Title of Invention

OPTICAL FIBER PERFORM MANUFACTURING APPARATUS AND METHOD FOR SHRINKAGE AND CLOSING OF DEPOSITED TUBE

Abstract An optical fiber perform manufacturing apparatus for shrinking and closing a deposited tube comprising; a lathe for supporting a deposited tube In such a fashion that It extends vertically, the deposited tube having a clad layer and a core layer while being sealed at one end thereof; a circular heater arranged around the deposited tube white being clrcumferentlally spaced apart from the deposited tube by a desired distance, the circular heater serving to supply heat to the deposited tube supported by the lathe and being movable upwardly and downwardly at a desired speed; a vacuum pump connected to the other end of the deposited tube and adapted to pump air existing in the interior of the deposited tube using a vacuum; and a process control unit for setting a heating temperature of the circular heater to a desired temperature, and conducting a control operation for processes of shrinking and closing the deposited tube while upwardly and downwardly moving the circular heater.
Full Text This invention relates to an Optical fiber perform manufacturing apparatus and method for shrinkage and closing of deposited tube.
The present invention relates to an apparatus for and a method of manufacturing an optical fiber preform, and more particularly to an optical fiber preform manufacturing apparatus and method for more effectively shrinking and closing a deposited tube.
2. Description of the Related Art
Manufacture of optidal fiber preforms using a modified chemical vapor deposition (MCVD) method is well known. In a deposition process in which a deposited layer is formed in the form of a tube on the inner surface of a preform tube in accordance with the MCVD method, the deposited tube is shrunk by itself as the thickness of thenlepbsited layer increases gradually. To this end, a burner configured to have a large heating area while using a low flame pressure is typically used in the deposition process. The large heating area of the burner makes it possible to allow an easy heat transfer to the inner portion of a preform tube, thereby achieving an improved deposition efficiency. On the other hand, the low flame pressure of the burner results in a reduced undesirable shrinkage of the deposited tube occurring during the deposition process. However, it is necessary to use a high flame pressure in a tube shrinking and closing process to be conducted for the deposited tube, as different from the deposition process. Where a burner suitable for the deposition process is used, as it is, for the shrinking and closing process, in spite of the above mentioned fact, it is necessary to move the burner at a low speed while keeping a high heating temperature in order to allow the deposited tube to be softened at the low flame pressure used. As a result, the processing time of the tube shrinking and closing process occupies a large portion of the entire processing time of the optical fiber preform manufacture process. For this- reason, the conventional tube
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shrinking and closing process serves as a great obstacle to a reduction in processing time.
The high heating temperature and low moving speed of the burner in the tube shrinking and closing process result in a degradation in the optical characteristics of optical fibers finally produced, as follows.
That is, a trace of moisture (generally, several ppm) contained in the preform tube penetrates into the layer deposited on the inner surface thereof. The penetrated moisture is coupled to P2O5 or SiO2 of the deposited layer, thereby forming P-O-H or Si-O-H bonds. OH reaching the core region of the deposited layer is coupled to SiO2 or GeO2 of the deposited layer, thereby forming Si-O-H or Ge-O-H bonds while releasing Si-0 or Ge-0 bonds. These O-H or P-O-H bonds resulting from the coupling of the moisture to the compounds of the deposited layer at respective regions of the deposited layer serve to generate an optical loss in the optical fiber, finally produced, due to an absorption band established in a particular wavelength range. OH penetrated into the core layer forms mono-oxygen, thereby resulting in a degradation in the structural uniformity of the vitreous components in the core layer. This causes a non-uniformity in density of the core layer. As a result, an increase in scattering loss occurs.
Second, where the preform tube is heated in a rotating state at its lower end by the burner, a circumferential temperature gradient occurs. The temperature gradient results in a non-uniformity in viscosity of the preform tube. As a result, the balance of surface tension in the deposited tube is lost, thereby causing the deposited tube to be deformed in shape. This causes an increase in the non-circularity of the deposited tube. As the shrinking process advances, the non-circularity of the deposited tube increases, thereby resulting in an increase in polarization mode dispersion.
Conventionally, the deposition process, shrinking process, and closing process have been conducted using the same burner, which is suitable only for the deposition process, in spite of the fact that those processes involve different mechanisms, respectively. For this reason, an increase in the thickness of the deposited layer occurs. This causes various problems such as a deformed geometrical structure of the deposited tube, a
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degradation in the optical characteristics of optical fibers finally produced, and an increased processing time.
SUMMARY OF THE INVENTION
