NL2019098B1

NL2019098B1 - Method of applying coating liquid to an optical fiber

Info

Publication number: NL2019098B1
Application number: NL2019098A
Authority: NL
Inventors: Clark Moore Robert; Gregg Neilson Douglas; Edward Watson Johnnie
Original assignee: Corning Inc
Priority date: 2017-04-24
Filing date: 2017-06-20
Publication date: 2018-11-05
Also published as: CN110546119B; JP7050089B2; CN110546119A; JP2020517435A; RU2019137429A; DK3395775T3; RU2019137429A3; RU2763944C2

Abstract

The invention relates to a method of applying a coating liquid to an optical fiber. An optical fiber is drawn through a guide die into a pressurized coating chamber and through the pressurized coating chamber to a sizing die. The pressurized coating chamber contains a coating liquid. The method includes directing coating liquid in a direction transverse to the processing pathway of the optical fiber in the pressurized coating chamber. The transverse flow of coating liquid counteracts detrimental effects associated with gyres that form in the pressurized coating chamber during the draw process. Benefits of the transverse flow include removal of bubbles, reduction in the temperature of the gyre, improved wetting, homogenization of the properties of the coating liquid in the pressurized coating chamber, and stabilization of the meniscus.

Description

Octrooicentrum

Nederland

(21) Aanvraagnummer: 2019098 © Aanvraag ingediend: 20 juni 2017

Θ 2019098 © BI OCTROOI (51) Int. CL:

C03C 25/10 (2017.01) C03C 25/12 (2018.01) C03C

25/18 (2018.01)

(30) Voorrang:	© Octrooihouder(s):
24 april 2017 US 62/489,123	Coming Incorporated te CORNING, New York,
	Verenigde Staten van Amerika, US.
(4^ Aanvraag ingeschreven:
5 november 2018	© Uitvinder(s):
	Robert Clark Moore te CORNING, New York
(43) Aanvraag gepubliceerd:	(US).
	Douglas Gregg Neilson te CORNING,
	New York (US).
© Octrooi verleend:	Johnnie Edward Watson te CORNING,
5 november 2018	New York (US).
© Octrooischrift uitgegeven:
6 februari 2019	© Gemachtigde:
	ir. P.J. Hylarides c.s. te Den Haag.

(© METHOD OF APPLYING COATING LIQUID TO AN OPTICAL FIBER © The invention relates to a method of applying a coating liquid to an optical fiber. An optical fiber is drawn through a guide die into a pressurized coating chamber and through the pressurized coating chamber to a sizing die. The pressurized coating chamber contains a coating liquid. The method includes directing coating liquid in a direction transverse to the processing pathway of the optical fiber in the pressurized coating chamber. The transverse flow of coating liquid counteracts detrimental effects associated with gyres that form in the pressurized coating chamber during the draw process. Benefits of the transverse flow include removal of bubbles, reduction in the temperature of the gyre, improved wetting, homogenization of the properties of the coating liquid in the pressurized coating chamber, and stabilization of the meniscus.

NL Bl 2019098

Dit octrooi is verleend ongeacht het bijgevoegde resultaat van het onderzoek naar de stand van de techniek en schriftelijke opinie. Het octrooischrift komt overeen met de oorspronkelijk ingediende stukken.

METHOD OF APPLYING COATING LIQUID TO AN OPTICAL FIBER

The invention relates to a method for coating an optical fiber. More particularly, this description relates to a method according to the invention for applying a coaling liquid to an optical fiber.

The transmittance of light through an optical fiber is highly dependent on the properties of the coatings applied to the fiber. The coatings typically include a primary coating and a secondary coating, where the secondary coaling surrounds the primary coating and the primary coating contacts the glass waveguide (core + cladding) portion of the fiber. The secondary coating is a harder material (higher Young’s modulus) than the primary coating and is designed to protect the glass waveguide from damage caused by abrasion or external forces that, arise during processing and handling of the fiber. The primary coating is a softer material (low Young’s modulus) and is designed to buffer or dissipates stresses that result from forces applied to the outer surface of the secondary coating. Dissipation of stresses within the primary layer attenuates the stress and minimizes the stress that reaches the glass waveguide. The primary coating is especially important, in dissipating stresses that arise when the fiber is bent. The bending stresses transmitted to the glass waveguide on the fiber needs to be minimized because bending stresses create local perturbations in the refractive index profile of the glass waveguide. The local refractive index perturbations lead to intensity losses for the light, transmitted through the waveguide. By dissipating stresses, the primary coating minimizes bend-induced intensity losses,

A coating liquid commonly used in the manufacture of optical fibers is an acry late-based composition which is curable by exposure to heat or ultraviolet (UV) light. The coating liquid is applied to the surface of the fiber in a liquid state and is subsequently exposed to heat or UV light for curing. The coating liquid may be applied in one or more layers, with a two-Jayer coating system (primary + secondary) often being a preferred embodiment. The primary coating is applied directly to the surface of the fiber, and the secondary coating is applied over the primary coating.

In a typical optical fiber draw process, fiber is continuously drawn from a glass preform at a particular draw speed. The glass preform includes a central region having the core composition desired for the drawn fiber and one or more surrounding annular regions having the composition desired for one or more cladding regions of the drawn optical fiber. The preform is positioned tn a draw furnace and heated sufficiently to soften the glass. The action of gravity leads to extension of glass from the softened portion of the preform. As the glass extends, it thins and forms a fiber. The diameter of the fiber is controlled, the fiber is cooled, and is then directed to a coating unit for application of one or more coating liquids. The coating liquids are cured to form sol id coatings and the coated fiber is taken up and wound on a spool. The route traversed by the fiber as it progresses from the draw furnace to the spool is referred to as the process pathway.

There is a continuing need to reduce the cost of optical fiber manufacturing by increasing the draw speed. As draw speed increases, however, it becomes more difficult to apply and cure the coating liquid. In particular, it becomes more difficult to achieve coatings with uniform thickness over the length and circumference of the fiber. Uniformity of coating thickness is needed to facilitate splicing and joining of coated fibers, and to attach connectors to the ends of coated fibers. There is currently a need for coaling processes that permit formation of coatings of uniform thickness on glass fibers in continuous high speed draw processes.

A method of applying a coating liquid to an optical fiber according to the invention is described that obviates or at least reduces one or more of the foregoing needs. An optical fiber is drawn through a guide die into a coating chamber and through the coating chamber to a sizing die. The coating chamber contains a coating liquid. The method includes directing coating liquid in a direction transverse to the processing pathway of the optical fiber in the coating chamber. The transverse flow of coating liquid counteracts detrimental effects associated with gyres that, form in the coating chamber during the draw process. Benefits of the transverse flow include removal of bubbles, reduction in the temperature of the gyre, improved wetting, homogenization of the properties of the coating liquid in the coating chamber, and stabilization of the meniscus.

The present invention relates to a method of processing an optical fiber comprising: drawing an optical fiber through a guide die to a pressurized coating chamber at a draw speed, said pressurized coating chamber containing a first coating liquid; forming a meniscus of said first coating liquid on said optical fiber in said pressurized coating chamber;

forming a boundary layer on said optical fiber in said pressurized coating chamber, said boundary layer comprising said first coating liquid and initiating at said meniscus, said boundary layer having a thickness that increases with increasing distance from said guide die;

drawing said optical fiber through said pressurized coating chamber at said draw speed to a sizing die, said sizing die inducing constriction of said boundary layer, said constriction causing expulsion of said first coating liquid from said boundary layer to said pressurized coating chamber and formation of a gyre in said pressurized coating chamber, said gyre comprising said first coating liquid;

drawing said optical fiber through said sizing die at said draw speed, said optical fiber exiting said sizing die with a surface layer of said first coating liquid; and flowing said first coating liquid in said coating chamber in a transverse direction through a channel positioned between said guide die and said sizing die.

Additional features and advantages will be set forth in the detailed description which follows, and in part will be readily apparent to those skilled in the art from the description or recognized by practicing the embodiments as described in the written description and claims hereof, as well as the appended drawings.

It is to be understood that both the foregoing general description and the following detailed description are merely exemplary, and are intended to provide an overview or framework to understand the nat ure and character of the claims.

The accompanying drawings are included to provide a further understanding, and are incorporated in and constitute a part of this specification. The drawings are illustrative of selected aspects of the present description, and together with the specification serve to explain principles and operation of methods, products, and compositions embraced by the present description. Features shown in the drawing are illustrative of selected embodiments of the present description and are not necessarily depicted in proper scale.

While the specification concludes with claims particularly pointing out and distinctly claiming the subject matter of the written description, it is believed that the specification will be better understood from the following written description when taken in conjunction with the accompanying drawings, wherein:

Figure 1 shows a calculated boundary layer of coating liquid on an optical fiber. Figure 2 shows a conventional design of a sizing die.

Figure 3 shows a cone-only design of a sizing die.

Figure 4 shows a calculated temperature profile of a gyre formed by a sizing die having a conventional design.

Figure 5 shows a calculated temperature profile of a gyre formed by a sizing die having a cone-only design.

Figure 6 depicts transverse flow of a coating liquid in a coating chamber operatively coupled to a sizing die having a conventional design.

Figure 7 depicts transverse flow of a coating liquid in a pressurized coating chamber operatively coupled to a cone-only sizing die.

Figure 8 depicts transverse flow of a coating liquid through a channel in a pressurized coating chamber positioned bet ween a guide die and sizing die.

Figure 9 depicts a coating unit with pressurized coating chambers for applying a primary coating liquid and a secondary coating liquid to an optical fiber.

Figure 10 depicts a coating unit with pressurized coating chambers for applying a primary coating liquid and a secondary coating liquid to an optical fiber.

