Method and apparatus for drying and consolidating a preform for optical fibres
11325854 · 2022-05-10
Assignee
Inventors
Cpc classification
International classification
Abstract
A process and an apparatus for drying and consolidating an optical fibre preform in a furnace tube comprising a heating chamber, wherein an extension tube having an extension chamber configured to house at least a length portion of the preform is removably joined to the furnace tube and the drying process starts with the preform not completely inserted into the furnace tube, an upper length portion of the preform being surrounded by the extension tube joint to the furnace tube.
Claims
1. A method for manufacturing an optical fibre preform comprising: providing a furnace comprising a furnace tube having an elongated heating chamber configured to house a preform, the heating chamber having an upper entry opening for the insertion of the preform; providing an extension tube comprising an extension chamber having a lower opening and configured to house at least a length portion of a preform; inserting a lower length portion of an optical fibre preform, the preform being a porous preform, in the heating chamber in such a way that an upper length portion of the optical fibre preform lies outside of the furnace tube; enclosing the upper length portion of the optical fibre preform in the extension tube; joining the furnace tube with the extension tube so as the lower opening of the extension chamber is in communication with the upper entry opening of the heating chamber to form a single chamber; dehydrating the lower length portion of the preform by exposing said lower length portion to a first heating zone of the furnace tube set at a dehydration temperature, and gradually lowering the optical preform through the first heating zone so as to dehydrate the upper length portion of the optical fibre preform, wherein, the furnace tube has a second heating zone positioned below the first heating zone and set at a consolidation temperature, wherein gradually lowering the optical fibre preform further comprises exposing successive length portions of the preform to the first heating zone and subsequently to the second heating zone until the whole optical fibre preform has passed through the first heating zone.
2. The method of claim 1, further comprising, after passing the optical fibre preform through the first heating zone, continuing to gradually lower the preform through the second heating zone until the whole optical fibre preform has passed through the second heating zone so as to consolidate the whole optical fibre preform.
3. The method of claim 1, further comprising, before inserting a lower length portion of the optical fibre preform, holding in suspension the optical fibre preform by a supporting member connected to a first lifting mechanism for vertically moving the preform.
4. The method of claim 3, further comprising, after providing an extension tube and before enclosing the upper length portion of the optical fibre preform, holding in suspension the extension tube above the optical fibre preform and lowering the extension tube until it surrounds and encloses the upper length portion of the optical fibre preform.
5. The method of claim 1, further comprising, after providing an extension tube and before enclosing the upper length portion of the optical fibre preform, holding in suspension the extension tube above the optical fibre preform and lowering the extension tube until it surrounds and encloses the upper length portion of the optical fibre preform.
6. The method of claim 5, wherein the extension tube is connected to a second lifting mechanism for a vertical movement independent of the vertical movement of the preform.
7. The method of claim 1, wherein the first heating zone is vertically positioned adjacent to the upper entry opening such that the preform enters the first heating zone right after the insertion in the furnace tube.
8. The method of claim 1, wherein gradually lowering of the optical fibre preform is at a downfeed rate is of from 4 mm/min to 7 mm/min.
9. An apparatus for drying a porous optical fibre preform, comprising: a furnace comprising a furnace tube comprising an elongated heating chamber for housing and moving a preform in a vertical direction, wherein the heating chamber has an upper entry opening for the insertion of the preform, the furnace further comprising a first heater surrounding the furnace tube for heating a first longitudinal section of the heating chamber defining a first heating zone, and an extension tube comprising an extension chamber having a lower opening, the extension tube being removably joint to the furnace tube so as to close the upper entry opening, wherein the lower opening is in communication with the upper entry opening when the extension tube is joined to the furnace tube to form a single chamber, the extension chamber being configured to house at least a length portion of the preform, wherein: the appearance is for drying and consolidating a porous optical fibre preform and the furnace further comprises a second heater placed below the first heater and surrounding the furnace tube for heating a second longitudinal section of the heating chamber defining a second heating zone for consolidation of the porous optical fibre preform.
10. The apparatus of claim 9, wherein the furnace tube and the extension tube are made of glass so as joining the furnace tube with the extension tube is a glass-to-glass seal.
11. The apparatus of claim 9, wherein the furnace tube comprises a first flange positioned radially outwardly the upper entry opening and the extension tube comprises a second flange positioned radially outwardly the lower opening, the first and the second flange comprising a respective joining surface, wherein joining is achieved by joining the joining surfaces of the first and of the second flanges.
