burner and the second clad portion depositing burner.

[0015] FIG. 3 illustrates a reference of a refractive index difference of the refractive index distribution of the optical fiber preform describing using an exemplary embodiment 1.

DESCRIPTION OF EXEMPLARY EMBODIMENTS

[0016] In the present invention, as a result of intensive research, by adjusting the flow rate ratio of carrier gas and silicon tetrachloride to 0.79 or less, preferably 0.39 to 0.73, and adjusting the flow rate of sealing gas and silicon tetrachloride to 2.7 or less, preferably 1.5 to 2.5, a position where the refractive index difference between the center of the core portion and the clad portion has a value of 45%, is set as the boundary reore (mm) between the core portion and the clad portion, and when the radius position r, with the refractive index difference being the maximum value in the region of the core portion where the radius position r is between 0.5 reore to 1.0 reore, is rside (mm), when r.sub.side/r.sub.core is 0.745 or more, it could be found that the optical properties of the optical fiber obtained by wire drawing the preform become desirable. Note that if the value of r.sub.side/r.sub.core is 0.745 or less, the zero dispersion wavelength is 1318.9 nm or more, which is not desirable. Note that rside and reore are defined as follows. The refractive index of the clad portion at a position of 47.5% of the outer diameter of the optical fiber preform is used as the reference for the refractive index difference (0.0), and the refractive index difference from the clad portion at the center of the core portion is further set at a refractive index ratio of 1.0. The radius position at which the refractive index ratio becomes 0.45 is considered to be the boundary between the core portion and the clad portion, and this position is defined as the core radius reore (mm) The radius position r of the core portion where the radius position r is the maximum value in the range of 0.5 reore to 1.0 reore was defined as rside (mm) (refer to FIG. 3).

[0017] The following is a description of the present invention through exemplary embodiments and comparative examples based on the drawings, but the present invention is not limited to these, and various forms are possible. FIG. 1 shows a schematic view of the glass fine particle deposit being produced. The core portion burner for deposition 13, depicted at the bottom, is provided independently of the clad portion burners for deposition 14 and 15 in order to accompany dopant materials such as germanium tetrachloride in addition to silicon tetrachloride, and a plurality of burners are often arranged as a whole to produce soot. After the core portion is deposited on the starting material located at the center, the clad portion is formed by the clad portion burner for deposition arranged above it to cover the core portion from the outside.

[0018] [Exemplary embodiment] [Exemplary embodiment 1] In exemplary embodiment 1, a total of three burners, a core portion burner for deposition 13 and a burner 20, whose cross-sectional shape is shown in FIG. 2, which is used as the first clad portion depositing burner 14 and the second clad portion depositing burner 15, were used to produce core soot bodies under the following conditions. A concentric quadruple burner was used in the core portion burner for deposition, with 0.32 L/min of silicon tetrachloride, 15 mL/min of germanium tetrachloride, and 0.19 L/min of argon as the carrier gas flowing through the central pipe. 6.2 L/min of hydrogen flowed through the second pipe from the center, 0.75 L/min of argon as sealing gas flowed through the third pipe, and 10.2 L/min of oxygen flowed through the outermost pipe. Herein, the flow rate ratio of argon to silicon tetrachloride as carrier gas is 0.59, and the flow rate ratio of argon to silicon tetrachloride as sealing gas is 2.3. The horizontal distance from the soot of the core portion burner for deposition is increased by 1.0 mm compared to a comparative example 1 described below.

[0019] Silicon tetrachloride 0.80 L/min and oxygen 0.66 L/min were flowed into the nozzle 21a of the first clad portion depositing burner. In addition, 32 L/min of hydrogen flowed to nozzle 21d, 18 L/min of oxygen flowed to nozzle 21f, and a total of 1.5 L/min of oxygen flowed to the small diameter nozzle group 21c. On the other hand, the nozzles 21a of the second clad portion depositing burner were set to 4.8 L/min of silicon tetrachloride and 3.6 L/min of oxygen, while 65 L/min of hydrogen flowed to nozzle 21d, 31 L/min of oxygen flowed to nozzle 21f, and a total of 6.2 L/min of oxygen flowed to the small diameter nozzle group 21c.

[0020] The outer diameter of the core soot body produced was 230 mm. This was heated to around 1200° C. in a reactor core pipe containing chlorine gas to dehydrate it, and then heated to around 1550° C. in a reactor core pipe containing helium gas to turn it into transparent glass. The outer diameter of the obtained core glass rod was 108 mm.