The present invention has been made to overcome the above-described problems. Therefore, it is an object of the present invention to provide an optical fiber preform manufacturing apparatus and method in which processes for shrinking and closing a deposited tube are conducted using a device suitable for those processes, which device is other than the device used in a deposition process for forming the deposited tube on the inner surface of a preform tube, thereby reducing the processing time while reducing the amount of OH penetrated from the preform tube into a vitreous component of the deposited tube, thereby achieving a reduction in OH loss.
In accordance with one aspect, the present invention provides an optical fiber preform manufacturing apparatus for shrinking and closing a deposited tube comprising: a lathe for supporting a deposited tube in such a fashion that it extends vertically, the deposited tube having a clad layer and a core layer while being sealed at one end thereof; a circular heater arranged around the deposited tube while being circumferentially spaced apart from the deposited tube by a desired distance, the circular heater serving to supply heat to the deposited tube supported by the lathe and being movable upwardly and downwardly at a desired speed; a vacuum pump connected to the other end of the deposited tube and adapted to pump air existing in the interior of the deposited tube using a vacuum; and a process control unit for setting cheating temperature of the circular heater to a desired temperature, and conducting a control operation for processes of shrinking and closing the deposited tube while upwardly and downwardly moving the circular heater.
In accordance with another aspect, the present invention provides an optical fiber preform manufacturing method comprising the steps of: depositing a clad layer and a core layer on an inner surface of a preform tube, thereby forming a deposited tube; shrinking one end of the deposited tube, thereby sealing the one end of the deposited tube; arranging the deposited tube in such a fashion that it extends vertically through a circular heater;
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moving the circular heater to the sealed end of the deposited tube, and then adjusting a heating temperature of the circular heater to be not lower than a softening point of the deposited tube; and heating the deposited tube while moving the circular heater at a desired speed, thereby shrinking and closing the deposited tube.
BRIEF DESCRIPTION OF THE DRAWINGS
The above objects and advantages of the present invention will become more apparent by describing in detail preferred embodiments thereof with reference to the attached drawings in which:
Fig. 1 is a view illustrating a deposition apparatus suitable for an MCVD process;
Fig. 2 is a view illustrating an optical fiber preform manufacturing apparatus capable of conducting the shrinking and closing processes in accordance with the present invention;
Fig. 3 is a flow chart illustrating a method for manufacturing optical fiber preforms in accordance with the present invention; and
Figs. 4a and 4b are views respectively illustrating examples in which a burner or a furnace is used as a heating means.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
The present invention discloses an optical fiber preform manufacturing method and apparatus which involve a process for depositing a reaction product of raw material gas on the inner surface of a preform tube, thereby forming a deposited tube, and a process for shrinking and closing the deposited tube, thereby obtaining an optical fiber preform. The deposition process is carried out in accordance with a well-known deposition method, for example, an MCVD method. On the other hand, the shrinking and closing process is simply and rapidly carried out in accordance with the present invention.
Fig. 1 is a view illustrating a deposition apparatus suitable for an
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MCVD process. This deposition apparatus is used to deposit a reaction product of raw material gas in the inner surface of a preform tube. Referring to Fig. 1, a lathe 11 is illustrated which serves to support a preform tube 12. A heating means 14 heats partially the preform tube 12 when viewed in both the longitudinal and circumferential directions of the preform tube 12. In Fig. 1, the region where the preform tube is heated is denoted by the reference numeral 13. The preform tube 2 rotates in a direction, for example, the direction indicated by the arrow 15a in Fig. 1. The heating means 14 moves in directions indicated by the arrows 15b in Fig. 1 in accordance with the operation of a moving member (not shown). Accordingly, the heating region 13 is defined while not only moving along the entire length of the preform tube 12, but also rotating around the circumference of the preform tube 12. Raw material gas is introduced from a raw material gas supply unit 19 into the preform tube 12 via an input tube 17. The raw material gas supply unit 19 contains a reactant of a liquid phase therein and supplies this reactant to the preform tube 12 using carriage gas. Exhaust materials are discharged from the preform tube 12 through an outlet 18. The flow rate of the raw material gas is controlled by a mixing valve (not shown) and a shutoff valve (not shown).