12. The apparatus of claim 9, further comprising a supporting member for holding in suspension a preform, the supporting member being operatively connected to a first lifting mechanism for the translational movement of the preform up and down in the longitudinal direction (20), wherein the supporting member comprises a holding portion for holding the preform and a supporting rod for the connection with the first lifting mechanism.
13. The apparatus of claim 9, wherein the extension tube is operatively connected to a second lifting mechanism for holding in suspension the extension tube above the preform when it is not joined to the furnace tube and for causing the extension tube to move up and down independently of the supporting member.
14. The apparatus of claim 13, wherein the extension tube comprises a cover plate opposite to the lower opening and having a throughhole through which the supporting rod passes.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The present invention will now be described in more detail hereinafter with reference to the accompanying drawings, in which some, but not all embodiments of the invention are shown.
(2) Drawings illustrating the embodiments are not-to-scale schematic representations.
(3) For the purpose of the present description and of the appended claims, except where otherwise indicated, all numbers expressing amounts, quantities, percentages, and so forth, are to be understood as being modified in all instances by the term “about”. Also, all ranges include the maximum and minimum points disclosed and include any intermediate ranges therein, which may or may not be specifically enumerated herein.
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DETAILED DESCRIPTION
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(15) Preferably, the furnace tube 11 is made of glass, more preferably quartz. Customarily, furnace tubes for the processing a silica-based preform for the production of optical transmission fibres are made of highly pure quartz to avoid contaminations in the preform during heating.
(16) The furnace tube 11 further comprises a first flange 14 placed radially outwardly the upper entry opening 15. The first flange 14 has an upper surface (non visible in the figures), indicated in the following with first joining surface. In an embodiment, the first flange is an annular flange.
(17) The furnace 9 comprises a first heater 13 surrounding the furnace tube 11. The first heater defines a first heating zone extending over a first length of the furnace tube and thus of the heating chamber. In operation, the first heating zone is set at a first temperature suitable for dehydration of the porous layers of the preform.
(18) The Applicant has observed that complete drying can be achieved by moving the preform through a heating zone of a relatively limited longitudinal extension, at a suitable downfeed rate. The Applicant has realised that, if the size of the first heating zone in the downfeed direction is reduced, a significant reduction of the furnace tube length can be obtained by positioning the first heating zone in an upper portion of the furnace tube.
(19) Preferably, the first heater 13 surrounds the furnace tube 11. Preferably, the first heater has a ring shape which may comprise one or more annular heating elements.
(20) A second heater 12, positioned below the first heater 13, surrounds the furnace tube 11. The second heater defines a second heating zone extending over a second length of the furnace tube, the second heating zone being positioned below the first heating zone. In operation, the second heating zone is set at a second temperature for consolidation of the porous preform into a solid glass preform. The second temperature is higher than the first temperature and it is usually of from 1450° C. to 1550° C. In an embodiment, the second temperature is of 1500° C.
(21) Preferably, the second heater 12 has a ring shape which may comprise one or more annular heating elements. For example, the first and the second heaters 13, 12 are attached to the outer circumference of the furnace tube.
(22) The apparatus 10 further comprises a hollow extension tube 19, shown in more detail in
(23) Preferably, the heating chamber has an inner diameter substantially equal to the inner diameter of the extension tube so as to form an extended hollow cylindrical chamber when the two chambers are joined.
(24) Preferably, the extension tube has a length such that an upper length portion of the preform is contained in the extension tube when the latter surrounds the preform. In a preferred embodiment, the length of the extension tube is selected to be equal to the difference between the length of the preform and the length of the dehydration zone of the furnace. In some embodiments, the length of the extension tube is selected so as to surround an upper length portion of from 30% to 50% of the total preform length. Preferably, the length of the extension tube is between 0.5 and 2.5 m. For example, the extension tube has a length of 1.2 m.
(25) The extension chamber 21 is provided at one of its ends with a lower opening 24 for the insertion of the preform. Opposite to the lower opening 24, the extension tube comprises a cover plate 22 having a through-hole 23, preferably centrally positioned in said cover plate 22. A second flange 25 is positioned at the lower opening 24 and extends radially outwardly from the lower opening. The second flange 25 has an exterior-facing surface 25a, which corresponds to the below surface when the extension tube 19 is placed in the apparatus for drying and consolidating. The surface 25a is referred to as the second joining surface. The extension tube 19 is preferably one-piece. Preferably, the extension tube is made of quartz.
