Optical fiber draw production systems, pressure devices and methods applying pressure to optical fiber

1 . A method of processing an optical fiber comprising:

drawing the optical fiber from a preform through a draw furnace operable to draw the optical fiber from the preform;

directing the optical fiber in a downstream direction along a process pathway, the optical fiber having a forming point at a first position along the process pathway, the optical fiber having a forming point temperature T fp at the forming point; and

passing the optical fiber through a pressure device downstream from the draw furnace and operable to receive the optical fiber from the draw furnace and subject the optical fiber to an applied pressure greater than 10 atm at a second position along the process pathway, the second position upstream of the first position, and the optical fiber having a temperature T 1 at the second position,

wherein T fp −150° C.≤T 1 ≤T fp +100° C.

2 . The method of claim 1 , wherein T fp is between 1500° C. and 1700° C., including endpoints.

3 . The method of claim 1 , further comprising directing the optical fiber to a cooling device positioned along the process pathway, the cooling device configured to cool the optical fiber at a rate less than 5000° C./s.

4 . The method of claim 3 , wherein the optical fiber enters the cooling device at a temperature greater than T 1 −100° C.

5 . The method of claim 3 , wherein a residence time of the optical fiber inside of the cooling device is less than 0.5 seconds.

6 . A fiber draw production system comprising:

a draw furnace operable to draw an optical fiber from a preform in a downstream direction along a process pathway, the optical fiber having a forming point at a first position along the process pathway, the optical fiber having a forming point temperature T fp at the forming point; and

a pressure device downstream from the draw furnace and operable to receive the optical fiber from the draw furnace and subject the optical fiber to an applied pressure greater than 10 atm at a second position along the process pathway, the second position upstream of the first position, and the optical fiber having a temperature T 1 at the second position,

wherein T fp −150° C.≤T 1 ≤T fp +100° C.

7 . The fiber draw production system of claim 6 , wherein the fiber draw production system is such that a residence time of the optical fiber within the pressure device is greater than 40 msec.

8 . The fiber draw production system of claim 6 , wherein the pressure device comprises a pressure chamber, an inlet nozzle at an entrance end of the pressure chamber, and an exit nozzle at an exit of the pressure chamber.

9 . The fiber draw production system of claim 8 ,

wherein: the exit nozzle comprises a straight section

and a tapered section;

the straight section has a diameter that is less than 150 μm and a length within a range of 50 μm and 150 μm, including end points;

the tapered section has an increasing diameter defined by a taper angle; and a flow rate to the exit nozzle is less than 100 g/min.

10 . The fiber draw production system of claim 6 , wherein the pressure device comprises at least one nozzle.

11 . The fiber draw production system of claim 10 , wherein the at least one nozzle comprises a series of step bearings, wherein each step bearing of the series of step bearings comprises a first segment having a first diameter and a first length and a second segment having a second diameter and a second length.

12 . The fiber draw production system of claim 11 , wherein the first diameter is greater than the second diameter and the first length is shorter than the second length.

13 . The fiber draw production system of claim 6 , further comprising a cooling device positioned along the process pathway, the cooling device configured to cool the optical fiber at a rate less than 5000° C./s.

14 . The fiber draw production system of claim 13 , wherein the optical fiber enters the cooling device at a temperature greater than T1-100° C.

15 . The fiber draw production system of claim 13 , wherein a residence time of the optical fiber inside of the cooling device is less than 0.5 seconds.

16 . A pressure device for applying pressure to an optical fiber drawn from a draw furnace along a process pathway, the optical fiber having a forming point at a first position along the process pathway, the optical fiber having a forming point temperature Tip at the forming point, and the pressure device comprising:

a pressure chamber comprising an entrance end and an exit end; an entrance nozzle at the entrance end;

an exit nozzle at the exit end; and

an inlet fluidly coupled to the entrance nozzle, wherein:

the pressure device is operable to receive the optical fiber at a second position along the process pathway and subject the optical fiber to an applied pressure greater than 10 atm;

the exit nozzle comprises a straight section and a tapered section;

the straight section has a diameter that is less than 150 μm and a length within a range of 50 μm and 150 μm, including end points;

the tapered section has an increasing diameter defined by a taper angle; and

a flow rate to the exit nozzle is less than 100 g/min.

17 . The pressure device of claim 16 , wherein the exit nozzle comprises a series of nozzles.

18 . The pressure device of claim 16 , wherein:

at least one of the entrance nozzle and the exit nozzle comprises a series of step bearings; and

each step bearing of the series of step bearings comprises a first segment having a first diameter and a first length and a second segment having a second diameter and a second length.

19 . The pressure device of claim 18 , wherein the first diameter is greater than the second diameter and the first length is shorter than the second length.

20 . The pressure device of claim 16 , wherein the inlet has a taper angle of less than or equal to 5 degrees.

21 . The pressure device of claim 16 , wherein:

the second position is upstream of the first position; and

the optical fiber having a temperature T 1 at the second position; and

T fp −150° C.≤T 1 ≤T fp +100° C.