In accordance with the MCVD method, highly pure raw material gas such as SiCl4, GeCl4, or POC13 is blown into a glass preform tube along with oxygen. When heat is applied to the glass preform tube using a heating means, a thermal oxidation is generated, so that an oxide is deposited in the form of soot on the inner surface of the preform tube. At this time, a clad layer and a core layer are deposited on the inner surface of the preform tube under the condition in which the refractive indexes of those layers are adjusted by precisely controlling the concentration of the raw material gas. Thus, a deposited tube is formed on the inner surface of the preform tube. After completion of the deposition process, the preform tube is heated again by the heating means, so that the deposited tube is shrunk. Thus, an optical fiber preform is obtained.
Fig. 2 is a view illustrating an optical fiber preform manufacturing apparatus capable of conducting the shrinking and closing processes in accordance with the present invention. This apparatus is adapted to shrink and close the deposited tube produced by the apparatus of Fig. 1.
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As shown in Fig. 2, the optical fiber preform manufacturing apparatus according to the present invention includes a lathe 21 for supporting a deposited tube, to be treated, by its upper and lower support members 22 and 23 in such a fashion that the deposited tube extends vertically. The optical fiber preform manufacturing apparatus also includes a circular heater 24 for heating the deposited tube, a vacuum pump 25 for pumping air or other contaminants existing in the deposited tube using a vacuum, a pressure meter 26 for measuring the pumping pressure of the vacuum pump 25, a chlorine gas injector 27 for supplying chlorine gas into the deposited tube, and valves, that is, a vacuum exhaust value 26 and a gas supply valve 28. For the circular heater 24, a burner or a furnace may be used. The circular heater 24 is configured to provide a sufficient amount of heat while being controlled in flame pressure, so that it is suitable for the shrinking and closing processes, as compared to the heating means of Fig. 1 suitable for the deposition process.
In the optical fiber preform manufacturing apparatus having the above mentioned configuration, a deposited tube 20b, which may be manufactured by the apparatus of Fig. 1, is supported by the lathe 21. The deposited tube 20b has a sealed end to which a rod 20a is connected. The upper support member 22 supports the rod 20a connected to the sealed end of the deposited tube 20b whereas the lower support member 23 supports the other end of the deposited tube 20b, which end is open. The lathe 21 also has a length adjusting member 20c adapted to adjust the tube support length of the lathe 21. The circular heater 24, which serves to supply heat to the deposited tube 20b, is arranged around the deposited tube 20b while being radially spaced apart from the deposited tube 20b by a desired distance. The circular heater 24 is movable vertically along the deposited tube 20b at a desired speed. The chlorine gas injector 27 supplies chlorine gas to the deposited tube 20b through the lower support member 23 of the lathe 21 in order to remove moisture existing in the deposited tube 20b.
The optical fiber preform manufacturing apparatus also includes a control unit not shown. The control unit performs control operations for the processes of shrinking and closing the deposited tube 20b. That is, the control unit sets the heating temperature of the circular heater 24 to a desired temperature, and rotates the deposited tube 20b supported between the upper
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and lower support members 22 and 23 at a desired speed while vertically moving the deposited tube 20b. The heating temperature of the circular heater 24 is first adjusted to be lower than the softening point of the deposited tube 20b. In this state, the circular heater 24 is moved at a desired speed. During the movement of the circular heater 24, contaminants existing in the deposition tube 22b are then exhausted in accordance with an operation of the vacuum pump 27. Thereafter, the heating temperature of the circular heater 24 is adjusted again so that it is not lower than the softening point of the deposited tube 20b. In this state, the processes of shrinking and closing the deposited tube 20b is carried out. Where a furnace is used for the circular heater 24, inert gas such as argon or nitrogen is supplied to the furnace in order to prevent an oxidation thereof at a heat generating region.
In accordance with the apparatus of the present invention, the deposited tube is vertically arranged during the tube shrinking and closing process. Heat is supplied to the vertically-arranged deposited tube by the circular heater arranged around the deposited tube while using a high flame pressure. During the heating, the deposited tube is evacuated using a vacuum. By virtue of such features, it is possible to considerably reduce the processing time while preventing the deposited tube from having a non-circularity, as compared to conventional methods.
Fig. 3 is a flow chart illustrating an optical fiber preform manufacturing apparatus according to the present inventiofi.
In accordance with this method, a clad layer and a core layer are first deposited on the inner surface of a preform tube horizontally arranged, using the apparatus shown in Fig. 1, thereby forming a deposited tube (Step 31). Thereafter, the deposited tube is locally heated at one end thereof corresponding to a region where chemical raw gas is exhausted during the deposition process, thereby causing the end to be sealed (Step 32). A rod is horizontally joined to the sealed end of the deposited tube (Step 33). The rod-joined deposited tube is separated from the lathe, and then fed to the tube shrinking/closing lathe shown in Fig. 3. In the tube shrinking/closing lathe, the deposited tube is then vertically arranged in such a fashion that it extends vertically through the circular heater while the rod is upwardly directed (Step 34). Subsequently, the circular heater is moved to the joint