The embodiments set forth in the drawings are illustrative in nature and not intended to be limiting of the scope of the detailed description or claims. Whenever possible, the same reference 5 numeral will be used throughout the drawings to refer to the same or like feature.

The present disclosure is provided as an enabling teaching and can be understood more readily by reference to the following description, drawings, examples, and claims. To this end, those skilled in the relevant art will recognize and appreciate that many changes can be made to the various aspects of the embodiments described herein, while still obtaining the beneficial results. It 10 will also be apparent that some of the desired benefits of the present embodiments can be obtained by selecting some of the features without utilizing other features. Accordingly, those who work in the art will recognize that many modifications and adaptations are possible and can even be desirable in certain circumstances and are a part of the present disclosure. Therefore, it is to be understood that this disclosure is not limited to the specific compositions, articles, devices, and methods disclosed unless otherwise specified. It is also to be understood that the terminology used herein is for the purpose of describing particular aspects only and is not intended to be limiting.

The present description refers to methods and processes for forming optical fibers. In a continuous optical fiber manufacturing process, an optical fiber is drawn from a heated preform positioned in a draw furnace and passed through a series of processing stages. Processing stages typically include metrology units (e.g. fiber diameter control) to assess quality and other characteristics of the optical fiber, heating stages, cooling states, a primary coating stage, a secondary coating stage, an ink layer stage, one or more curing stages to cure coating liquids or ink layer liquids applied to the fiber, and a spool or other winding stage to receive and store the coated optical fiber. The pathway traversed by the optical fiber as it passes from the draw furnace through one or more process units to the winding stage is referred to herein as the process pathway of the optical fiber. The process pathway may be linear or may include turns.

The relative position of one process unit relative to another process unit along the process pathway is described herein as upstream or downstream. The upstream direction of the process pathway is the direction toward the preform and the downstream direction of the process pathway 30 is the direction toward the winding stage. Positions or processing units upstream from a reference position or processing unit are closer, along the process pathway, to the preform than the reference position or processing unit. A process unit located at a position closer to the draw furnace along the process pathway is said to be upstream of a process unit located at a position further away from the draw furnace along the process pathway. The draw furnace is upstream from all other process units 35 and the take-up spool (or winding stage or other terminal unit) is downstream of all other process units. By way of example, the process pathway of an optical fiber in an illustrative draw process extends from a draw furnace to a cooling unit, from the cooling unit to a coating application unit., from the coaling application unit to a coating curing unit, and from the coating curing unit to a take-up spool. In the context of the terminology used herein, the draw furnace is upstream of the cooling unit, which is upstream of the coating application unit, which is upstream from the coating curing unit, which is upstream of the take-up spool. Similarly, the take-up spool is downstream of the coating curing unit, which is downstream of the coating application unit, which is downstream of the cooling unit, which is downstream of the draw furnace.

The present description provides a method for applying a coating liquid to an optical fiber. The method is used to apply a coating liquid to a glass fiber, a coating liquid to another coating liquid, or a coating liquid to a cured coating. The method includes directing an optical fiber along a process pathway that includes passing an optical fiber through a coaling application unit. The coating application unit includes a guide die, a pressurized coating chamber and a sizing die. The pressurized coating chamber contains a coating liquid that is used to coat the optical fiber. The guide die is upstream of the pressurized coating chamber, which is upstream of the sizing die. The optical fiber passes through the guide die into the pressurized coating chamber, through the pressurized coating chamber to the sizing die, and through the sizing die to downstream units in a fiber draw process.

The present method enables high draw speed processes for manufacturing optical fibers. Draw' speed is currently limited by two problems: (1) difficulties in wetting the optical fiber with the coating liquid as it exits the guide die and enters the coating chamber; and (2) increased severity of effects associated with gyres formed in the coating chamber in the vicinity of the sizing die as the optical fiber exits the coating chamber. The present method addresses both problems and allows for increased draw speed while minimizing coating defects. Draw speeds available from the current method are at least 30 m/s, or at least 40 m/s, or at least 50 m/s, or at least 60 m/s, or at least 70 m/s, or in the range from 30 m/s - 90 mA. or in the range from 40 m/s -- 80 m/s.

As the fiber exits the guide die and enters the coating chamber, it contacts the coating liquid. As the fiber wets, a meniscus of coating liquid forms on the fiber adjacent the exit of the guide die. Coating liquid is entrained by the fiber as it progresses along the process pathway to the sizing die, The fiber exits the sizing die with a layer of coating liquid adhered to it and is directed along the process pathway to a downstream processing unit (e.g. another coating unit or a curing unit). The thickness of coating liquid applied to the fiber is determined by the geometry of the sizing die, the viscosity of the coating liquid, the temperature of the fiber, and the draw speed. The diameter of the exit of the sizing die is particularly important in establishing the thickness of coating liquid applied to the fiber.

Successful coating and uniformity of coating thickness requires effective wetting of the fiber by the coating liquid as the fiber enters the coating chamber. The ambient of the fiber as it passes through the guide die is a gas (e.g. air, CO?, He). By virtue of the motion of the fiber through the gas ambient, a gas boundary layer forms on the surface of the fiber as it passes through the guide die. The gas boundary layer remains with the fiber as it exits the guide die and enters the coating chamber.

Wetting refers to the process of displacing the gas boundary layer with the coating liquid as the fiber contacts and passes through the coating liquid. When the fiber is properly welted with the coating liquid, a meniscus of coating liquid forms at the interface of the surface of the fiber and the 10 coating liquid in the vicinity of the exi t of the guide die and a boundary layer of coating liquid forms on the fiber from the tip of the meniscus as the optical fiber is conveyed toward the exit of the sizing die.

If the coating liquid fails to wet the fiber, a gas boundary layer remains on the fiber. This leads to entrainment of gas into the coating chamber and incorporation of gas in the coating liquid.

The presence of gas in the coating liquid leads to the formation of bubbles in the coating liquid and to inclusion of the bubbles in the coating liquid applied to the fiber. The bubbles destabilize the meniscus and lead to non-uniformities in the coverage of coating liquid on the surface of the fiber.

The bubbles entrapped in coating liquid adhered to the fiber remain in the coating when the coating liquid is cured downstream of the sizing die. Bubbles in the cured coating constitute defects that 20 compromise the performance of the fiber and facilitate delamination of the cured coating. The presence of bubbles in the coating chamber also makes it difficult to center and stabilize the position of the fiber as it passes through the coating application unit, an effect that further contributes to non-uniformity in coating thickness.

As draw speed increases, the force needed to displace the gas boundary layer increases. In the present method, force sufficient to displace the gas boundary layer to enable wetting of the fiber at high draw speeds is achieved with a pressurized coating chamber. By increasing the pressure of the coating liquid in the coating chamber, greater force is available for applying the coating liquid to the fiber and consistent wetting of the fiber is maintained at the draw speeds disclosed herein. Pressurization of the coating chamber can be accomplished by equipping the coating chamber with a pressure transducer and using the pressure transducer to control the pressure of the coating chamber, In one embodiment, the stream of coating liquid deli vered to the coating chamber is supplied from a pressurized source. By increasing the pressure of the coating chamber, the pressure of coating liquid in the coating chamber is increased and it becomes possible to overcome the pressure associated with the gas phase boundary layer to achieve wetting as draw speed is increased.

As used herein, pressurized coating chamber refers to a coating chamber having a pressure greater than 1.01 bar (0 psig). In various embodiments, the pressure of the pressurized coating chamber is at least 1.02 bar (0.10 psig), or at least 1.05 bar (0.50 psig), or at least 1.08 bar (1.0 psig), or at least 1.36 bar (5.0 psig), or at least 1.70 bar (10 psig), or at least 2.74 bar (25 psig), or at least 4.46 bar (50 psig), or at least 7.91 bar (100 psig), or at least 14.80 bar (200 psig), or in the range twin 1.02 bar 21.70 bar (0.10 psig -- 300 psig), or in the range from 1,03 bar 19.97 bar (0.25 psig - 275 psig), or in the range from 1.05 bar - 18.25 bar (0.50 psig - 250 psig), or in the range lwm 1.08 bar - 16.53 bar (1.0 psig - 225 psig), or in the range from 1.36 bar - 14.80 bar (5.0 psig - 200 psig), or in the range from 1.70 bar - 13,08 bar (10 psig - 175 psig), or in the range from 2,74 bar 11.36 bar (25 psig 150 psig) or in the range from 4.46 bar 7.91 bar (50 psig 100 psig), where psig refers to gauge pressure in units of psi (pounds per square inch). The higher pressure of coating liquid in the pressurized coaling chamber leads to a higher meniscus pressure. Higher draw speeds are accordingly achieved by stabilizing a meniscus of coating liquid having a high pressure. The pressure of the meniscus of the coating liquid provided by the present method is greater than 0 psig, or at. least. 0.10 psig, or at least 0.50 psig, or at least 1.0 psig, or at least 5.0 psig, or at least 10 psig, or at least 25 psig, or at least 50 psig, or at least 100 psig, or at least 200 psig, or in the range from 0.1 psig - 500 psig, or in the range from 1.0 psig - 400 psig, or in the range from 5.0 psig 300 psig, or in the range from 10 psig 200 psig.

Measures taken to increase meniscus pressure are complicated by effects that occur in the vicinity of the sizing die as the optical fiber exits the coaling chamber. As noted above, as a wetted fiber moves from the guide die to the sizing die, a meniscus of coating liquid forms on the fiber and a boundary layer of coating liquid develops at the tip of the meniscus. The boundary layer extends with the fiber as it passes through the coating liquid. Figure 1 shows a calculated (finite element) boundary layer of a coating liquid on an optical fiber as it passes through a coating chamber. Optical fiber 10 enters coating chamber 20 through guide die exit 30, passes through coating chamber 20 to sizing die 40 and exits through sizing die exit 50. Coating chamber 20 contains a coating liquid and optical fiber 10 is wetted with the coating liquid as it enters coating chamber 20 through guide die exit 30. For purposes of the calculation, wetting of optical fiber 10 includes complete displacement of the gas boundary layer associated with optical fiber 10 in the guide die by the coating liquid and occurs without formation of bubbles in coating chamber 20.

