Method of producing an optical fibre

Abstract: An optical fiber is coated with at least one carbon layer formed by thermally decomposing at least one hydrocarbon or halogenated hydrocarbon having 15 or less carbon atoms optionally at a temperature of 400-1100°C. There is also disclosed an apparatus for producing such optical fiber.

Description: The present invention relates to a method of forming a carbon layer on an optical fibre. Quartz-based optical fibres have been widely used for communication cables. Hydrogen coming into contact with these fibres can diffuse through them, and the molecular vibrations of the hydrogen lead to greater absorption losses. In addition, the hydrogen may react with P 2 O 3 , GeO 2 , or B 2 O 3 , which are contained in the fibre as dopants, and forming compounds with one or more OH groups. Absorption by the OH group also increases absorption losses. One way to solve these problems is to add a liquid-phase composition which can absorb hydrogen in the fibre (Unexamined Japanese Patent Publication No. 61-251808). However, this method is impractical: the produced fibre has a limited capacity for hydrogen absorption and is structurally complex. Corning glass (International Wire & Cable Symposium Proceedings 1987, pages 241-244, and JOURNAL OF LIGHTWAVE TECHNOLOGY, vol. 6, no. 2, February 1988, pages 240-244), and AT&T (ELECTRONICS LETTERS, 13th October 1988, vol. 24, no. 21, pages 1323-1324, and OFC '88, OPTICAL FIBER COMMUNICATION CONFERENCE, Technical Digest, Tuesday 26th) have recently disclosed that coating the fibre with carbon by chemical vapour deposition (CVD) can enhance its resistance to hydrogen. The hydrogen-resistance characteristics of this carbon coating and the mechanical properties of the carbon-coated fibre depend greatly on the carbon source and on deposition conditions. At present, the CVD process cannot yet produce optical fibres that are sufficiently hydrogen-resistant and mechanically strong. In EP-A-0308143, the thermal decomposition of acetylene and trichloroloethylene to form a hermetic coating on an optical fiber is disdosed. The coating is essentially impermeable to both water and hydrogen; however, the light transmission loss of the optical fiber is not sufficiently reduced. Accordingly, it is an object of the present invention to provide a method of forming a carbon layer on an optical fibre to give it sufficient hydrogen-resistance and mechanical strength. According to the present invention, there is provided a method of forming a carbon layer on an optical fibre, characterised in that the carbon layer is formed by feeding to the optical fibre a gaseous feed material comprising at least one halogenated hydrocarbon compound having 15 or fewer carbon atoms and thermally decomposing the halogenated hydrocarbon, provided that the halogenated hydrocarbon compound does not consist of trichloroethylene. According to a further aspect there is provided the use of at least one halogenated hydrocarbon compound having 15 or fewer carbon atoms as a carbon source in a method of forming a carbon layer on an optical fibre, the carbon layer being formed by feeding a gaseous feed material comprising the said at least one halogenated hydrocarbon to the optical fibre and thermally decomposing the said at least one halogenated hydrocarbon. The present invention will now be illustrated with reference to the accompanying drawings wherein: Fig. 1 is a cross-sectional view showing an optical fibre obtainable by the present invention; Fig. 2 is a side view showing an apparatus for use in the method of the present invention, which produces the optical fibre having carbon coatings; Fig. 3 is a diagram showing the relationship between carbon coating thickness and optical fibre spinning speed for the apparatus of Figure 2 and compares this relationship with that for a conventional apparatus. Fig. 1 is an optical fibre obtainable by the present invention, where an uncoated optical glass fibre 1 made of quartz or multi-component glass is coated with carbon coating layers 2 and 3 in that order. Carbon coating layer 2 prevents diffusion of hydrogen into the uncoated optical fibre 1 and is prepared by thermally decomposing a halogenated hydrocarbon compound having 15 or fewer carbon atoms, included in a gaseous feed material as defined above. To reduce transmission losses in the optical fibre from hydrogen diffusion and to improve mechanical properties of the optical fibre, the thickness of carbon coating layer 2 should be between 0.1 to 0.6µm. When the thickness is