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between the deposited tube and rod. The heating temperature of the circular heater is then adjusted so that it is lower than the softening point of the deposited tube. In this state, the circular heater is upwardly and downwardly moved at a low speed to heat the deposited tube. At the same time, the vacuum exhaust value is opened to remove contaminants, including moisture, from the interior of the deposited tube (Step 36).
The movements of the circular heater are carried out in such a fashion that when the deposited tube, which moves downwardly from the joint to the lower end thereof, reaches the lower end, the moving direction is changed to allow the deposited tube to move upwardly to the joint. After the evacuation of the deposited tube, the heating temperature of the circular heater is adjusted again so that it is not lower than the softening point of the deposited tube (Step 37). When the circular heater reaches a predetermined temperature during the operation thereof, it is maintained at that temperature for 2 or 3 minutes to obtain a temperature stability. Thereafter, the vacuum pump operates to maintain the interior of the deposited tube in a negative pressure state. In this state, the deposited tube is heated under the condition in which it moves downwardly at a desired speed, thereby causing it to be shrunk and closed (Step 38). The shrinking and closing processes of step 38 are conducted under the condition in which the deposited tube rotates at a desired speed of, typically, 10 rpm or less. The shrinkage of the deposited tube may be achieved by conducting the shrinking process one time or several times. After the shrinkage of the deposited tube, the deposited tube is closed to form a solid preform. Where a furnace is used for the circular heater, inert gas such as argon or nitrogen is supplied to the interior of the furnace in order to prevent an oxidation thereof at a heat generating region.
Figs. 4a and 4b are views respectively illustrating examples in which a burner or a furnace is used as the circular heater. In the case of Fig. 4a, a circular burner 41 applies'heat to a deposited tube having a deposited clad/core layer 43 deposited on the inner surface of a preform tube 42, around the deposited tube, while moving downwardly, thereby shrinking and closing the deposited tube. During this heating process, a vacuum is generated in the interior of the deposited tube in order to allow the deposited tube to be more easily shrunk and closed. In the case of Fig. 4b, a circular furnace 45 applies heat to a deposited tube having a deposited clad/core layer 47 deposited on the inner surface of a preform tube 46, around the deposited tube, while moving downwardly, thereby shrinking and closing
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As apparent from the above description, the present invention provides an optical fiber preform manufacturing apparatus and method in which processes for shrinking and closing a deposited tube are conducted using a device suitable for those processes, which device is other than the device used in a deposition process for forming the deposited tube on the inner surface of a preform tube, thereby reducing the processing time to a degree corresponding to half that of the conventional method or less. This is because the processing time of the tube shrinking and closing process occupies a large portion (2/3 or more) of the entire processing time of the optical fiber preform manufacture process. In accordance with the present invention, the shrinking and closing process are carried out under the condition in which a negative pressure is applied to the interior of the deposited tube. Accordingly, it is possible to further reduce the processing time while considerably reducing the period of time, for which the deposited tube is exposed at a high temperature. This results in a reduction in the amount of OH penetrated from the preform tube into a vitreous component of the deposited tube, thereby achieving a reduction in OH loss. Since a circular burner or circular furnace is used as the heating means for the shrinking and closing processes, there is no or little surface temperature gradient in association with heat applied to the deposited tube. Accordingly, it is possible to reduce a non-circularity of the deposited tube. This results in a reduction in polarization mode dispersion.
While the present invention has been particularly shown and described with reference to a particular embodiment thereof, it will be understood by those skilled in the art that various changes in form and detail may be effected therein without departing from the scope of the invention as defined by the appended claims.
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1. An optical fiber perform manufacturing apparatus for shrinking and closing a
deposited tube comprising;
a lathe for supporting a deposited tube in such a fashion that it extends vertically, the deposited tube having a clad layer and a core layer while being sealed at one end thereof;
a circular heater arranged around the deposited tube while being circumferentially spaced apart from the deposited tube by a desired distance, the circular heater serving to supply heat to the deposited tube supported by the lathe and being movable upwardly and downwardly at a desired speed; a vacuum pump connected to the other end of the deposited tube and adapted to pump air existing in the interior of the deposited tube using a vacuum; and