As optical fiber 10 passes through coating chamber 20, a boundary layer 60 of coating liquid forms. The thickness of boundary layer 60 increases as optical fiber 10 progresses toward sizing die 40. To a first order approximation, the thickness of the boundary layer is proportional to (vX/Vf), where V is the kinematic viscosity of the coating liquid, X is the distance along the fiber pathway of a position in the boundary layer relative to the point of initiation of the boundary layer at the meniscus tip in the vicinity of the guide die exit, and V_tis the draw speed of the fiber.

Sizing die 40 includes tapered surface 70 that constricts the space available for coating liquid. As constriction occurs, a portion 80 of the coating fluid from boundary layer 60 is expelled from sizing die 40 back into coating chamber 20. The expelled coating fluid forms gyres in coating chamber 20 adjacent to sizing die 40. A gyre is a loop-like localized flow pattern of coating liquid with nearly closed streamlines. As coating liquid recirculates within the gyre during the draw process, shear stresses associated with the flow lead to an increase in the temperature of the coating liquid in the gyre.

The shape of the gyre and distribution of temperatures within the gyre depends on the design of the sizing die. The size and severity of gyres, for example, depends on the degree of constriction in the space available to the coating liquid. For thinner fiber coalings, narrower sizing dies are required and greater constriction occurs. Greater constriction leads to expulsion of a larger amount of coating liquid from the boundary layer as the fiber enters the tapered section of the sizing die and to more pronounced gyre formation.

The shape of the sizing die also influences the position, shape and temperature distribution of a gyre. Figure 2 illustrates a conventional design for a sizing die. The conventional design includes a bell section 90, a taper section 92, and a land section 94. Figure 3 illustrates a cone-only design for a sizing die. The cone-only design lacks a bell section and includes a cone section 96 and a land section 98. Further information on the cone-only design can be found in U.S. Published Patent Application No, 20150147467A1, the disclosure of which is incorporated by reference herein.

Figure 4 shows the calculated shape and temperature profile of a gyre formed adjacent to a sizing die having the conventional design shown in Figure 2. Optical fiber 110 enters a coating chamber section 120 through guide die exit 130 and passes through exit 150 of conventional sizing die 140. The draw speed of optical fiber 110 is 50 m/s. A gyre having outer boundary 160 forms around optical fiber 110. Shading within the gyre indicates the temperature profile that develops in the gyre at steady state. Darker shading corresponds to higher temperature for coating liquid present in the gyre. The temperature scale shown at left indicates temperatures in units of °C. The temperature of coating liquid is highest near optical fiber 110 and decreases away from optical fiber 110. The gyre is surrounded by coating liquid. Boundary 160 of the gyre corresponds to position at which equalization of the temperat ure of coating liquid in the gyre and the temperature of the surrounding coating liquid occurs. For purposes of the calculation, the temperature of the coating liquid surrounding the gyre was set at 60 °C. Figure 4 indicates that the gyre formed by a conventional die is elongated along the process pathway of the fiber and that the spatial extent of the gyre is confined to regions close to the fiber. Figure 4 also indicates that the highest temperatures in the gyre are approximately 80 °C warmer than the temperature of the coating fluid away from the gyre.

Figure 5 shows the calculated shape and temperature profile of a gyre formed adjacent to a sizing die having the cone-only design shown in Figure 3. Optical fiber 210 enters a coating chamber section 220 through guide die exit 230 and passes through exit 250 of cone- only sizing die 240. A gyre having outer boundary 260 forms around optical fiber 210. Shading within the gyre indicates the temperature profile that develops in the gyre at steady state. The temperature scale shown at left indicates temperatures in units of °C, Darker shading corresponds to higher temperature for coating liquid present in the gyre. The temperature of coating liquid is generally higher near optical fiber 210 and decreases away from optical fiber 210 until equalization with the temperature of the surrounding coating liquid occurs at outer boundary 260 of the gyre. For purposes of the calculation, the temperature of the coating liquid surrounding the gyre was set at 60 C. Figure 5 indicates that the gyre formed by a cone-only die is elongated in a direction transverse to the process pathway of the fiber. Relative to the conventional die, the gyre formed by a coneonly die is less lightly confined io spaces close to the fiber. The gyre extends for significant distances in lateral directions away from the process pathway. Figure 5 also indicates that the highest temperatures in the gyre are approximately 70 °C warmer than the temperature of the coating fluid away from the gyre. The extent of heating of coating liquid in the gyre is less for the cone-only sizing die than for the conventional sizing die shown in Figure 4.

The heating of coating liquid that occurs in the gyre is detrimental to the stability of title meniscus and leads to flooding of the guide die. Flooding is a process failure in which coating liquid is forced through the guide die exit into the guide die by the pressure of the coating liquid in the coating chamber. Flooding typically leads to breakage of the fiber, which necessitates process shut down. Flooding becomes more likely due to the presence of gyres because as the coating liquid heats in a gyre, its viscosity decreases. The extent of heating and decrease in viscosity become more pronounced as the draw speed increases because higher draw speeds increase the circulatory flow' rate within the gyre, which leads to greater shear effects and more heating due to viscous dissipation. For draw speeds typical of current manufacturing processes, the temperature increase associated with gyres (~70 °C and higher) is sufficient to reduce the viscosity of the coating liquid by an order of magnitude or more. As draw speed increases above current values, heating and thermal effects associated with gyres become more pronounced.

Heating and a reduction in the viscosity of the coating liquid increase the likelihood of flooding because they (1) make the coating liquid more buoyant than the surrounding coating liquid and (2) reduce the pressure needed to induce back flow of the coating liquid into the guide die. As a result, if warmer, less viscous coating liquid escapes from the gyre and enters the surrounding coating liquid, it tends to flow upward in the coating chamber to the guide die. If the warmer, less viscous coaling liquid reaches the meniscus, it destabilizes the meniscus and leads to dewetting of the fiber. As the fiber dowels, the drag force associated with the liquid boundary layer 5 needed to resist back flow of coating liquid into the guide die is lost and the pressure needed to force the coating liquid up through the guide die exit into the guide die is reduced. Flooding accordingly ensues.

Bubbles in the coaling liquid also promote flooding. The presence of bubbles leads to random, chaotic motion of coating liquid within and around the gyre. The random, chaotic motion 10 facil itates escape of warmer, viscous coating liquid from the gyre and promotes migration of warmer, viscous coating liquid toward the meniscus.

To maintain a stable meniscus and uninterrupted, continuous wetting of the fiber, it is necessary to limit the effects of gyres on the coating process. The present method mitigates deleterious effects of gyres by supplying a transverse flow of coating liquid to the space between 15 the exit of the guide die and the entrance to the sizing die. Transverse flow refers to flow of coating liquid in a direction transverse to the process pathway of the fiber as it passes through the coating chamber. Transverse direction refers to any direction that is not parallel to the process pathway of the fiber. The transverse flow of coating l iquid mixes or interacts with coating fluid in the gyre. In one embodiment, the transverse flow of coating liquid enters a gyre, mixes with coating liquid in 20 the gyre, flows across the gyre, exits the gyre, and removes or otherwise displaces a portion of coating liquid from the gyre. In another embodiment, the transverse flow of coating liquid is directed around the gyre without entering the gyre. In one embodiment, establishing transverse flow includes adding coating liquid from an external source to existing coating liquid in the coating chamber and removing coating liquid from the coating chamber. The removed coating liquid is 25 coating liquid originally present in the coating chamber, coating liquid added to the coating chamber, or a combination thereof. In one embodiment, a transverse flow of coating liquid is supplied to a pressurized coating chamber.

The transverse flow of coating liquid mitigates the effect of the gyre in several ways. First, the temperature of the coating liquid in the transverse flow at its point of entry to the coating 30 chamber can be controlled and maintained at a temperature below the maximum, average or minimum temperature of coating fluid contained in the gyre. When the cooler coating fluid of the transverse flow interacts with the warmer coating fluid of the gyre, the gyre cools. As the gyre cools, the coating liquid in the gyre becomes less buoyant and more viscous. This reduces the likelihood of escape of the coating liquid from the gyre. To the extent that coating liquid does 35 escape from the gyre, the reduced buoyancy lower temperature and higher viscosity lessen the likelihood that coating liquid from the gyre will reach the meniscus. If coating liquid from the gyre does reach the meniscus, the lower temperature and higher viscosity mean that, higher pressure is needed to force it into the guide die. The likelihood of flooding is accordingly reduced. By maintaining a continuous transverse flow of coating liquid and continuously removing coating liquid, the temperature of coating fluid within the gyre can be managed.

Second, the cooling of the coating fluid provided by the transverse flow also reduces temperature gradients in the gyre and the difference between the average temperature of the gyre and the surrounding coating fluid. The greater equalization in temperature leads to a more homogeneous coating liquid with more stable and consistent properties (e.g. gyre flow pattern, density, viscosity). Better homogeneity improves uniformity and concentricity of coating.

Third, displacement and removal of coating liquid in the coating chamber, whether in the gyre or surrounding the gyre, decreases the concentration of bubbles in the coating chamber. The coating fluid of the transverse flow has not been subjected to entrained gases in the coating chamber and enters the coating chamber essentially free of bubbles. Transverse flow of coating fluid thus dilutes the concentration of bubbles in the coating chamber. Removal from the coating chamber of coaling fluid of coating liquid that contains bubbles leads to a reduction in bubble concentration, A lower bubble concentration minimizes the likelihood of dewetting and flooding. A lower bubble concentration also eliminates random, chaotic motion in the gyre, which leads to better concentricity through a more consistent., stabilized flow pattern in the gyre and a reduced tendency for coating fluid io escape from the gyre.