less than 0.1µm, thinner areas or pinholes form more easily. Hydrogen then diffuses through these weak areas into the body of the optical fibre and increases transmission losses. Increasing the thickness of carbon coating layer 2 beyond 0.6µm is undesirable because it does little to improve the layer's capacity for preventing hydrogen penetration and it also tends to lead to the formation of cracks within the layer and exfoliation of the layer from the surface of the optical fibre 1. Carbon coating layer 2 is prepared by thermally decomposing a halogenated hydrocarbon compound having 15 or fewer carbon atoms. Halogenated hydrocarbons with 15 or less carbon atoms that apply to this invention include dichloromethane, dichloroethane, dichloroethylene, dichlorobenzene and trichloroethane. Considering the toxicities of the halogenated compounds, chlorine is thus the chosen halogen atom. Halogenated hydrocarbons with 2 carbon atoms are preferable because they deposit faster, forming a given thickness of carbon coating layer 2 in less time, and thus increasing optical fibre spinning efficiency. Hydrocarbons or halogenated hydrocarbons with 16 or more carbon atoms are undesirable for the present invention because they decompose too slowly to coat the uncoated optical fibre surfaces with carbon coating layer 2 efficiently. Thus, when the chemical vapour deposition process combines with the optical fibre spinning process, these hydrocarbons reduce the overall efficiency of the production process. Alcohols, ketones, esters, and other carbon compounds containing oxygen are undesirable for the present invention because they decompose too slowly to form carbon coating layer 2. Further, they produce more soot when decomposed, and the further reduces coating efficiency. The feed halogenated hydrocarbon compound may be decomposed thermally by a resistance furnace, an induction furnace, or an infrared furnace, or they may be decomposed after being ionised. In the case of ionization, the feed hydrocarbon compound is diluted with an inert gas such as nitrogen, helium, or argon, and is subjected to high-frequency waves or microwaves to generate plasma. Carbon coating layer 2 may be prepared by thermally decomposing the said halogenated hydrocarbon in its gaseous feed material between 400 and 1100°C. The thermal decomposition temperature is at least 400°C for carbonisation of the feed compounds. Increasing the temperature beyond 1100°C, on the other nand, is undesirable because it damages the carbon coating layers' ability to prevent hydrogen penetration and generates strains within the optical fibre body, increasing transmission losses and reducing mechanical strength. Furthermore, high temperatures cause spun quartz to change its cyrstal structure. Since the annealing temperature of quartz is around 1170°C, overheating releases compressive stresses on the fiber's surface, thereby reducing elasticity of the fibre and making it fragile. Therefore, the temperature at which the feed compounds are decomposed to form the carbon coating layer that increases hydrogen-resistance and mechanical strength of the optical fibre is preferably between 400 and 1100°C. When carbon coating layer 2 is prepared under the above conditions, it is free of pinholes, very capable of preventing hydrogen penetration, and hence highly desirable. The above conditions have another advantage in that they accelerate the deposition of carbon coating layer 2. If necessary, the carbon coating layer 2 may be further coated with another carbon coating layer 3. Fig. 3 shows the apparatus for producing optical fibre 1 and coating it with carbon layers. The uncoated optical fibre 1 is produced by spinning the optical fibre material (not shown) in a heated optical fibre spinning furnace 4. It is then passed to a chemical vapour-phase growth reactor furnace 5, which is housed in the lower stage of the optical fibre spinning furnace 4. The chemical vapour-phase growth reactor furnace 5 contains reactor furnaces 6 connected in series and kept air-tight. Each reactor furnace 6 consists of nearly cylindrical reactor tubes 7 which are heated by heaters 8. In the reactor tubes 7, chemical vapour-phase growth reactions are activated to coat the uncoated optical fibre 1 with carbon coating layer 2. Each reactor tube 7 has a feed compound supply tube 9 at the top, through which the feed compound is charged, and an exhaust tube 10 at the bottom, through which unreacted gas is exhausted. Many types of reactor tubes 7 and heaters 8 can be employed, depending on