a process control unit for setting a heating temperature of the circular heater to a desired temperature, and conducting a control operation for processes of shrinking and closing the deposited tube while upwardly and downwardly moving the circular heater.
2. The optical fiber perform manufacturing apparatus as claimed in claim 1,
wherein the lathe comprises:
an upper support member for supporting the sealed end of the deposited tube; and
a lower support member for supporting the other end of the deposited tube, the lower support member cooperating with the upper support member to rotate the deposited tube at a desired speed during the tube shrinking and closing processes.
3. The optical fiber perform manufacturing apparatus as claimed in claim 1,
comprising:
a chlorine gas injector for supplying chlorine gas to the interior of the deposited tube to remove moisture generated in the interior of the deposited tube due to heat from the circular heater.
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4. The optical fiber perform manufacturing apparatus as claimed in claim 1,
wherein the circular heater comprises a furnace.
5. The optical fiber perform manufacturing apparatus as claimed in claim 1,
wherein the circular heater comprises a burner.
6. The optical fiber perform manufacturing apparatus as claimed in claim 4,
comprising an inert gas injector for supplying inert gas to the furnace to
prevent an oxidation of the furnace at a heat generating region.
7. The optical fiber perform manufacturing apparatus as claimed In claim 1,
wherein the process control unit conducts sequential control operations for
setting the heating temperature of the circular heater to a temperature lower
than a softening point of the deposited tube, exhausting contaminants
existing in the interior of the deposited tube while moving the circular heater
at a desired temperature, setting the heating temperature of the circular
heater to a temperature not lower than the softening point of the deposited
tube, and shrinking and closing the deposited tube while moving the circular
heater to a desired temperature.
8. The optical fiber perform manufacturing apparatus as claimed in claim 1,
wherein the process control unit conducts a control operation for rotating the
deposited tube supported by the lathe at a desired speed during the
shrinking and closing processes.
9. An optical fiber perform manufacturing method comprising the steps of:
depositing a clad layer and a core layer on an inner surface of a perform
tube by using a first heater, thereby forming a deposited tube;
shrinking one end of the deposited tube by using said first heater, thereby sealing the one end of the deposited tube;
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arranging the deposited tube in such a fashion that it extends vertically through a circular heater by making the sealed end the upper end; moving the circular heater to the sealed end of the deposited tube, and then adjusting a heating temperature of the circular heater to be not lower than a softening point of the deposited tube; and shrinking and closing the deposited tube by heating the deposited tube while moving the circular heater at a desired speed and rotating the deposited tube, wherein a flame pressure of said circular heater during the shrinking and closing step is higher than a flame pressure of said first heater during the deposition step.
10. The optical fiber perform manufacturing method as claimed in claim 9,
further comprising the steps of:
moving the circular heater to the sealed end of the deposited tube, and then adjusting the heating temperature of the circular heater to be lower than a softening point of the deposited tube; and heating the deposited tube while moving the circular heater at a desired speed, thereby exhausting contaminants existing in the interior of the deposited tube.
11. The optical fiber perform manufacturing method as claimed In claim 9,
wherein the shrinking and closing step is carried out under the condition in
which the deposited tube rotates at a desired speed, and the interior of the
deposited tube is maintained at a negative pressure.
12. The optical fiber perform manufacturing method as claimed in claim 9,
wherein the circular heater is a furnace, and inert gas is supplied to the
furnace to prevent an oxidation of the furnace at a heat generating region.
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13. The optical fiber perform manufacturing method as claimed in claim 9, wherein the shrinking and closing step is carried out under the condition in which chlorine gas is supplied to the interior of the deposited tube, thereby removing moisture generated in the interior of the deposited tube due to heat of the circular heater.
An optical fiber perform manufacturing apparatus for shrinking and closing a deposited tube comprising; a lathe for supporting a deposited tube In such a fashion that It extends vertically, the deposited tube having a clad layer and a core layer while being sealed at one end thereof; a circular heater arranged around the deposited tube white being clrcumferentlally spaced apart from the deposited tube by a desired distance, the circular heater serving to supply heat to the deposited tube supported by the lathe and being movable upwardly and downwardly at a desired speed; a vacuum pump connected to the other end of the deposited tube and adapted to pump air existing in the interior of the deposited tube using a vacuum; and a process control unit for setting a heating temperature of the circular heater to a desired temperature, and conducting a control operation for processes of shrinking and closing the deposited tube while upwardly and downwardly moving the circular heater.