Fourth, replenishment of coating l iquid in the coating chamber lowers the concentration of dissolved gases in the coating fluid. As noted above, gas can enter the coating chamber through entrainment by the fiber as it exits the guide die. Entrainment can lead to dewetting and is undesirable. Gas can enter the coating chamber, however, even when the fiber is properly wetted.

Wetting of the fiber includes formation of a meniscus of coating liquid on the fiber as the fiber enters the coating liquid. As the meniscus forms, the gas boundary layer on the fiber is displaced. The meniscus, however, is exposed to gas from the displaced boundary layer. Common process gases present in the guide die (e.g. air, CO?, He) are soluble in the coating liquids typically used to coat fibers. As the draw process is operated over time, the concentration of gas dissolved in the coating liquid increases and ultimately reaches a saturation level.

Two adverse effects occur when the coating liquid is saturated with gas. First, dissolution of gas into the coating liquid is one of the steps associated with the wetting process. The speed of wetting is related to the permeability of the gas from the gas boundary layer of the fiber into the coating liquid. (See, for example, Jacqmin, D.; Journal of Fluid Mechanics, 455, 347-358 (2002). ) 35 Gas permeability is proportional to solubility and rate of diffusion of the gas in the coating liquid.

If the coating liquid is saturated with gas, further gas is unable to dissolve in the coating liquid and gas from the gas boundary layer of the fiber cannot enter the coating liquid. Dewetting can occur as a result. Second, the inability of gas to dissolve in the coating liquid increases the likelihood of bubble formation in the coating liquid. Dissolution of gas in the coating liquid removes gas that might otherwise form bubbles in the coating liquid. Through dissolution, bubble formation is inhibited. If the coating liquid becomes saturated with gas, however, dissolution is no longer possible and incorporation of gas in the form of bubbles in the coating liquid becomes more prevalent. Replenishment of saturated coating liquid with fresh coating liquid aids wetting and suppresses bubble formation by avoiding saturation and maintaining consistent dissolution of gas into the coating liquid.

Fifth, the reduction in the temperature of coating liquid in the coating chamber increases the solubility of common process gases in the coating liquid. Higher solubility leads to greater dissolution of gases in the coating l iquid and longer times before saturation occurs. This allows for longer operational times before concents about dewetting and bubble entrapment associated with saturation of the coating liquid arise.

Establishing transverse flow of coating liquid includes directing a stream of coating liquid in the space between the exit of the guide die and the entrance of the sizing die. This space defines a channel through which coating liquid flows in a transverse direction. The process pathway is coincident with the optical fiber and extends from the exit of the guide die to the entrance of the sizing die. The transverse flow sweeps across, through, and/or around trie process pathway to mix with, dilute, remove or otherwise interact (thermally or mechanically) with coating liquid present in the coating chamber. The rate of transverse flow is adjusted to counteract detrimental effects of gyres. Greater transverse flow rates are preferred as draw speed increases. In various embodiments, the rate of transverse flow is greater than 0.1 cnr/s, or greater than 0.2 cnr/s, or greater than 0.3 cm7s, or greater than 0.4 cm7s, or greater than 0.5 cm7s, or greater than 0.75 cm7s, or greater than 1.0 cnr’/s, greater than 2.5 cnr/s, or greater than 5.0 cm’/s, or in the range from 0.1 cm’Vs - 20 cm³/s, or in the range from 0.1 cm’/s - 10 cm³/s, or in the range from 0.1 cm’/s - 5.0 cm’/s, or in the range from 0.2 cm’/s - 20 cm’/s, or in the range from 0.2 cnr/s - 10 cm’/s, or in the range from 0.2 cm’/s .- 5.0 cm7s, or in the range from 0.5 cm’/s - 20 cm7s, or in the range from 0.5 cm7s - 10 cm’/s, or in the range from 0.5 cm’/s - 5.0 cm’/s.

Figure 6 depicts a modification of the configuration shown in Figure 4 that includes transverse flow of coating liquid in a channel between guide die exit 130 and sizing die 140. The transverse flow includes introduction 170 of coating liquid and removal 180 of coating liquid from the gyre and/or coating chamber. S imilarly, Figure 7 depicts a modification of the configuration shown in Figure 5 that includes transverse flow of coating liquid in a channel between guide die exit 230 and sizing die 240. The transverse flow includes introduction 270 of coating liquid and removal 280 of coating liquid from the gyre and/or coating chamber. In one embodiment, the transverse flow rate corresponds to the rate of introduction of coating liquid at the inlet to the coating chamber. In another embodiment, the transverse flow rate corresponds to the rate of removal of coating liquid from the coating chamber. In a further embodiment, the transverse flow rate is measured by placing a sensor or flow meter within the coating chamber in the vicinity of the gyre.

In various embodiments, the rate of introduction of coating liquid used to generate the transverse flow is greater than 0.1 cm’/s, or greater than 0.2 cm’/s, or greater than 0,3 cm7s, or greater than 0.4 cm’/s. or greater than 0.5 cm’/s. or greater than 0.75 cm³/s, or greater than 1.0 cnr’/s, greater than 2.5 cm³/s, or greater than 5.0 cm’/s, or in the range from 0.1 cnr’/s - 20 cm’/s, or in the range from 0.1 cm³/s - 10 cm7s, or in the range from 0.1 cm³/s - 5.0 cm³/s, or in the range from 0,2 cnr/s - 20 cm³/», or in the range from 0,2 cnr/s - 10 cnr’/s, or in the range from 0,2 cnr/s 5,0 cm’/s, or in the range from 0.5 cm³/s 20 cm7s, or in the range from 0.5 cm’/s 10 cm’/s, or in the range from 0.5 cm7s - 5.0 cnr’/s.

In various embodiments, the rate of removal of coating liquid from the coating chamber is greater than 0.1 cnr’/s, or greater than 0.2 cnr’/s, or greater than 0.3 cnr’/s, or greater than 0.4 cm’/s, or greater than 0.5 cm’/s, or greater than 0.75 cm’/s, or greater than 1.0 cnr’/s. greater than 2.5 cnr’/s, or greater than 5.0 cm’/s, or in the range from 0,1 cm’/s - 20 cnr’/s, or in the range from 0.1 cnr’/s -10 cm³/s, or in the range from 0.1 cm³/s - 5.0 cnr’/s, or in the range from 0.2 cnr/s - 20 cm’/s, or in the range from 0,2 cnr’/s -10 cm’/s, or in the range from 0,2 απ’/s - 5,0 cm’/s, or in the range from 0.5 cm7s - 20 cm’/s, or in the range from 0.5 cnr’/s - 10 cm’/s, or in the range from 0.5 cm’/s - 5,0 cm’/s.

To accommodate a transverse flow of coating liquid in one embodiment, the coating chamber is adapted to include an inlet for delivering a transverse flow of coating liquid and an outlet for removing the transverse flow of coating liquid. The inlet and outlet are distinct from the entrance and exit points of the fiber into the coating chamber, Figure 8 shows an embodiment of a coating chamber that includes an inlet for supplying coating liquid 282 to the coating chamber from an external source and an outlet for removing coating liquid 290 from the coating chamber.

The flow' of the coating liquid is depicted with gray arrows in Figure 8. The coating liquid flows from the inlet 282 into the coating chamber and in a transverse direction in a channel between the guide die 284 and the sizing die 286 past the optical fiber 299. The coating liquid in the transverse flow exits the channel and is removed from the coating chamber at the outlet 290, The inlet 282 for supplying coating liquid from an external source is distinct from the point of entry of the optical fiber 288 to the coating chamber (guide die 284 exit). The outlet 240 for removing coating liquid from the coating chamber is distinct from the points of entry and exit of the optical fiber 288 from the sizing die 286. At steady state, the amount of coating liquid removed at. the outlet 290 is approximately equal to the amount of coating liquid supplied at the inlet 282. An exact balancing of the amounts of coating liquid at the inlet 282 and outlet 290 does not occur due to removal of coating liquid in the form of a thin layer on the optical fiber 288 at the sizing die 286 and, if present, leakage of coating liquid into the guide die 284.

In Figs. 4 and 5, the gyre occupies a substantial portion of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber.

Consequently, as shown in Figure 8, to promote mitigation of the effects of the gyre on wetting of the fiber, it is preferable for the coating liquid in the transverse flow to interact with a significant portion of the gyre. In Figure 8, the fiber entrance to the coating chamber corresponds to the exit of a guide die and the fiber exit from the coating chamber corresponds to the entrance to the sizing die. In one embodiment, interaction of the transverse flow with the gyre is determined by the overlap of the cross-section of transverse flow with the gyre. The transverse flow is characterized by a cross-section in a plane normal to the direction of transverse flow. The crosssection is a two-dimensional area defined by a perimeter having a shape and size. The shape and size of the perimeter are influenced by factors including the shape and size of the inlet that suppl ies the transverse flow to the coating chamber and the dimensions of the channel between the guide die and sizing die through which the transverse flow passes. In various embodiments, the shape of the perimeter is circular, elliptical, square, rectangular, or irregular. The size of the perimeter is characterized by a cross-sectional dimension. The cross-sectional dimension corresponds to the longest, line segment that connects two points of the perimeter of the cross-section. For example, when the shape of the perimeter is circular, the cross-sectional dimension is diameter. When the shape of the perimeter is square or rectangular, the cross-sectional dimension is the diagonal length. When the shape of the perimeter is elliptical, the cross-sectional dimension is the length of the major axis of the ellipse.

