Ferrule and use thereof for cooling a melt spun hollow glass fiber as it emerges from a spinnerette

Claim 2

A ferrule having utility for uniformly cooling an individual, melt-spun, hollow glass fiber, without making substantial contact with the fiber, as it issues from a spinnerette and passes downwardly through the ferrule, said ferrule having a rigid, heat-conductive body member, an interior wall of which defines a vertical, rectilinear passageway extending completely through said member and having the general shape of a long-stemmed, conical funnel, every cross-section of said passageway along its axis being generally circular in shape, said ferrule being adapted, by generally vertical cuts which form a slot therein or divide the ferrule into mating segments, so that it can be emplaced adjacent to a spinnerette and closely fitted around a moving fiber is issuing therefrom, in a position such that the axes of the fiber and passageway will coincide and the fiber will enter the funnel-shaped portion of said passageway as it leaves the spinnerette and exit from the lower terminus of the stem-shaped section, the width of said slot or the widths of the spaces between the mated segments being such that not more than 25 percent of any circumference of said passageway is interrupted by said slot or spaces, said ferrule, or each of said segments, being so composed as to have an average heat conductivity at least equal to that of graphite and being adapted to be brought into heat-transfer-effective contact with a heat sink.

Claim 3

A ferrule, as defined in claim 1 wherein the funnel section of the passageway has the shape of a major frustum of an inverted right, circular cone; the maximum possible angle, alpha, between two surface elements of said cone is within the range of from about 30° to about 75°; the passageway diameter at the mouth of the funnel section is within the range of from about 1700 to about 10,000 microns, the diameter at the terminus of the stem section of said passageway is within the range of about 50 to about 750 microns, the overall length of the passageway is within the range of from about 12,700 to 25,400 microns and the diameter of the stem section, from said terminus to the juncture with the funnel section, is constant or increases smoothly or in one or more discrete stages.

Claim 4

A ferrule segment which when mated with one or more similar segments will constitute a segmented ferrule as defined in claim 1.

Claim 5

A ferrule segment which when mated with one or more similar segments will constitute a segmented ferrule as defined in claim 2.

Claim 6

A segmented ferrule, as defined in claim 1 which consists of a mirror image pair of half-ferrules.

Claim 7

A ferrule as in claim 1 in heat-transfer-effective contact with a fluid-cooled heat sink.

Claim 8

A ferrule as in claim 1 wherein the wall of the funnel section of said passageway is inwardly convex and the angle of intersection of tangents drawn to the curved lines of intersection between the wall and a plane including the axis of the passageway, at the points of maximum inflection of said curves, is from about 35° to about 80°.

Claim 9

The method of removing heat from a melt-spum hollow glass fiber as it issues from a spinnerette, which comprises 1. providing a ferrule, as defined in claim 1, which is in heat-transfer-effective contact with said heat sink, the passageway in said ferrule being of such shape and size that the wall defining it will conform closely to but not make substantial contact with said fiber when the ferrule is positioned so that the fiber enters the mouth of said funnel section of the passageway as it exits the spinnerette, and leaves the stem section of said passageway at said terminus thereof, the axes of the fiber and the passageway coinciding, 2. positioning said ferrule as in (1) above, the space between said fiber and said wall being occupied by a gaseous fluid, 3. conducting said heat from the fiber to the ferrule, by means of said gaseous fluid, and from the ferrule to the heat sink, the thermal conductivity of said fluid, the length of said passageway, the fiber take-up rate and the maximum radial distance between the fiber and said wall being such that the fiber attains a non-fluid state upon or prior to leaving said passageway.

Claim 10

The method of claim 8 in which the ferrule is as defined in claim 2.

Claim 11

The method of claim 8 in which the gas constituting said fluid is air.

Claim 12

The method of claim 8 in which the gas constituting said fluid is helium.

Claim 13

The method of claim 8 in which the walls of the passageway through the ferrule are coated with graphite.

Claim 14

The method of claim 8 comprising the following steps: 1. providing a spinnerette adapted by means of a core gas needle for (melt) spinning of hollow glass fibers, the outer to inner diameter ratio of the orifice being within the range of from about 0.5 to about 1.3 times the outer to inner diameter ratio of the fiber to be spun and said needle extending from the terminus of the orifice from about 0 to about 0.1 inches (2540μ); 2. while passing a core gas through said needle under sufficient pressure to prevent capillary rise of glass into the needle, flowing a molten glass vertically downward through said orifice under a pre-selected head and at a pre-selected temperature, thereby establishing a volume flow rate V g determined by the viscosity of the glass at said temperature; 3. leading the resulting fiber onto a take-up drum of a size and rotating at a pre-selected rate such as to provide a linear take-up rate equal to V g /a, where a is a cross-sectional area of the fiber (solid or hollow); 4. positioning a ferrule of the present invention around the moving fiber, adjacent the spinnerette face, so that the fiber enters the passageway through the ferrule as it exits the spinnerette orifice; 5. placing a heat sink in functionally effective contact with the ferrule; 6. collecting the fiber on the take-up drum until an essentially steady state condition has been established in the fluid portion of the fiber; 7. determining the area a and, if necessary, adjusting the glass flow rate or take-up rate, or both, until a is equal to π(d o 2 -d i 2 )/4, d o and d i being the desired outer and inner fiber diameters, respectively; 8. establishing a pre-selected, core gas pressure head of from about 3 to about 15 cm of water; 9. again collecting fiber until an essentially steady state condition has been established in the fluid portion of the fiber; and

Claim 15

determining the outer and inner diameters of the fiber being produced and, if necessary, adjusting the core gas pressure to obtain the desired wall thickness.

Claim 16

determining the outer and inner diameters of the fiber being produced and, if necessary, adjusting the core gas pressure to obtain the desired wall thickness.