Documents:

in-pct-2000-00205-kol abstract.pdf

in-pct-2000-00205-kol claims.pdf

in-pct-2000-00205-kol correspondence.pdf

in-pct-2000-00205-kol description(complete).pdf

in-pct-2000-00205-kol drawings.pdf

in-pct-2000-00205-kol form-1.pdf

in-pct-2000-00205-kol form-18.pdf

in-pct-2000-00205-kol form-2.pdf

in-pct-2000-00205-kol form-3.pdf

in-pct-2000-00205-kol form-5.pdf

in-pct-2000-00205-kol g.p.a.pdf

in-pct-2000-00205-kol letters patent.pdf

in-pct-2000-00205-kol priority document others.pdf

in-pct-2000-00205-kol priority document.pdf

in-pct-2000-205-kol-granted-abstract.pdf

in-pct-2000-205-kol-granted-claims.pdf

in-pct-2000-205-kol-granted-description (complete).pdf

in-pct-2000-205-kol-granted-drawings.pdf

in-pct-2000-205-kol-granted-form 2.pdf

in-pct-2000-205-kol-granted-specification.pdf

in-pct-2000-205-kol-priority document.pdf

in-pct-2000-205-kol-translated copy of priority document.pdf


Patent Number 212982
Indian Patent Application Number IN/PCT/2000/205/KOL
PG Journal Number 51/2007
Publication Date 21-Dec-2007
Grant Date 19-Dec-2007
Date of Filing 10-Aug-2000
Name of Patentee SAMSUNG ELECTRONICS CO. LTD.
Applicant Address 416, MAETAN-DONG, PALDAL-GU, SUWON-SHI, KYUNGKI-DO, 442-370 KOREA.
Inventors:
# Inventor's Name Inventor's Address
1 OH SUNG KOOG 109-1, KONGDAN 1-DONG, KUMI-SHI, KYONGSANGBUK-DO 730-031
2 SEO, MAN-SEOK SHIYOUNG APT. NO. 202-512 SSANGCHON-DONG, S0-GU, KWANGJU-KWANGYOKSHI 502-206
3 YANG, JIN-SEONG 109-1, KONGDAN 1-DONG, KUMI-SHI, KYONGSANGBUK-DO 730-031,
4 DO, MUN-HYUN 37 SONGJONG-DONG, KU,I-SHI, KYONGSANGBUK-DO, 730-090
PCT International Classification Number C03B 37/07
PCT International Application Number PCT/KR99/00692
PCT International Filing date 1999-11-17
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 1998/54193 1998-12-10 Republic of Korea