the temperature at which the feed compounds decompose. The feed compound may be decomposed thermally by a resistance furnace, induction furnace, or infrared furnace. Or the heater 8 may produce plasma by high-frequency waves or microwaves to ionise and decompose the feed compound. The chemical vapour-phase growth reactor 5 also has gas supply tubes at the top 11 and bottom 11, through which an inert gas such as helium or nitrogen is blown in to eliminate oxygen. The chemical vapour-phase growth reactor furnace 5 is followed by a resin coating unit 12 and a resin hardening unit 13 connected in series. These units coat the carbon coating layer formed over the uncoated optical fibre 1 in the reactor furnace with a resin coating layer 3. Using this apparatus, the optical fibres of the present invention are produced in the following manner. The optical fibre material is spun in a heated optical fibre spinning furnace 4 into the uncoated optical fibre 1. The uncoated optical fibre 1 feeds down to the chemical vapour-phase reaction furnace 5, where it passes through the reactbr tubes 7, the resin coating unit 12, and the resin hardening unit 13 successively, running at a given speed along the axes of these units. Then, the heaters start to heat the fibres running through the reaction tubes 7 to a given temperature. At the same time, the inert gas and the feed compound feed into the chemical vapour-phase reaction furnace 5 via the gas supply tubes 11 and the feed compound supply tubes 9, respectively. The feed compound for forming carbon coating layer 2 may vary so long as it is at least one halogenated hydrocarbon compound having 15 or fewer carbon atoms which thermally decomposes into carbon coating layer 2. It may be supplied in a gaseous state, or diluted with an inert gas. The feed supply rate can also vary widely depending on the type of feed compound and on the temperature at which it decomposes. The feed supply rate will generally be from 0.2 to 1.02 L/min. The thermal decomposition temperature varies depending on the type of feed compound, but is generally from 400 to 1100°C. Thermal decomposition will not take place below 400°C. Increasing the temperature beyond 1100°C is also undesirable. Excessive heat generates large quantities of by-product soot and at the same time makes carbon coating layer 2 fragile. It also makes the optical fibre fragile and less elastic because the annealing temperature of the quartz which makes up the optical fibre is 1170°C. In order to minimize formation of by-product soot, it is best to keep the reactor tubes 7 slightly below the thermal decomposition temperature of the feed compound. Thus coated with carbon coating layer 2, the optical fibre 1 then passes to the resin coating unit 12 and the resin hardening unit 13 installed below the chemical vapour-phase growth furnace 5. In the resin coating unit 12, it is further coated with an ultraviolet-setting or a thermo-setting resin. To form resin coating layer 3, the resin coating layer over the carbon coating layer is hardened in the resin hardening unit 13 under conditions suited for the resin coating. This configuration of the chemical vapour-phase growth reaction furnace 5, in which reaction furnaces 6 are connected in series, allows for increased contact time between the carbon radicals and the uncoated optical fibre 1 in the entire chemical vapour-phase reaction furnace 5. This configuration also decreases contact time in the reaction furnaces 6, so the uncoated optical fibre 1 can be coated efficiently with a high quality carbon coating layer 2. It further has the advantage of permitting higher optical fibre spinning rates. The carbon radicals formed in the reaction furnaces 6, if not deposited over the uncoated optical fibre 1, are exhausted immediately through each of the exhaust tubes 10 so that they do not react with each other to form a polymer in the reactor tubes 7. Therefore, carbon coating layer 2 over the uncoated optical fibre 1 is of made low molecular weight carbon radicals. Hence, it always has a uniform, tight structure, and effectively prevents hydrogen penetration. In the above apparatus, the carbon radicals are deposited directly over the uncoated optical fibre 1 to form carbon coating layer 2 in the uppermost reaction furnaces 6. Later, in the downstream reaction furnaces 6, carbon radicals can again be deposited over the carbon coating layer 2 to increase its thickness. When carbon coating layer 2 is produced in two stages, growth of pinholes is kept to a minimum. Carbon coating layers 