(26) Referring back to
(27) The first and second joining surfaces of the respective flanges 14, 25 are mating surfaces when the extension tube 19 is placed on top of the furnace tube so as to put in communication the heating chamber with the extension chamber and form an extended elongated chamber. With the furnace tube and the extension tube made of glass, preferably quartz, joining of the furnace tube with the extension tube is a glass-to-glass seal. The first and the second joining surfaces are flat surfaces, preferably polished to reduce the surface roughness so as to prevent gas leakage between the surfaces. A suitable surface roughness is for example 0.8 Ra. Surface finishing for reducing roughness and improving flatness of the quartz joining surfaces can be made in a way per se known.
(28) Dehydration of the preform is achieved by moving the preform through a first heating zone of a relatively limited length, i.e. shorter than the length of the preform. The first heater and thus the first heating zone extends along the furnace longitudinal direction for a first length.
(29) Preferably, the first length of the first heating zone is of from 50 cm to 100 cm. For example, the first length is 60 cm.
(30) By providing an extension chamber for housing a length portion of the preform, drying may take place in a furnace having a first heating zone arranged at the top of the furnace tube. In the preferred embodiments, the first heating zone for drying the preform is placed close to the entry opening of the furnace tube.
(31) With “close to the entry” of the furnace tube, when referred to the arrangement of the first heater/heating zone, it is meant the uppermost possible vertical position while taking into account practical considerations, such as the isolation and furnace shell surrounding the heating elements. In some embodiments, the first heater 13 is arranged so as to form a first heating zone having an upper end at a distance of not less than 30 cm from the entry opening 15 of the furnace tube, preferably from 30 cm to 60 cm from the entry opening of the furnace tube 11.
(32) With the first heater 13 arranged at a vertical position close to the entry opening 15 of the furnace tube, the preform lies in the first heating zone right after the insertion in the furnace tube.
(33) The second heating zone extends along the furnace longitudinal direction for a second length.
(34) Preferably, the second length of the second heating zone is of from 30 cm to 50 cm.
(35) In some embodiments, the preform has a length of from 2.0 to 3.5 meters.
(36) In some embodiments, the heating chamber of the furnace tube extends below the second heating zone for a length configured to house the whole preform. This longitudinal section of the heating chamber positioned below the second heating zone is not heated and defines a cooling zone for allowing the preform to cool, preferably while flowing inert gas across the furnace.
(37) Preferably, the furnace tube has a length of two times the length of the longest preform to be processed in the furnace.
(38) The furnace 9 comprises a gas inlet opening 26 connected to the heating chamber of the furnace tube 11 for the supply of one or more drying gases, such as a mixture of helium and chlorine. Gases entering the gas inlet 26 pass through the porous glass to remove impurities and reduce the water content of the glass. Usually, gases are discharged from a gas discharge opening positioned at the opposite side of the furnace body with respect to the gas inlet opening, e.g. bottom to top. According to the preferred embodiments, elements for carrying away the gases from the furnace tube and from the extension tube, when the two chambers are joined, are connected to the extension tube.
(39) With reference to
(40) A shaft 36 is placed in the vicinity of the entry of the furnace tube for holding the pipe in position for the connection to the gas discharge opening of the exhaust hood 37. It is to be understood that the presence of a means for holding the discharge pipe is optional since other configurations may be envisaged for the discharge of the gases from the extension chamber enclosing the preform during the process of dehydration and consolidation.
(41) The apparatus 10 further comprises a moving system 27 for the translational movement of the preform 16 and of the extension tube 19. In the embodiment of the figures, a downfeed tower 33 acts as a supporting structure, which the moving system 27 is fixed to. The downfeed tower 33 stands on a base 32, which may be an upper floor having an opening for communication with the furnace tube, standing on a lower floor (non shown). In the embodiment, the upper entry opening 15 of the furnace tube and the surrounding flange 14 are positioned on the upper floor 32.
(42) In the usual ways, the preform 16 is suspended on a supporting member 18, shown more in detail in
(43) The moving system comprises a first lifting mechanism and a second lifting mechanism. The first lifting mechanism is configured to lower the preform into the furnace tube 11 and to lift the preform up from the furnace tube when the process of drying and consolidation has been completed. In the embodiment, the first lifting mechanism raises and lowers a motor-driven carriage 29 along a pair of guide rails 28, 28′ arranged parallel to the longitudinal axis of the furnace tube 11 for the vertical movement. For example, the guide rails 28, 28′ stand on the floor 32 (as shown in
(44) The extension tube 19 is moved up and down by a second lifting mechanism that moves cables 30 and 30′, which are spooled on a pair of reels 38, 38′ coupled together and mounted on the carriage 29. An idler pulley 39 can be used to maintain tension of cables 30, 30′. The reels 38, 38′ are driven by a motor (not shown) mounted on the carriage 29 for winding and unwinding cables 30, 30′. The cables 30 and 30′ are connected with the extension tube 19 for enabling the up and down movement of the extension tube, which is performed by controlling the motor of the reels.