[0021] The refractive index distribution of the optical fiber preform produced using the obtained core glass rods was measured using a preform analyzer, and as the result, the obtained r.sub.side/r.sub.core value was 0.745. Note that the value of r.sub.side/r.sub.core was calculated according to the following. First, as shown in FIG. 3, the refractive index of the clad portion at a position of 47.5% of the outer diameter of the optical fiber preform is set as the reference for the refractive index difference (0.0), and further, the refractive index difference from the clad portion at the center of the core portion is set at a refractive index ratio of 1.0. The radius position at which the refractive index ratio becomes 0.45 is considered to be the boundary between the core portion and the clad portion, and this position is defined as the core radius reore (mm). The radius position r of the core portion where the radius position r is the maximum value in the range of 0.5 reore to 1.0 reore was defined as rside (mm), and the ratio r.sub.side/r.sub.core was obtained. The mode field diameter and zero dispersion wavelength of the optical fiber obtained by wire drawing the preform were 9.13 μm and 1318.1 nm, respectively.

[0022] [Exemplary embodiment 2] The core soot body was produced under the following conditions using a total of three burners as in the exemplary embodiment 1. That is, a concentric quadruple burner was used in the core portion burner for deposition, with 0.40 L/min of silicon tetrachloride, 17.5 mL/min of germanium tetrachloride, and 0.29 L/min of argon as the carrier gas flowing through the central pipe. 7.0 L/min of hydrogen flowed through the second pipe from the center, 1.0 L/min of argon as sealing gas flowed through the third pipe, and 10.2 L/min of oxygen flowed through the outermost pipe. Herein, the flow rate ratio of argon to silicon tetrachloride as carrier gas is 0.73, and the flow rate ratio of argon to silicon tetrachloride as sealing gas is 2.5. The horizontal distance from the soot of the core portion burner for deposition is increased by 1.0 mm compared to a comparative example 1 described below. Silicon tetrachloride 0.77 L/min and oxygen 0.65 L/min were flowed into the nozzle 21a of the first clad portion depositing burner. In addition, 33 L/min of hydrogen flowed to nozzle 21d, 19 L/min of oxygen flowed to nozzle 21f, and a total of 1.5 L/min of oxygen flowed to the small diameter nozzle group 21c. On the other hand, the nozzles 21a of the second clad portion depositing burner were set to 5.0 L/min of silicon tetrachloride and 3.7 L/min of oxygen, while 69 L/min of hydrogen flowed to nozzle 21d, 30 L/min of oxygen flowed to nozzle 21f, and a total of 6.5 L/min of oxygen flowed to the small diameter nozzle group 21c.

[0023] The outer diameter of the core soot body produced was 235 mm. This was heated to around 1200° C. in a reactor core pipe containing chlorine gas to dehydrate it, and then heated to around 1550° C. in a reactor core pipe containing helium gas to turn it into transparent glass. The outer diameter of the obtained core glass rod was 110 mm.

[0024] The refractive index distribution of the optical fiber preform produced by the above described conditons was measured using a preform analyzer, and as the result, the obtained r.sub.side/r.sub.core value was 0.831. The mode field diameter and zero dispersion wavelength of the optical fiber produced by wire drawing the preform were 9.15 μm and 1317.8 nm, respectively.

[0025] Exemplary embodiment 31 The core soot body was produced under the following conditions using a total of three burners as in the exemplary embodiment 1. That is, a concentric quadruple burner was used in the core portion burner for deposition, with 0.49 L/min of silicon tetrachloride, 18.0 mL/min of germanium tetrachloride, and 0.19 L/min of argon as the carrier gas flowing through the central pipe. 6.7 L/min of hydrogen flowed through the second pipe from the center, 0.73 L/min of argon as sealing gas flowed through the third pipe, and 10.2 L/min of oxygen flowed through the outermost pipe. Herein, the flow rate ratio of argon to silicon tetrachloride as carrier gas is 0.39, and the flow rate ratio of argon to silicon tetrachloride as sealing gas is 1.5. The distance from the soot of the core portion burner for deposition is the same as in the comparative example 1, as described below. Silicon tetrachloride 0.77 L/min and oxygen 0.65 L/min were flowed into the nozzle 21a of the first clad portion depositing burner. In addition, 31 L/min of hydrogen flowed to nozzle 21d, 17.5 L/min of oxygen flowed to nozzle 21f, and a total of 1.4 L/min of oxygen flowed to the small diameter nozzle group 21c. On the other hand, the nozzles 21a of the second clad portion depositing burner were set to 5.3 L/min of silicon tetrachloride and 3.6 L/min of oxygen, while 72 L/min of hydrogen flowed to nozzle 21d, 28 L/min of oxygen flowed to nozzle 21f, and a total of 6.9 L/min of oxygen flowed to the small diameter nozzle group 21c.