2 produced this way contain fewer pinholes than coating layers of the same thickness produced by a one-stage apparatus, and so are more effective in preventing hydrogen penetration. The apparatus shown in Fig. 3 has three reaction furnaces 6 connected in series. The number of reaction furnaces can vary depending on the feed compound, the spinning rate, and other conditions. The apparatus shown in Fig. 3 has a chemical vapour-phase growth reaction furnace 5 connected below the optical fibre spinning furnace 4. The optical spinning furnace 4 and the chemical vapour-phase growth reaction furnace 5 may be connected to each other and to the resin coating unit 12 and the resin hardening unit 13 in any configuration so long as they are all kept air tight. The present invention will be described further with reference to the following examples: EXAMPLES (Example 1) A resistance furnace was connected to a 40 mm i.d. quartz tube in a spinning unit in which the optical fibre material was spun into an uncoated optical fibre. Optical fibre material, with an outer diameter of 30 mm, and with a core impregnated with GeO 2 as a dopant, was placed in the spinning unit. The material was spun at 2000°C and at a spinning speed of 30 m/min into a fibre of 125 µm o.d. 1,2 dichloroethane diluted with argon gas to about 1% by volume was used as the feed compound. The vapor-gas mixture was thenfed at about 5 l/min to the reaction tubes and kept at 1000°C, while the uncoated optical fibres were coated with the carbon coating layer. As confirmed by electron microscopic analysis, the thickness of the carbon coating layer was uniform at 0.1 to 0.3 µm over a fibre length of 1 km. (Example 2) The same procedure as described in Example 1 was followed, except that to form the carbon coating layer, 1,1,1-trichloroethane diluted with argon gas to about 1% by volume was used as the feed compound, and the resistance furnace was heated to achieve 500°C in the rection tubes. As confirmed by electron microscopic analysis, the thickness of the carbon coating layer was 0.1 to 0.3 µm over a fibre length of 1 km. (Example 3) The same procedure as described in Example 1 was followed, except that to form the carbon coating layer 1,2-dichloroethylene diluted with argon gas to about 1% by volume was used as the feed compound, and the resistance furnace was heaτed to 600°C for the reaction tubes. (Example 4) The same procedure as described in Example 1 was followed, except that to form the carbon coating layer, dichloromethane diluted with argon gas to about 1% by volume was used as the feed compound, and the resistance fumace was heated to attain 800°C in the reaction tubes. As confirmed by electron microscopic analysis, the thickness of the carbon coating layer was 0.1 to 0.2 µm over a fibre length of 1 km. (Example 5) The same procedure as described in Example 1 was followed, except that to form the carbon coating layer, the resistance furnace was heated to attain 1200°C in the reaction tubes. (Example 6) The same procedure as described in Example 1 was followed, except that to form the carbon coating layer, the resistance furnace was heated to 400°C, and 1,2-trans-dichloroethylene diluted with argon to about 1% by volume was used as the feed compound. (Comparison Example 1) A 30 mm o.d. optical fibre material with a core impregnated with GeO 2 as a dopant was spun into 125 µm fibres at 2000°C and at a speed of 30 m/min. (Test 1) The 500 m long optical fibres prepared in Examples 1 through 6 and Comparison Example 1 were measured for their light transmission losses at wavelengths of 1.24 and 1.39 µm, where absorption by OH groups occurs. Each tested fibre was then kept for 24 hours in a tightly sealed container at 150°C and at a hydrogen partial pressure of 1 atm. The fibres were again measured at the same wavelengths for light transmission losses to determine the differential transmission loss caused by penetration of hydrogen. The results are shown in Table 1. (Test 2) The optical fibres prepared in Examples 1 through 6 and Comparison Example 1 were measured for their tensile strength. Twenty fibres from each sample were subjected to pulling stresses under a gauge length of 30 cm and a strain rate of 10%/min. To determine tensile strength at a 50% fracture probability, fracture probability was plotted against tensile strength in a Weibull plot. The results are also shown in Table 1. These test results show that compared to the uncoated carbon fibre prepared in Comparison Example 1, the carbon-coated optical fibres prepared in Examples 