(45) The horizontal position (i.e. in a plane perpendicular to the longitudinal axis 20) of the supporting rod 18b is such that to allow the supporting rod 18b of the supporting member 18 to pass through the through-hole 23 of the extension tube 19 and the corresponding through-hole of the exhaust hood 37 without mutual interference. For example, lateral dimensions (e.g. diameters) of the supporting rod and of the through-hole 23 are such that a lateral play exists between the support rod and the extension tube. An alignment system, per se known and not shown, can be used for adjusting the horizontal position of the preform and/or of the extension tube.
(46) Automatic control enabling independent movement of the carriage 29 and the cables 30, 30′ can be performed in ways per se known, such us by means of a motion controller software platform logically connected to the motors of the carriage and of the cable reels for control of the vertical location, along longitudinal axis 20, of the preform and the extension tube.
(47) It is to be understood that other configurations of the moving system 27 may be envisaged, as long as they provide an independent vertical movement of the extension tube and the preform. In a first initial stage, shown in
(48) The preform 16 is then lowered into the furnace tube 11.
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(50) Preferably, the extension tube descents after the preform is partly inserted in the furnace. It is however to be understood that descent of the extension tube to a vertical location such that to surround the upper length portion of the preform may be performed when the preform has not entered the furnace, for example in the stage shown in
(51) When the extension tube 19 is joint to the furnace tube, the temperature of the second heater 13 is increased to a temperature suitable for consolidation, e.g. 1500° C. As shown in more detail in
(52) An exemplary temperature profile 40, along the furnace tube, for dehydration and consolidation is shown in
(53) Subsequently, the preform is gradually lowered through the first heating zone at a given rate so as to dehydrate the whole preform when the entire preform length has passed the first heating zone. Preferably, the downfeed rate is of from 4 mm/min to 7 mm/min. For example, the downfeed rate is of 5 mm/min.
(54) When the preform is down driven through the first heating zone 13, successive longitudinal portions of the preform are exposed to the first heating zone 13 and subsequently to the second heating zone 12.
(55) Preferably, the second heating zone 12 set at a temperature suitable for vitrification of the dried soot material, is positioned at a relatively short distance from the first heating zone so as, during the descent of the preform, two different portions of the preform are exposed to a first heating zone and to a second heating zone, respectively, until the whole preform exits the first heating zone. Then, a remaining upper portion of the dried preform undergoes consolidation by passing through the second heating zone in order to fully consolidate the preform from the bottom to the top. The process of drying and consolidation ends when the whole preform exits from the second heating zone.
(56) In some embodiments, during dehydration and consolidation, the preform rotates about its longitudinal axis in order to improve axial symmetry. In ways per se known, a rotation transmission mechanism (not shown) coupled to the supporting rod 18b transmits rotation to the preform.
(57) After vitrification of the whole preform has been carried out, the temperature of the second heater is lowered. The preform is lowered to the cooling zone for cooling, preferably in the presence of inert gases flowing through the furnace tube.
(58) After cooling, the furnace tube is opened by lifting the extension tube up and the preform is removed from the furnace tube.
(59) It should be understood that the terms “lower” or “below” and “upper” or “above”, with reference e.g. to the openings of the chambers housing the preform and to the longitudinal portions of the preform, are used to indicate the relative position of the elements to one another in their orientation during processing of the preform.
(60) By “porous preform” in this application it is meant both a totally porous preform (e.g. for the formation of a glass core rod) and a partially porous preform comprising a porous soot layer for the formation of the overcladding on a core rod.
(61) The apparatus and the process according to present disclosure are particularly suitable for the drying and consolidating of a final preform having a porous overcladding layer formed around a core rod. In ways per se known, after consolidation, the solid glass preform can be drawn in an optical fibre.
(62) Preferably, the porous glass soot preform is a silica-based porous glass preform for the fabrication a silica-based optical fibre of low attenuation for use in telecommunication systems. The porous soot layers can be formed by a flame hydrolysis process of silica-based soot, such as outside vapour deposition (OVD) and vapour axial deposition (VAD).