[0026] The outer diameter of the core soot body produced was 225 mm. This was heated to around 1200° C. in a reactor core pipe containing chlorine gas to dehydrate it, and then heated to around 1550° C. in a reactor core pipe containing helium gas to turn it into transparent glass. The outer diameter of the obtained core glass rod was 104 mm.

[0027] The refractive index distribution of the optical fiber preform produced by the above described conditons was measured using a preform analyzer, and as the result the obtained r.sub.side/r.sub.core value was 0.767. The mode field diameter and zero dispersion wavelength of the optical fiber produced by wire drawing the preform were 9.17 pm and 1318.3 nm, respectively.

[0028] [Exemplary embodiment 4] The core soot body was produced under the following conditions using a total of three burners as in the exemplary embodiment 1. The silicon tetrachloride flow rate of the core portion burner for deposition was set to 0.44 L/min, germanium tetrachloride was set to 20.0 mL/min, argon flow rate as the carrier gas was set to 0.19 L/min, and argon as the sealing gas was set to 0.70 L/min. Herein, the flow rate ratio of argon to silicon tetrachloride as carrier gas is 0.43, and the flow rate ratio of argon to silicon tetrachloride as sealing gas is 1.6. The horizontal distance from the soot of the core portion burner for deposition is increased by 2.0 mm compared to a comparative example 1 described below. The other conditions are the same as in the exemplary embodiment 1.

[0029] The refractive index distribution of the optical fiber preform produced by the above described conditons was measured using a preform analyzer, and as the result. the obtained r.sub.side/r.sub.core value was 0.809. The mode field diameter and zero dispersion wavelength of the optical fiber produced by wire drawing the preform were 9.09 μm and 1317.5 nm, respectively.

[0030] Comparative example As a comparative example 1, core soot bodies were produced under the following conditions using a total of three burners, a core portion burner for deposition 13 and a burner 20 which is used as the first clad portion depositing burner 14 and the second clad portion depositing burner 15. That is, a concentric quadruple burner was used in the core portion burner for deposition, with 0.48 L/min of silicon tetrachloride, 19 mL/min of germanium tetrachloride, and 0.38 L/min of argon as the carrier gas flowing through the central pipe. 6.8 L/min of hydrogen flowed through the second pipe from the center, 1.3 L/min of argon as sealing gas flowed through the third pipe, and 10.1 L/min of oxygen flowed through the outermost pipe. Herein, the flow rate ratio of argon to silicon tetrachloride as carrier gas is 0.79, and the flow rate ratio of argon to silicon tetrachloride as sealing gas is 2.7. Silicon tetrachloride 0.80 L/min and oxygen 0.66 L/min were flowed into the nozzle 21a of the first clad portion depositing burner. In addition, 30 L/min of hydrogen flowed to nozzle 21d, 18 L/min of oxygen flowed to nozzle 21f, and a total of 1.5 L/min of oxygen flowed to the small diameter nozzle group 21c. On the other hand, the nozzles 21a of the second clad portion depositing burner were set to 4.8 L/min of silicon tetrachloride and 3.6 L/min of oxygen, while 65 L/min of hydrogen flowed to nozzle 21d, 31 L/min of oxygen flowed to nozzle 21f, and a total of 6.2 L/min of oxygen flowed to the small diameter nozzle group 21c.

[0031] The outer diameter of the core soot body produced was 229 mm. This was heated to around 1200° C. in a reactor core pipe containing chlorine gas to dehydrate it, and then heated to around 1550° C. in a reactor core pipe containing helium gas to turn it into transparent glass. The outer diameter of the obtained core glass rod was 107 mm.

[0032] The refractive index distribution of the optical fiber preform produced by the above described conditons was measured using a preform analyzer, and as the result, the obtained r.sub.side/r.sub.core value was 0.660. The mode field diameter and zero dispersion wavelength of the optical fiber produced by wire drawing the preform were 9.12 μm and 1319.1 nm, respectively.