To increase the interaction of the transverse flow of coating liquid with the gyre, the crosssectional dimension of the transverse flow of coating liquid is greater than 30% of the distance between the exit of the guide die and the entrance of the sizing die, or greater than 40% of the distance between the exit of the guide die and the entrance of the sizing die, or greater than 50% of the distance between the exi t of the guide die and the entrance of the sizing die, or greater than 70% of the distance between the exit of the guide die and the entrance of the sizing die, or greater than 90% of the distance between the exit of the guide die and the entrance of the sizing die, or in the range from 30% - 100% of the distance between the exit of the guide die and the entrance of the sizing die, or in the range from 50% - 100% of the distance between the exit of the guide die and the entrance of the sizing die, or in the range from 70% 100% of the distance between the exit of the guide die and the entrance of the sizing die, or in the range from 30% - 90% of the distance between the exit of the guide die and the entrance of the sizing die.

In other embodiments, the cross-sectional dimension of the transverse flow of coating liquid is greater than 30% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or greater than 40% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or greater than 50% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or greater than 70% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or greater than 90% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or in the range from 30% - 100% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or in the range from 50% - 100% of the distance between fiber entrance to the coating chamber and the fiber exit from the coating chamber, or in the range from 70% 100% of the distance between fiber entrance to the coating chamber and the fiber exit from the coating chamber, or in the range from 30% - 90% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber.

In one embodiment, the cross-sectional dimension of the transverse flow of coating liquid is controlled by the dimensions of the inlet that supplies the transverse flow of coating liquid to the coating chamber. The inlet includes an opening at the interface with the coating chamber through which the transverse flow of coating liquid is supplied. The inlet has a cross-sectional area determined by the size and shape of the opening and is characterized by a cross-sectional di mension. The cross-sectional dimension of the inlet corresponds to the longest line segment that connects two points of the perimeter of the opening.

In different embodiments, the cross-sectional dimension of the inlet is greater than 30% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or greater than 40% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or greater than 50% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or greater than 70% of the distance between the fiber entrance to the coating chamber and the fiber exit, from the coating chamber, or greater than 90% of' the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or i n the range from 30% - 100% of the distance between the fiber entrance to the coating chamber and the fiber exit from the coating chamber, or in the range from 50% - 100% of the distance between fiber entrance to the coating chamber and the fiber exit from the coating chamber, or in the range from 70% - 100% of the distance between liber entrance to the coating chamber and the liber exi t from the coating chamber, or in the range from 30% - 90% of the distance between the fiber entrance to the coating chamber and the liber exit from the coating chamber.

In different embodiments, the cross-sectional dimension of the inlet is greater than 30% of the distance between the exit of the guide die and the entrance of the sizing die, or greater than 40% of the distance between the exit of the guide die and the entrance of the sizing die, or greater than 50% of the distance between the exit, of the guide die and the entrance of the sizing die, or greater than 70% of the distance between the exit of the guide die and the entrance of the sizing die, or greater than 90% of the distance between the exit of the guide die and the entrance of the sizing die, or in the range from 30% 100% of the distance between the exit of the guide die and the entrance of the sizing die, or in the range from 50% - 100% of the distance between the exit of the guide die and the entrance of the sizing die, or in the range from 70% - 100% of the distance between the exit of the guide die and the entrance of the sizing die, or in the range from 30% - 90% of the distance between the exit of the guide die and the entrance of the sizing die.

The temperature and/or flow rate of coating liquid supplied at the inlet can be controlled to manage the thermal environment of coaling liquid in the coating chamber or in the gyre. The temperature of coating liquid supplied at the inlet is less than the maximum temperature of coating liquid in the gyre, or less than the average temperature of coating liquid in the gyre, or less than the minimum temperature of coating liquid in the gyre, or less than the average temperature of the coating liquid in the coating chamber that is outside of the gyre.

Management of the thermal environment of the coating liquid includes minimizing the difference in temperature of coating liquid within the gyre. By including transverse flow of coating liquid in the channel between the guide die and sizing die, the difference between the maximum temperature of coating fluid in the gyre and the minimum temperature of coating fluid in the gyre is less than 80 °C, or less than 60 °C, or less than 50 °C, or less than 40 °C, or less than 30 °C.

In different embodiments, the temperature of coating liquid supplied at the inlet of the coating chamber is less than the average temperature of coating fluid in the gyre by at least 5 °C, at least 10 °C, or at least 20 °C, or at least 30 °C. or by an amount in the range from 5 °C - 40 °C, or by an amount in the range from 10 °C - 30 °C.

Management of the thermal environment of the coating liquid includes minimizing the difference in the temperatures of coating liquid in the gyre and i n the coating liquid surrounding the gyre. By including transverse flow of coating liquid in the channel between the guide die and the sizing die, the difference between the maximum temperature of coating fluid in the gyre and the temperature of coating fluid surrounding the gyre is less than 80 °C, or less than 60 °C, or less than 50 °C, or less than 40 °C. or less than 30 °C.

A coating assembly featuring transverse flow of coating liquid in accordance with the present description is utilized in the application of one or more coatings to the optical fiber, A typical optical fiber includes a low modulus primary coating on the glass fiber and a high modulus secondary coating on the primary coating, A coloring layer is often formed on the secondary coating as well. The benefits associated with transverse flow of coating liquid extend to any of the coatings formed on an optical fiber. When applying multiple coatings to the fiber, a liquid primary coating composition is applied to the fiber at a point along the process pathway upstream of the point at which a liquid secondary coating composition is applied to the fiber. In one embodiment, the liquid primary coating composition is cured before applying the liquid secondary coating composition ('wet-on- dry process). In another embodiment, the liquid primary coating composition is uncured before applying the liquid secondary coating composition (wet-on-wet process). If applied, the liquid coloring layer composition is applied at a position along the process pathway downstream from the point of application of the liquid secondary coating composition. In one embodiment, the liquid secondary coating composition is cured .before applying the liquid coloring layer composition (wet-on-dry process). In another embodiment, the liquid secondary coating composition is uncured before applying the liquid coloring layer composition (wet-on-wet process).

Figure 9 illustrates an embodiment in which primary and secondary coating liquids are applied to an optical fiber in a wet-on-wet process. Coating unit. 300 is used to apply a liquid primary coating composition to optical fiber 305. Optical fiber 305 is drawn in the direction A indicated at a particular draw speed. Optical fiber 305 is drawn through guide die 310 into coating chamber 315, drawn through coating chamber 315 to sizing die 320, and drawn through sizing die 320 to downstream coating unit 325. A primary coating liquid is applied to optical fiber 305 in coating chamber 315. Primary coating liquid is supplied to coating chamber 315 at inlet 330 and removed from coating chamber 315 at outlet 335. The primary coating liquid flows in transverse directions 340 and 345 in coating chamber 315. Optical fiber 305 enters coating unit 325 at. guide die 350, is drawn through guide die 350 to coating chamber 355, is drawn through coating chamber 355 to sizing die 360, and drawn through sizing die 360 to downstream processing units (not shown). A secondary coating liquid is applied to optical fiber 305 in coating chamber 355.

Secondary coating liquid is supplied to coating chamber 355 at inlet 365 and removed from coating chamber 355 at outlet 370. The secondary coating liquid flows in transverse directions 375 and 380 in coating chamber 355. Although transverse flow of coating liquid is depicted as occurring in the same or similar transverse directions in coating chambers 315 and 355, it is understood that transverse flow of coating liquid can occur in different, directions in coating chambers 315 and 355.

Figure 10 illustrates another embodiment in which primary and secondary coating liquids are applied to an optical fiber in a wet-on-wet process. Coating unit. 400 is used to apply liquid primary and secondary coating compositions to optical fiber 405. Optical fiber 405 is drawn in the direction B indicated at a particular draw speed. Optical fiber 405 is drawn through guide die 410 into coating chamber 415, drawn through coating chamber 415 to hybrid die 420, drawn through hybrid die 420 to coating chamber 425, drawn through coating chamber 425 to sizing die 430, and drawn through sizing die 430 to downstream process units (not shown). Hybrid die 420 acts as a sizing die for optical fiber 405 as it exits coating chamber 415 and a guide die for optical fiber 405 as it enters coating chamber 425, A primary coating liquid is applied to optical fiber 405 in coating chamber 415. Primary coating liquid is supplied to coating chamber 415 at inlet 435 and removed from coating chamber 415 at. outlet 440. The primary coating liquid flows in transverse directions 445 and 450 in coating chamber 415. Optical fiber 405 enters coating chamber 425 through hybrid die at 420. A secondary coating liquid is applied to optical fiber 405 in coating chamber 425. Secondary coating liquid is supplied to coating chamber 425 at inlet 455 and removed from coating chamber 425 at outlet 460. The secondary coating liquid flows in transverse directions 465 and 470 in coating chamber 425. Although transverse flow of coating liquid is depicted as occurring in the same or similar transverse directions in coating chambers 415 and 425, it is understood that transverse flow of coating liquid can occur in different directions in coating chambers 415 and 425.

In another embodiment., coating liquid removed from the coating chamber is recycled to the coating chamber. Coating liquid removed from the coaling chamber is directed to a return loop that delivers the removed coating liquid directly to the coating chamber or to an external source of coating liquid operatively coupled to an inlet of the coating chamber.

In a preferred embodiment, the guide die is free of coating liquid. In another preferred embodiment, flooding of the guide die does not occur. In a further preferred embodiment, coating 25 liquid associated with the transverse flow does not enter the guide die.

