Purge device for an optical fiber draw system
An optical fiber production system is provided which includes a slow-cooling device and a purge device positioned above the slow-cooling device. The purge device includes a tube defining an inlet. An optical fiber extends through the slow-cooling device and the purge device. The purge device is configured to inject a purge gas through the inlet and against the optical fiber.
1. An optical fiber production system, comprising:
a draw furnace;
a slow-cooling device located downstream and separate from the draw furnace;
a purge device positioned above the slow-cooling device and positioned below and spaced from the draw furnace, the purge device comprising a tube defining an inlet; and
an optical fiber extending from the draw furnace through the slow-cooling device and the purge device, wherein the purge device is configured to inject a purge gas through the inlet and against the optical fiber in a direction generally opposite to a direction the optical fiber is drawn, wherein the slow-cooling device cools the optical fiber at a rate that is slower than a cooling rate of the optical fiber in air at 25° C. and a pressure of 1 ATM, and wherein the injection of the purge gas disrupts a boundary layer of gas present along the optical fiber sufficiently to result in a reduction of particles present in the boundary layer from flowing into the slow-cooling device.
2. The system of claim 1 , wherein the purge gas has a flow rate through the inlet of between about 10 SLPM and about 40 SLPM.
3. The system of claim 1 , wherein the inlet is continuous around a circumference of the tube.
4. The system of claim 1 , wherein the inlet has an angle with respect to an X-Y plane of the optical fiber production system of greater than about 0° and less than about 40°.
5. The system of claim 4 , wherein the inlet has an angle with respect to an X-Y plane of the optical fiber production system of greater than about 10° and less than about 35°.
6. The system of claim 1 , wherein the inlet has a height of between about 0.1 mm and about 10.0 mm.
7. The system of claim 1 , wherein the tube further defines an inlet manifold, the inlet fluidly coupling the inlet manifold and a passageway of the tube.
8. An optical fiber production system, comprising:
a draw furnace;
a slow-cooling device located downstream and separate from the draw furnace;
a purge device positioned above the slow-cooling device and positioned below and spaced from the draw furnace, comprising:
a tube defining a passageway through which an optical fiber is drawn and an inlet, the purge device configured to inject a purge gas into the passageway through the inlet and against the optical fiber in a direction generally opposite to a direction the optical fiber is drawn such that the purge gas disrupts a boundary layer of gas present along the optical fiber, wherein the slow-cooling device cools the optical fiber at a rate that is slower than a cooling rate of the optical fiber in air at 25° C. and a pressure of 1 ATM.
9. The system of claim 8 , wherein the injection of the purge gas disrupts the boundary layer of gas present along the optical fiber sufficiently to result in a reduction of particles present in the boundary layer from flowing into the slow-cooling device.
10. The system of claim 9 , wherein the inlet has a height of between about 0.1 mm and about 10.0 mm.
11. The system of claim 8 , wherein the inlet has an angle with respect to an X-Y plane of the optical fiber production system of greater than about 0° and less than about 40°.
12. The system of claim 8 , wherein the inlet is continuous around a circumference of the tube.
13. The system of claim 8 , wherein a gap is defined between the tube and an upper member of the purge device.
14. A method of forming an optical fiber, comprising:
providing a tube and a nozzle assembly positioned over a slow-cooling treatment device and positioned below and spaced from a draw furnace, the tube defining an inlet;
heating an optical fiber preform in the draw furnace;
drawing an optical fiber from the preform;
passing the optical fiber through the tube and the nozzle assembly, wherein the slow-cooling treatment device is located downstream and separate from the draw furnace and the slow-cooling treatment device cools the optical fiber at a rate that is slower than a cooling rate of the optical fiber in air at 25° C. and a pressure of 1 ATM; and
injecting a purge gas through the inlet toward the optical fiber, wherein the injection of the purge gas toward the optical fiber is in a direction generally opposite a drawing direction of the optical fiber such that the purge gas disrupts a boundary layer of gas present along the optical fiber.
15. The method of claim 14 , further comprising the step:
drawing the purge gas within the slow-cooling treatment device into the tube.
16. The method of claim 14 , wherein the inlet has an angle with respect to an X-Y plane of the optical fiber production system of between about 0° and about 40°.
17. The method of claim 14 , wherein the purge gas has a flow rate through the inlet of between about 10 SLPM and about 40 SLPM.