[0033] [Comparative example 2] As a comparative example 2, a total of three burners, a core portion burner for deposition 13 and a burner 20, whose cross-sectional shape is shown in FIG. 2, which is used respectively as the first clad portion depositing burner 14 and the second clad portion depositing burner 15, were used to produce core soot bodies under the following conditions. That is, a concentric quadruple burner was used in the core portion burner for deposition, with 0.22 L/min of silicon tetrachloride, 13 mL/min of germanium tetrachloride, and 0.18 L/min of argon as the carrier gas flowing through the central pipe. 4.5 L/min of hydrogen flowed through the second pipe from the center, 1.3 L/min of argon as sealing gas flowed through the third pipe, and 9.5 L/min of oxygen flowed through the outermost pipe. Herein, the flow rate ratio of argon to silicon tetrachloride as carrier gas is 0.82, and the flow rate ratio of argon to silicon tetrachloride as sealing gas is 5.9. The horizontal distance from the soot of the core portion burner for deposition is decreased by 0.5 mm compared to a comparative example 1 described above. Silicon tetrachloride 0.80 L/min and oxygen 0.66 L/min were flowed into the nozzle 21a of the first clad portion depositing burner. In addition, 30 L/min of hydrogen flowed to nozzle 21d, 18 L/min of oxygen flowed to nozzle 21f, and a total of 1.5 L/min of oxygen flowed to the small diameter nozzle group 21c. On the other hand, the nozzles 21a of the second clad portion depositing burner were set to 4.8 L/min of silicon tetrachloride and 3.6 L/min of oxygen, while 65 L/min of hydrogen flowed to nozzle 21d, 31 L/min of oxygen flowed to nozzle 21f, and a total of 6.2 L/min of oxygen flowed to the small diameter nozzle group 21c.

[0034] The outer diameter of the core soot body produced was 230 mm. This was heated to around 1200° C. in a reactor core pipe containing chlorine gas to dehydrate it, and then heated to around 1550° C. in a reactor core pipe containing helium gas to turn it into transparent glass. The outer diameter of the obtained core glass rod was 110 mm.

[0035] The refractive index distribution of the optical fiber preform produced by the above described conditons was measured using a preform analyzer, and as the result the obtained r.sub.side/r.sub.core value was 0.703. The mode field diameter and zero dispersion wavelength of the optical fiber produced by wire drawing the preform were 9.11 μm and 1318.9 nm, respectively.

[0036] The results of the above exemplary embodiments 1 to 4 and comparative examples 1 and 2 are shown in Table 1. According to Table 1, the r.sub.side/r.sub.core values of the optical fiber preforms of exemplary embodiments 1 to 4, where the flow rate ratio of argon and silicon tetrachloride as carrier gas flowed into the core portion burner for deposition was 0.79 or less and the flow rate ratio of argon and silicon tetrachloride as sealing gas was 2.7 or less, were 0.745 or more. The zero dispersion wavelength of the optical fiber obtained from the optical fiber preform of exemplary embodiments 1 to 4 was 1318.9 nm or less, which was excellent in terms of optical properties. On the other hand, the r.sub.side/r.sub.core values of the optical fiber preforms of comparative examples 1 to 4, where the flow rate ratio of argon and silicon tetrachloride as carrier gas flowed into the core portion burner for deposition was 0.79 or more and the flow rate ratio of argon and silicon tetrachloride as sealing gas was 2.7 or more, were 0.745 or less. The zero dispersion wavelength of the optical fiber obtained from the optical fiber preform of comparative examples 1 and 2 is 1318.9 nm or more, indicating that the optical properties are inferior to those of exemplary embodiments 1 to 4.

TABLE-US-00001 TABLE 1 Flow rate Flow rate ratio of ratio of Mode field carrier gas sealing gas diameter Zero-dispersion Ar to Si Ar to Si r.sub.side/r.sub.core (μm) wavelength (nm) Example 0.59 2.3 0.745 9.13 1318.1 Embodiment 1 Example 0.73 2.5 0.831 9.15 1317.8 Embodiment 2 Example 0.39 1.5 0.767 9.17 1318.3 Embodiment 3 Example 0.43 1.6 0.809 9.09 1317.5 Embodiment 4 Comparative 0.79 2.7 0.660 9.12 1319.1 Example 1 Comparative 0.82 5.9 0.703 9.11 1318.9 Example 2