Preferred coating liquids are curable coating liquids. Curable coating liquids include one or more curable components. As used herein, the term “curable is intended to mean that the component, when exposed to a suitable source of curing energy, includes one or more curable functional groups capable of forming covalent bonds that participate in linking (bonding) the component to itself or to other components to form a polymeric coating material. The cured product obtained by curing a curable coating liquid is a coating. The curing process is induced by any of several forms of energy. Forms of energy include radiation or thermal energy. A radiationcurable component is a component that is induced to undergo a curing reaction when exposed to radiation of a suitable wavelength at a suitable intensity for a sufficient period of time. The radiation curing reaction preferably occurs in the presence of a photoinitiator. A radiation-curable component is optionally also thermally curable. Similarly, a thermally-curable component is a component that is induced to undergo a curing reaction when exposed to thermal energy of sufficient intensity for a sufficient period of lime. A thermally curable component is optionally also radiation curable. Curable components include monomers, oligomers, and polymers.

A curable component includes one or more curable functional groups, A curable component with only one curable functional group is a monofunctional curable component. A curable component having two or more curable functional groups is a multifunctional curable component. Multifunctional curable components include two or more functional groups capable of forming covalent bonds during the curing process and can introduce crosslinks into the polymeric network formed during the curing process. Multifunctional curable components are also referred to as “crosslinkers” or “curable crosslinkers”. Examples of functional groups that participate in covalent bond formation during the curing process are identified below.

The coating composition includes a single monomer or a combination of monomers. The monomers include ethylenically-unsaturated compounds, ethoxylated acrylates, ethoxylated alkylphenol monoacrylates, propylene oxide acrylates, n-propylene oxide acrylates, isopropylene oxide acrylates, monofunctional acrylates, monofunctional aliphatic epoxy acrylates, multifunctional acrylates, multifunctional aliphatic epoxy acrylates, and combinations thereof.

In one embodiment, the monomer component of the curable coating liquid includes ethylenically unsaturated monomers. The monomers include functional groups that are polymerizable groups and/or groups that facilitate or enable crosslinking. The monomers are monofunctional monomers or polyfunctional monomers. In combinations of two or more monomers, the constituent monomers are monofunctional monomers, polyfunctional monomers, or a combination of monofunctional monomers and polyfunctional monomers. Suitable functional groups for ethylenically unsaturated monomers include, without limitation, ('meth)acrylates, acrylamides, A-vinyl amides, styrenes, vinyl ethers, vinyl esters, acid esters, and combinations thereof.

Exemplary monofunctional ethylenically unsaturated monomers for the curable coating liquid include, without limitation, hydroxyalkyl acrylates such as 2-hydroxyethyl-acrylate, 2hydroxypropyl-acrylate, and 2-hydroxybutyl-acrylate; long- and short-chain alkyl acrylates such as methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, butyl acrylate, amyl acrylate, isobutyl acrylate, r-butyl acrylate, pentyl acrylate, isoamyl acrylate, hexyl acrylate, heptyl acrylate, octyl acrylate, isooctyl acrylate, 2-ethylhexyl acrylate, nonyl acrylate, decyl acrylate, isodecyl acrylate, undecyl acrylate, dodecyl acrylate, lauryl acrylate, octadecyl acrylate, and stearyl acrylate; aminoalkyl acrylates such as dimethylaminoethyl acrylate, diethylaminoethyl acrylate, and 7-amino~3,7~dimethvloctyl acrylate; alkoxyalkvl acrylates such as butoxvethyl acrylate, phenoxyethyl acrylate (e.g., SR339. Sartomer Company, Inc.), and ethoxyethoxyethyl acrylate; single and multi-ring cyclic aromatic or non-aromatic acrylates such as cyclohexyl acrylate, benzyl acrylate, dicyclopentadiene acrylate, dicyclopentanyl acrylate, tricyclodecanyl acrylate, bomyl acrylate, isobomyl acrylate (e.g., SR423, Sartomer Company, Inc.), tetrahydrofiurfuryl acrylate (e.g,, SR285, Sartomer Company, Inc,), caprolactone acrylate (e.g., SR495, Sartomer Company,

Inc.), and acryloylmorpholine; alcohol -based acrylates such as polyethylene glycol monoacrylate, polypropylene glycol monoacrylate, methoxyethylene glycol acrylate, methoxypolypropylene glycol acrylate, methoxypolyethylene glycol acrylate, ethoxydieihylene glycol acrylate, and various alkoxylated alkylphenol acrylates such as ethoxylated (4) nonylphenol acrylate (e.g.,

Photomer 4066, IGM Resins); acrylamides such as diacetone acrylamide, isobutoxy methyl acrylamide, AW-dimethyl-aminopropyl acrylamide, (V./V-dimethyl acrylamide, diethyl acrylamide, and r-octyl acrylamide; vinylic compounds such as ΛΓ-vinylpyrrolidone and N~ vinyl caprolactam; and acid esters such as maleic acid ester and fumaric acid ester. With respect to tiie long and short chain alkyl acrylates listed above, a short chain alkyl acrylate is an alkyl group 15 with 6 or less carbons and a long chain alkyl acrylate is an alkyl group with 7 or more carbons.

Representative radiation-curable ethylenically unsaturated monomers include alkoxylated monomers with one or more acrylate or methacrylate groups. An alkoxylated monomer is one that includes one or more alkoxylene groups, where an alkoxylene group has the form OR- and R is a linear or branched hydrocarbon. Examples of alkoxylene groups include ethoxylene (-O-CHb-CH,20 ), π-propoxylene (-O-CH₂-CH₂-CH₂-), isopropoxylene (-O-CH₂~CH(CH₃)-), etc. As used herein, the degree of alkoxylation refers to the number of alkoxylene groups in the monomer. In one embodiment, the alkoxylene groups are bonded consecutively in the monomer.

Representative polyfunctional ethylenically unsaturated monomers for the curable coating liquid include, without limitation, alkoxylated bisphenol A diacrylates, such as ethoxylated 25 bisphenol A diacrylate, with the degree of alkoxylation being 2 or greater. The monomer component of the secondary composition may include ethoxylated bisphenol A diacrylate with a degree of ethoxylation ranging from 2 to about 30 (e.g. SR349 and SR601 available from Sartomer Company, Inc. West Chester, Pa. and Photomer 4025 and Photomer 4028, available from IGM Resins), or propoxylated bisphenol A di acrylate with the degree of propoxy lation being 2 or 30 greater; for example, ranging from 2 to about 30; methylolpropane polyacrylates with and without alkoxylation such as ethoxylated tri methylolpropane triacrylate with the degree of ethoxy lation being 3 or greater; for example, ranging from 3 to about 30 (e.g., Photomer 4149, IGM Resins, and SR499, Sartomer Company, Inc.); propoxylated-trimethylolpropane triacrylate with the degree of propoxylation being 3 or greater; for example, ranging from 3 to 30 (e.g., Photomer 4072, IGM 35 Resins and SR492, Sartomer); ditrimethylolpropane tetraacrylate (e.g., Photomer 4355, IGM

Resins); alkoxylated glyceryl triacrylates such as propoxylated glyceryl triacrylate with the degree of propoxy I ation being 3 or greater (e.g., Photomer 4096,IGM Resins and SR9020, Sartomer); erythritol polyacrylates with and without alkoxylation, such as pentaerythritol letraacrylate (e.g., SR295, available from Sartomer Company, Inc. (West Chester, Pa.)), ethoxylated pentaerythritol tetraacrylate (e.g., SR494, Sartomer Company, Inc.), and dipentaerytbritol pentaacrylate (e.g., Photomer 4399,IGM Resins, and SR399, Sartomer Company, Inc.)· isocyanurate polyacrylates formed by reacting an appropriate functional isocyanurate with an aery lie acid or acryloyl chloride, such as tris-(2~hydroxyethyl) isocyanurate triacrylate (e.g., SR368, Sartomer Company, Inc. ) and tris-Q-hydroxyethyl) isocyanurate diacrylate; alcohol polyacrylates with and without alkoxylation such as tricyclodecane dimethanol diacrylate (e.g., CD406, Sartomer Company, Inc.) and ethoxylated polyethylene glycol diacrylate with the degree of ethoxylation being 2 or greater; for example, ranging from about 2 to 30; epoxy acrylates formed by adding acrylate to bisphenol A diglycidylether and the like (e.g., Photomer 3016, IGM Resins); and single and multi-ring cyclic aromatic or non-aromatic polyacrylates such as dicyclopentadiene diacrylate and dicyclopentane diacrylate.

In embodiments, the monomer component of the coating liquid includes compounds having the general formula R₂- R₍ -O - (( IFCIECH -O)_;;- COCIfoCIE, where R; and R, are aliphatic, aromatic, or a mixture of both, and q~ 1 to 10, or R; O -(CH2CH3CH 0),,- COCH=CHj, where R₍ is aliphatic or aromatic, and q~l to 10, Representative examples include ethylenically unsaturated monomers such as lauryl acrylate (e.g., SR335 available from Sartomer Company, Inc., AGEFLEX FA12 available from BASF, and PHOTOMER 4812 available from IGM Resins), ethoxylated nonylphenol acrylate (e.g., SR504 available from Sartomer Company, Inc. and PHOTOMER 4066 available from IGM Resins), caprolactone acrylate (e.g,, SR495 available from Sartomer Company, Inc., and TONE M-100 available from Dow Chemical), phenoxyethyl acrylate (e.g., SR339 available from Sartomer Company, Inc., AGEFLEX PEA available from BASF, and

PHOTOMER 4035 available from IGM Resins), isooctyl acrylate (e.g., SR440 available from Sartomer Company, Inc. and AGEFLEX FAS available from BASF), tridecyl acrylate (e.g., SR489 available from Sartomer Company, Inc.), isobornyl acrylate (e.g., SR506 available from Sartomer Company, Inc. and AGEFLEX IBOA available from CPS Chemical Co.), tetrahydrofurfuryl acrylate (e.g., SR285 available from Sartomer Company, Inc.), stearyl acrylate (e.g., SR257 available from Sartomer Company, Inc.), isodecyl acrylate (e.g., SR395 available from Sartomer Company, Inc. and AGEFLEX FA 10 available from B ASF), 2-(2-ethoxyethoxy)ethyl acrylate (e.g., SR256 available from Sartomer Company, Inc.), epoxy acrylate (e.g.. CN120, available from Sartomer Company, and EBECRYL 3201 and 3604, available from Cytec Industries Inc.), lauryloxyglycidyl acrylate (e.g., CN130 available from Sartomer Company) and phenoxyglycidyl acrylate (e.g., CN131 available from Sartomer Company) and combinations thereof.

