Method of applying coating liquid to an optical fiber

Patent metadata

Field	Value
Publication number	US-12012358-B2
Application number	US-202117331979-A
Country	US
Kind code	B2
Filing date	May 27, 2021
Priority date	Jun 19, 2020
Publication date	Jun 18, 2024
Grant date	Jun 18, 2024

Abstract

Provided herein is a method of and system for processing an optical fiber. The method includes the steps of drawing an optical fiber in a drawing direction along a process pathway through a coating chamber comprising an inlet and an outlet, and a coating liquid volume to coat the optical fiber; supplying the coating liquid through the inlet, the coating liquid exiting the coating chamber through the outlet; and recirculating to coating liquid exiting the coating chamber to the inlet.

First claim

What is claimed is:

1. A method of processing an optical fiber, comprising the steps of:
drawing an optical fiber in a drawing direction along a process pathway through a coating chamber, the coating chamber comprising:
an inlet and an outlet, and
a coating liquid to coat the optical fiber;

supplying the coating liquid through the inlet into the coating chamber, the supplying comprising delivering the coating liquid to the coating chamber at a flow rate and a first pressure, the coating liquid exiting the coating chamber through the outlet; and
recirculating the coating liquid exiting the coating chamber to the inlet, the recirculating comprising reducing the pressure of the coating liquid from the first pressure to a second pressure; and
independently controlling the flow rate and first pressure, the independent controlling comprising one of (a) varying the flow rate without varying the first pressure or (b) varying the first pressure without varying the flow rate.

2. The method of claim 1 , wherein the supplying comprises varying the coating liquid between a maximum pressure and a minimum pressure, the minimum pressure being greater than a pressure of the coating liquid in the coating chamber.

3. The method of claim 1 , wherein a temperature of the coating liquid at the inlet is less than a temperature of the coating liquid at the outlet.

4. The method of claim 1 , wherein the optical fiber enters the coating chamber through a guide die and wherein the guide die comprises a bell section, a taper section, and a land section, or wherein the guide die comprises a cone-only guide die, the cone-only guide die comprising a cone section and a land section, the cone-only guide die lacking a bell section.

5. The method of claim 4 , wherein the optical fiber is drawn through the coating chamber to a sizing die and wherein the sizing die comprises a cone-only sizing die, the cone-only sizing die comprising a cone section and a land section, the cone-only sizing die lacking a bell section.

6. The method of claim 5 , wherein the coating liquid is directed in a transverse direction through a channel positioned in the coating chamber between the guide die and the sizing die.

7. The method of claim 5 , wherein the outlet is spaced apart from the guide die and the sizing die.

8. The method of claim 1 , wherein an approximately equal amount of the coating liquid exits through the outlet as enters through the inlet.

9. The method of claim 1 , wherein the coating liquid supplied through the inlet is directed against a gyre comprising the coating liquid contained in the coating chamber, the gyre being formed in the coating chamber adjacent to the optical fiber.

10. The method of claim 9 , wherein a 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.

11. The method of claim 1 , wherein the recirculating comprises:
delivering the coating liquid exiting the coating chamber to a pressurized catch can, the pressurized catch can containing the coating liquid at the second pressure;
pumping the coating liquid from the pressurized catch can to a pressurized keg, the pressurized keg containing the coating liquid at the first pressure;
and delivering the coating liquid from the pressurized keg to the inlet.

12. The method of claim 1 , wherein the delivering the coating liquid comprises removing the coating liquid from a keg pressurized to the first pressure and the recirculating comprises directing the coating liquid exiting the coating chamber to the keg.

13. The method of claim 12 , wherein the recirculating comprises directing the coating liquid exiting the coating chamber to a catch can pressurized to the second pressure and the directing the coating liquid to the keg comprises directing the coating liquid from the catch can to the keg.

14. The method of claim 1 , wherein the independently controlling further comprises varying the second pressure.

15. The method of claim 1 , wherein the independently controlling comprises (a) varying the flow rate without varying the first pressure.

16. The method of claim 15 , wherein the varying the flow rate comprises increasing the flow rate and the independently controlling further comprises reducing the second pressure.

17. The method of claim 1 , wherein the independently controlling comprises (b) varying the first pressure without varying the flow rate.

18. The method of claim 17 , wherein the varying the first pressure comprises increasing the first pressure and the independently controlling further comprises increasing the second pressure.

19. The method of claim 1 , wherein the second pressure is a pressure greater than atmospheric pressure.

Assignees

• Corning Inc

Inventors

• Biddix Derrick Baxter
• Kelmer Kenneth James
• Moore Robert Clark
• Neilson Douglas Gregg
• Sonnett Donald Justin
• Subler Jennifer Nicole
• Tucker David Andrew
• Watson John Edward

Classifications

• C03C25/26

  Macromolecular compounds or prepolymers · CPC title

• C03B37/02

  by drawing or extruding, {e.g. direct drawing of molten glass from nozzles; Cooling fins therefor (C03B37/04 takes precedence; sizing of the fibres C03C25/00)} · CPC title

• B05C11/1039

  Recovery of excess liquid or other fluent material; Controlling means therefor · CPC title

• B05C3/172

  in endless form · CPC title

• C03C25/18 Primary

  Extrusion · CPC title