1 through 6 are lower in differential transmission loss caused by the penetration of hydrogen and/or higher in tensile strength. Light Transmission Losses (dB/km) Tensile Fracture Strength (kg/125 mm diameter) 50% Probability Sample Measurement Wavelength of Fracture 1.24 µm 1.39 µm Example 1 1.1 2.2 4.3 Example 2 1.3 2.7 4.8 Example 3 0.7 1.9 4.1 Example 4 0.8 2.5 4.7 Example 5 5.8 4.9 2.4 Example 6 11.8 31.0 3.9 Comparison Example 1 17.3 30 3.5 Example 1 (Example 7) An apparatus similar to that shown in Fig. 2 where three sets of 50 mm i. d. infrared furnaces were connected in series, was set up underneath the spinning furnace to produce uncoated optical fibers from optical fiber material. The total length of the furnace was 100 mm. Optical fiber material with an outer diameter of 30 mm and with a core impregnated with GeO 2 as a dopant was placed in the spinning unit installed in the optical fiber production apparatus. The optical fiber material was passed into the optical fiber production apparatus and spun into 125 µm o.d. single-mode fibers at 2000°C and at a spinning speed of 20 m/min. The CVD furnace was kept at 1200°C. To coat each of the uncoated optical fibers with a carbon coating layer, a feed compound of 1,1,2-trichloroethane gas diluted with argon gas to about 5% by volume was fed through each feed supply tube at a rate of 3 l/min. The unreacted gas was purged through the exhaust pipe, which was maintained at a vacuum of -4mm of H 2 O. The carbon-coated optical fiber was coated further with a urethane acrylate resin by passing it through a die pot filled with liquefied UV resin (Young's modulus: 70 kg/mm 2 , elongation: 60%). The resin layer was hardened by a UV lamp. The final optical fiber with the resin protective layer had an outer diameter of 300µm. (Example 8) The same procedure as described in Example 7 was followed, except that the spinning rate was set at 40 m/min. (Example 9) The same procedure as described in Example 7 was followed, except that 4 reaction tubes were used instead of 3, and the spinning rate was set at 60 m/min. (Comparison Example 2) The same procedure as described in Example 7 was followed, except that 2 of 3 feed supply tubes and 2 of 3 exhaust tubes were plugged. (Comparison Example 3) The same procedure as described in Comparison Example 2 was followed, except that the chemical vapor-phase growth reaction furnace was 300 mm long, 3 times longer than the furnace used in Example 7. (Test 3) The optical fibers prepared in Examples 7 and 9 and Comparison Examples 2 and 3 were measured for their carbon coating layer thickness. Fibers from each sample were then formed into bundles 150 mm in diameter and 1 km long. Each bundle was kept for 48 hours in a pressurized container at 80°C and at a hydrogen partial pressure of 1 atm. To find the increase in hydrogen absorption losses, and fibers were again measured at a wavelength of 1.24 µm for differential transmission losses. The results are shown below in Table 2. Light Transmission Losses Thickness of Carbon Coating Layer Sample (xdB/km) (Angstroms) Example 7 0.21 1000 Example 8 0.57 800 Example 9 0.30 1000 Comparison Example 2 2. 53 150 Comparison Example 3 4. 25 800

Claims: A method of forming a carbon layer (2) on an optical fibre, characterised in that the carbon layer (2) is formed by feeding to the optical fibre a gaseous feed material comprising at least one halogenated hydrocarbon compound having 15 or fewer carbon atoms and thermally decomposing the halogenated hydrocarbon, provided that the halogenated hydrocarbon compound does not consist of trichloroethylene. A method according to claim 1, wherein the thermal decomposition is performed at 400-1,100°C. A method according to claim 1 or 2, wherein the halogenated hydrocarbon compound is selected from the group consisting of dichloromethane, dichloroethane, dichloroethylene, dichlorobenzene and trichloroethane. The use of at least one halogenated hydrocarbon compound having 15 or fewer carbon atoms as a carbon source in a method of forming a carbon layer on an optical fibre, the carbon layer being formed by feeding a gaseous feed material comprising the said at least one halogenated hydrocarbon to the optical fibre and thermally decomposing the said at least one halogenated hydrocarbon.

Inventors: ARAKI SHINJI, OOHASHI KEIJI, SHIMOMICHI TSUYOSHI, SUZUKI HIDEO, ARAKI, SHINJI, OOHASHI, KEIJI, SHIMOMICHI, TSUYOSHI, SUZUKI, HIDEO
Applicants: FUJIKURA LTD, FUJIKURA LTD.
Application year: 1989
Main classification: C03C25
IPC codes: C03C25, C23C16