In some embodiments, the monomer component of the coating liquid includes a multifunctional (meih)acrylate. As used herein, the term “(meth)acrylate” means acrylate or methacrylate. Multifunctional (meth)acrylates are (meth)acrylates having two or more polymerizable (meth)acrylate moieties per molecule, or three or more polymerizable (meth)acrylate moieties per molecule. Examples of multifunctional (meth)acrylates include dipentaerythritol monohydroxy pentaacrylate (e.g., PHOTOMER 4399 available from IGM Resins); methylol propane polyacrylates with and without alkoxylation such as trimethylolpropane triacrylate, ditrimethylolpropane tetraacrylate (e.g., PHOTOMER 4355, IGM Resins); alkoxylated glyceryl triacrylates such as propoxylated glyceryl triacrylate with propoxy! ation being 3 or greater (e.g., PHOTOMER 4096, IGM Resins); and erythritol polyacrylates with and without alkoxylation, such as pentaerythritol tetraacrylate (e.g., SR295, available from Sartomer Company, Inc. (Westchester, Pa.)), ethoxylated pentaerythritol tetraacrylate (e.g., SR494, Sartomer Company, Inc.), dipentaerythritol pentaacrylate (e.g., PHOTOMER 4399, IGM Resins, and SR399, Sartomer Company, Inc.), tripropyleneglycol di(meth)acrylate, propoxylated hexanediol di(meth)acrylate, tetrapropyleneglycol di(meth)acrylate, pentapropyleneglycol di(meth)acrylate.

In an embodiment, the monomer component of the coating liquid includes an A-vinyl amide such as an .(V-vinyl lactam, or W vinyl pyrrolidinone, or /V-vinyl caprolactam.

The curable coating liquid optionally includes one or more oligomers. One class of optional oligomers is etbylenically unsaturated oligomers. Suitable optional oligomers include monofunctional oligomers, polyfunctional oligomers, or a combination of a monofunctional oligomer and a polyfunctional oligomer. In some embodiments, the optional oligomer includes aliphatic and aromatic urethane ('meth)acrylate oligomers, urea ('meth)acrylate oligomers, polyester and polyether (meth)acrylate oligomers, acrylated acrylic oligomers, polybutadiene (meth/acrylate oligomers, polycarbonate (meth) aery late oligomers, and melamine (meth)acrylate oligomers or combinations thereof. The curable coating liquid may be free of urethane groups, groups that react to form urethane groups, urethane acrylate compounds, urethane oligomers, or urethane acry late oligomers.

The polymerization initiator facilitates initiation of the polymerization process associated with the curing of the coating composition to form the coating. Polymerization initiators include thermal initiators, chemical initiators, electron beam initiators, and photoinitiators. Photoinitiators include ketonic photoinitiating additives and/or phosphine oxide additives. When used in the photoformation of the coating of the present disclosure, the photoinitiator is present in an amount sufficient to enable rapid radiation curing. The wavelength of curing radiation is infrared, visible, or ultraviolet.

Representative photoinitiators include 1 -hydroxycyclohexylphenyl ketone (e.g., IRGACURE 184 available from BASF)); bis(2,6-dimethoxybenzoy1)-2,4,45 trimethyl pentylphosphine oxide (e.g., commercial blends IRGACURE 1800, 1850, and 1700 available from BASF); 2,2-dimethoxy-2-phenylaeetophenone (e.g., IRGACURE 651, available from BASF); bis(2,4,6-trimethylbenzoyl)-phenylphosphine oxide (IRGACURE 819); (2,4,6trimethylbenzoyl)diphenyl phosphine oxide (LUCIRIN TPO, available from BASF (Munich, Germany)); etboxy(2,4,6-trimethylbenzoyl)-phenylpbosphine oxide (LUCIRIN TPO-L from

BASF); (2,4,6-triiethylbenzoyl)diphenyl phosphine oxide (e.g., in commercial blend Darocur 4265, BASF); 2-hydroxy-2-methyl-l-phenylpropane-1-one (e.g., in commercial blend Darocur 4265, BASF) and combinations thereof.

In addition to monomer(s), oligomer(s) and/or oligomeric material(s), and polymerization initiator(s), the coating composition optionally includes one or more additives. Additives include 15 an adhesion promoter, a strength additive, an antioxidant, a catalyst, a stabilizer, an optical brightener, a property-enhancing additive, an amine synergist, a wax, a lubricant, and/or a slip agent.

Embodiments of the present method include curing the coating liquid on the optical fiber. In one embodiment, the curable coating liquid is cured with an LED or laser source. In one embodimen t, the LED source is a UVLED source. The peak wavelength of the LED or laser source is a wavelength less than 410 nm, or less than 405 nm, or less than 400 nm, or less than 395 nm, or in the range from 340 nm - 410 nm, or in the range from 350 nm - 405 nm, or in the range from 360 nm - 405 nm, or in the range from 365 nm - 400 nm, or in the range from 370 nm - 395 nm, or in the range from 375 nm - 390 nm, or in the range from 375 nm - 400 nm, or in the range from

380 nm - 400 nm.

Representative radiation-curable ethylenically unsaturated monomers included alkoxylated monomers with one or more acrylate or methacrylate groups. An alkoxylated monomer is one that includes one or more alkoxylene groups, where an alkoxylene group has the form (- O-R - and R is a linear or branched hydrocarbon. Examples of alkoxylene groups include ethoxylene (-O-CH230 CH_r), rt-propoxylene (- O - CH₃ - CH₃ - CH₃ -), isopropoxylene (- O- CH₃ - CH( Cl L) -), etc. As used herein, the degree of alkoxylation refers to the number of alkoxylene groups in the monomer. In one embodiment, the alkoxylene groups are bonded consecutively in the monomer, cf, ID27449 for description of secondary coating.

Unless otherwise expressly stated, it is in no way intended that any method set forth herein be construed as requiring that its steps be performed in a specific order. Accordingly, where a method claim does not actually recite an order to be followed by its steps or it is not otherwise specifically stated in the claims or description that the steps are to be limited to a specific order, it is no way intended that any particular order be inferred.

It will be apparent to those skilled in the art that various modifications and variations can be 5 nuide without departing from the spirit or scope of the illustrated embodiments. Since modifications, combinations, sub-combinations and variations of the disclosed embodiments that incorporate the spirit and substance of the illustrated embodiments may occur to persons skilled in the art, the description should be construed to include everything within the scope of the appended claims and their equivalents.

Claims

CLAUSES

1. A method of processing optical fiber, including the steps of:

drawing an optical fiber in a drawing direction along a process pathway through a coating chamber including coating liquid in order to coat the optical fiber, and directing a separate flow or stream or coating liquid through the coating chamber in a direction transverse to the direction of the drawing direction of the optical fiber through the coating chamber, which transverse flow or coating liquid sweeps across, through and / or around the process pathway in the drawing direction to mix with, dilute, or otherwise interact thermally or mechanically with the coating liquid comprised in the coating chamber,

2. The method according to clause 1, where the coating chamber is pressurized,

3. The method according to clause 1 or 2, the optical fiber enters the coating chamber through a guide die.

4. The method according to any of the preceding clauses, the optical fiber is drawn through the coating chamber to a sizing that.

5. The method according to any of the preceding clauses, the liquid flowing in a direction transverse to the drawing direction of the optical fiber through the coating chamber, is directed through a transverse directing channel positioned in the coating chamber between the guide that and the sizing that.

6. The method according to any of the preceding clause 3-5, said said guide that comprises a bell section, a taper section, and a land section, or said said guide that comprises a cone-only who, said cone-only who including a cone section and a land section, said cone-only that lacking a bell section.

7. The method according to any of the preceding clauses, the optical fiber is drawn at a draw speed or at least 30 m / s, for example said said draw speed is at least 40 m / s, preferably said said draw speed is at least 50 m / s, more preferably said said draw speed is in the range from 40 m / s - 80 m / s.

8. The method according to any of the preceding clauses further comprising curing the coating liquid after the optical fiber exits the sizing, preferably said said curing is accomplished with an LED source.

9. The method according to any of the preceding clauses concerning the coating liquid comprises one or more of the following:

a radiation-curable compound, an ethylenically unsaturated compound, an acrylate or methacrylate compound,

10. The method according to any of the preceding clauses 2-9, said said pressurized coaling chamber has a pressure selected from the following:

greater than 1.01 bar (Opsig), at least 1.02 bar (0.10 psig.).

at least 1.08 bar (1.0 psig), at least 1.36 bar (5.0 psig), at least 1.70 bar (10 psig), in the range from 1.02 bar 21.70 bar (0.10 psig 300 psig), in the range from 1.08 bar - 16.53 bar (1.0 psig - 225 psig), in the range from 1.36 bar - 14.80 bar (5.0 psig - 200 psig).

11. The method according to any of the preceding clauses, the transverse flow or coating liquid is directed against a gyre including the coating liquid, which gyre is formed in the coating chamber around the optical fiber.

12. The method according to clause 11, the difference between a maximum temperature of the coating liquid in the gyre and a minimum temperature of the coating liquid in the gyre is less than 80 ° C, preferably less than 60 ° C.

13. The method according to any of the preceding clauses 4-12, said said sizing that includes a cone-only that, said cone-only that included a cone section and a land section, said cone-only that lacking a bell section.

14. The method according to any of the preceding clauses 12 or 13, the transverse flowing coating liquid mixes with the coating liquid of the gyre.

15. The method according to any of the preceding clauses, where the transverse flowing coating liquid is flowed in the transverse direction at a rate selected from the following:

greater than 0.1 cm '/ s, greater than 0.2 cm' / s, greater than 0.5 cm '/ s, in the range from 0.1 cm' / s 20 cm '/ s, in the range from 0.2 cm '/ s - 20 cm' / s, in the range from 0.5 cm '/ s - 20 cm' / s.

16. The method according to any of the preceding clauses, the separate transverse flow or coating liquid has been introduced into the coating chamber at an inlet configured therefor.

17. The method according to clause 16, liquid coating has been removed from the coating chamber at an outlet configured therefor, said outlet being spaced apart from said guide die and said sizing die.

18. The method according to clause 17, where an approximately equal amount or coating liquid is removed at the outlet from the coating chamber as suppl everybody at the inlet or the coating chamber.

19. The method according to any of the clauses 16-18 the coating fluid supplied at the inlet has a temperature less than the average temperature of the coating liquid in the gyre, preferably the temperature of the coating fluid at the inlet is less than the average temperature of the firs coating liquid in the gyre by at least 5 ° C,

20. The method according to clause 18 or 19, further including returning the coating liquid removed at the outlet to the coating chamber.

21. The method according to any of the clauses 16-20, the coating liquid is introduced at the inlet and / or removed from the outlet at a rate selected fr one or more of the following:

greater than 0.1 cm7s, greater than 0.2 cm '/ s, greater than 0.5 cm' / s, or in the range from 0.1 cm '/ s - 20 cm ³ / s.

22. The method according to any of the preceding clauses, further including drawing the optical fiber, through a second coating chamber including a second coating liquid, and preferably subjecting the optical fiber to the same processing in the second coating chamber as in the first coating chamber,

23. The method according to any of the preceding clauses 3-22, said said guide that is free or said coating liquid.

24. A coated optical fiber, available according to the method according to one or more of the foregoing clauses.

25. A system for processing an optical fiber, including:

one or more coating chambers for holding coating liquid for coating an optical fiber, the coating chamber including a fiber entrance and a fiber exit, an inlet for delivering a stream or flow of coating liquid into the coating chamber, and an outlet for removing coating liquid from the coating chamber, which inlet and outlet are distinct from the fiber entrance and fiber exit, which inlet is configured to deliver the flow or stream or in a direction transverse to a drawing direction of the optical fiber through the coating chamber.

26. The system of clause 25, where the outlet is configured for removing the transverse flow or stream or coating liquid from the coating chamber,

27. The system according to clauses 25 or 26, further comprising a guide associated with a first side of the coating chamber for guiding the optical fiber into the coating chamber and a sizing that, associated with a second opposite side of the coating chamber, through which sizing that coated cable is drawn out of the coating chamber.

28. The system according to any of the clauses 25-28, further including a second coating chamber.

29. The system according to clause 28, the sizing that also functions as a guide for the second coating chamber.

30. The system according to any of clauses 25-29, where the cross-sectional dimension of the inlet is greater than 30% or the distance between the fiber entrance and the fiber exit, preferably greater than 50% or the distance between the fiber entrance and the fiber exit, more preferably greater than 70% of the distance between the fiber entrance and the fiber exit, most preferably for

5 the range from 30% -100% or the distance between the fiber entrance and the fiber exit.

CONCLUSIONS

A method for processing an optical fiber, comprising the steps of:

drawing an optical fiber in a draw direction along a process path through a coating chamber comprising coating liquid to thereby coat the optical fiber, and directing a separate stream or run of the coating liquid through the coating chamber in a direction transverse to the direction of the draw direction of the optical fiber through the coating chamber, which transverse flow of coating liquid moves along, through and / or around the process path in the draw direction to mix with, dilute, or otherwise thermally or mechanically interact with the coating liquid contained in the coating chamber,

The method of claim 1, wherein the coating chamber is pressurized.

The method of claim 1 or 2, wherein the optical fiber enters the coating chamber through a guide die.

A method according to any one of the preceding claims, wherein the optical fiber has been drawn through the coating chamber to a calibration matrix.

The method of any one of the preceding claims, wherein the coating fluid flows in a direction transverse to the draw direction of the optical fiber through the coating chamber, which is controlled through a transversely directed channel positioned in the coating chamber between the guide mold and the calibration mold.

The method of any one of claims 3-5, wherein the guide mold comprising a bubble section, a tapered section, and a land section, or wherein the guide mold comprises only a conical mold, the conical mold comprising a conical section and a land section, wherein the conical mold lacking a bubble section,

A method according to any one of the preceding claims, wherein the optical fiber is drawn at a draw speed of at least 30 m / s, for example wherein the draw speed is at least 40 m / s, preferably wherein the draw speed is at least 50 m / s is more preferably wherein the draw speed is in the range of 40 m / s - 80 m / s.

A method according to any one of the preceding claims, further comprising after-treatment of the coating liquid after the optical fiber leaves the calibration die, preferably wherein the after-treatment is done with an LED source.

The method of any one of the preceding claims, wherein the coating fluid comprising one or more of the following:

a radiation-curing compound, an ethylene-like unsaturated compound, an acrylate or a methacrylate compound,

The method of any one of claims 2-9, wherein the pressurized coating chamber has a pressure selected from the following:

greater than 1.01 bar (0 psig), at least 1.02 bar (0.10 psig), at least 1.08 bar (1.0 psig), at least 1.36 bar (5.0 psig), at least 1.70 bar (10 psig), in the range is 1.02 bar 21.70 bar (0.10 psig 300 psig), in the range of 1.08 bar - 16.53 bar ('1.0 psig - 225 psig), in the range of 1.36 bar -14.80 bar (5.0 psig - 200 psig).

A method according to any one of the preceding claims, wherein the transverse flow of the coating liquid is directed against a gyre comprising the coating liquid, which gyre is formed in the coating chamber around the optical fiber.

The method of claim 11, wherein the differences between a maximum temperature of the coating fluid in the gyre and a minimum temperature of the coating fluid in the vortex is less than 80 ° C, preferably less than 60 ° C.

A method according to any of claims 4-12, wherein the calibration die comprising a cone-shaped die, the cone-shaped die comprising a cone section and a land section, the cone-shaped matrices depriving a bubble section.

A method according to claim 12 or 13, wherein the cross-flowing coating liquid mixes with the coating liquid of the gyre.

The method according to any of the preceding claims, wherein the transversely flowing coating liquid in the transverse direction with. a speed selected from the following:

greater than 0.1 cm ³ / s, greater than 0.2 cm '' / s, greater than 0.5 cm '/ s.

in the range of 0.1 cm '/ s - 20 cm' / s, in the range of 0.2 cm '/ s - 20 cm ³ / s, in the range of 0.5 cm' / s - 20 cm '/ s.

A method according to any one of the preceding claims, wherein the separated transverse flow of the coating liquid is introduced into the coating chamber by means of an inlet configured for that purpose.

The method of claim 16, wherein the coating fluid is removed from the coating chamber by means of a roll-out configured therefor, the outlet being removed from the guide mold and calibration mold.

The method of claim 17, wherein an approximately equal amount of coating fluid is removed at the coating chamber outlet as it is supplied at the coating chamber inlet,

A method according to any one of claims 16-18, wherein the supplied coating liquid at the inlet has a temperature of less than the average temperature of the coating liquid in the gyre, preferably wherein the temperature of the coating liquid at the inlet is less than the average temperature of the first coating liquid in the gyre at least 5 ° C.

The method of claim 18 or 19, further comprising recycling the coating fluid removed at the outlet to the coating chamber.

The method of any one of claims 1.7-19, wherein the coating fluid is introduced at the inlet and removed from the outlet at a speed of one or more of the following:

greater than 0.1 cm "/ s, greater than 0.2 cm" / s, greater than 0.5 cnr "/ s, or in the range of 0.1 cm'Vs - 20 cnr / s.

The method of any one of the preceding claims, further comprising drawing the optical fiber through a second coating chamber comprising a second coating liquid, and preferably subjecting the optical fiber to the same processing in the second coating chamber as in the first coating chamber.

The method of any one of claims 3-22, wherein the guide mold is free from the coating fluid.

24, Coated optical fiber obtained in accordance with the method of any of the preceding claims,

25, Optical fiber processing system comprising:

one or more coating chambers for holding coating liquid for coating an optical fiber, the coating chamber comprising a fiber inlet and a fiber outlet, an inlet for feeding a loop or flow of coating liquid into the coating chamber, and an outlet for removing coating chamber coating fluid, the inlet and outlet of which are distinct from the fiber inlet and fiber outlet, the inlet being configured to transmit the flow or course of the coating fluid in a transverse direction to the draw direction of the optical fiber through the coating chamber to deliver.

26, A system according to claim 25, wherein the outlet is configured to remove the flow or run transversely of the coating fluid from the coating chamber,

27, System as claimed in claim 25 or 26, further comprising a guide mold which is associated with a first side of the coating chamber for guiding the optical fiber in the coating chamber and a calibrating mold, associated with a second opposite side of the coating chamber, wherein through the calibration mold coated cable has been pulled out of the coating chamber.

The system of any one of claims 25-28, further comprising a second coating chamber.

The system of claim 28, wherein the calibration die also as a guide die

5 functions for the second coating chamber.

The system of any one of claims 25-29, wherein the cross sectional dimensions of the inlet are greater than 30% of the distance between the fiber input and the fiber output, preferably greater than 50% of the distance between the fiber input and the fiber output, with more

Preferably greater than 70% of the distance between the fiber input and the fiber output, most preferably wherein the cross-section dimensions of the inlet are in the range of 30% - 100% of the distance between the fiber input and the fiber output.

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