Alternating and continuous microwave fiber tow coating thermo-chemical reactor furnace

Patent metadata

Field	Value
Publication number	US-12529143-B2
Application number	US-202418669826-A
Country	US
Kind code	B2
Filing date	May 21, 2024
Priority date	Dec 22, 2021
Publication date	Jan 20, 2026
Grant date	Jan 20, 2026

Abstract

A reactor furnace for coating fiber tow includes an elongate reactor having a fiber tow inlet and a fiber tow outlet; a thermo-chemical reactor section positioned along the elongate reactor; a first microwave source for directing microwave energy along the reactor from a first end of the reactor toward a second end of the reactor; a second microwave source for directing microwave energy along the reactor from the second end of the reactor toward the first end of the reactor; a gas inlet upstream of the thermo-chemical reactor; and a gas outlet downstream of the thermo-chemical reactor.

First claim

What is claimed is:

1 . A method for coating a fiber tow, comprising:
passing fiber tow through a reactor furnace in the presence of a coating gas; and directing a first microwave energy along a length of the fiber tow in one direction; and directing a second microwave energy along the length of the fiber tow in a second direction, wherein the first microwave energy is directed along the fiber tow in a direction of movement of the fiber tow through the reactor furnace, and wherein the second microwave energy is directed along the fiber tow in a direction opposite to the movement of the fiber tow in through the reactor furnace.

2 . The method of claim 1 , further comprising receiving the first microwave energy in a first circulator to direct the first microwave energy away from a source of the second microwave energy; and receiving the second microwave energy in a second circulator to direct the second microwave energy away from the source of the first microwave energy.

3 . The method of claim 2 , wherein the first circulator directs the first microwave energy to a first terminator, and wherein the second circulator directs the second microwave energy to a second terminator.

4 . The method of claim 3 , further comprising determining an amount of energy received in each of the first terminator and the second terminator, and adjusting power to a source of the first microwave energy and a source of the second microwave energy based on the amount of energy received.

5 . The method of claim 3 , further comprising recovering energy from the first terminator and the second terminator as heat and using the heat to preheat the coating gas.

6 . The method of claim 1 , further comprising alternating between directing the first microwave energy along the fiber tow and directing the second microwave energy along the fiber tow.

7 . The method of claim 1 , further comprising feeding fiber tow to the reactor furnace from a first fiber spool, and receiving coated fiber from the reactor furnace onto a second fiber spool, wherein at least one of the first fiber spool and the second fiber spool is electrically grounded.

8 . A method for coating a fiber tow, comprising:
passing fiber tow through a reactor furnace in the presence of a coating gas; and directing a first microwave energy along a length of the fiber tow in one direction; and directing a second microwave energy along the length of the fiber tow in a second direction, wherein the gas is introduced to the reactor furnace to flow through a thermo-chemical reactor section of the reactor furnace in a gas flow direction, and wherein one of the first microwave energy and the second microwave energy is directed in the same direction as the gas flow direction, and the other of the first microwave energy and the second microwave energy is directed opposite to the gas flow direction.

9 . A method for coating a fiber tow, comprising:
passing the fiber tow through a reactor furnace in the presence of a coating gas; and directing a first microwave energy along a length of the fiber tow in a first direction from a first end of the reactor furnace toward a second end of the reactor furnace; and directing a second microwave energy along the length of the fiber tow in a second direction from the second end toward the first end; receiving and directing the first microwave energy, after passing a reaction zone of the reactor furnace in the first direction, to a first termination point; and receiving and directing the second microwave energy, after passing the reaction zone of the reactor furnace in the second direction, to second a termination point.

10 . The method of claim 9 , wherein the first direction is directed along the fiber tow in the direction of feed of the fiber tow, and wherein the second direction is directed along the fiber tow in a direction opposite to the direction of feed.

11 . The method of claim 9 , further comprising determining an amount of energy received in each of the receiving and directing steps, and adjusting power to the first microwave energy relative to the second microwave energy based on the amount of energy received.

12 . The method of claim 9 , further comprising recovering energy from the termination point as heat and using the heat to preheat the coating gas.

13 . The method of claim 9 , further comprising alternating between directing the first microwave energy in the first direction along the fiber tow and directing the second microwave energy in the second direction along the fiber tow.

14 . The method of claim 9 , further comprising feeding the fiber tow to the reactor furnace from a first fiber spool, and receiving coated fiber from the reactor furnace onto a second fiber spool, wherein at least one of the first fiber spool and the second fiber spool is electrically grounded.

15 . The method of claim 9 , wherein gas is introduced to the reactor furnace to flow through a thermo-chemical reactor section of the reactor furnace in a gas flow direction, and wherein one of the first microwave energy and the second microwave energy is directed in the same direction as the gas flow direction, and the other of the first microwave energy and the second microwave energy is directed opposite to the gas flow direction.

16 . The method of claim 9 , wherein the first termination point and the second termination point are the same.

17 . The method of claim 9 , wherein the first termination point is different from the second termination point.

Assignees

• Rtx Corp

Inventors

• Gangloff Jr John J
• Holowczak John E
• She Ying
• Smith Kenneth David
• Cordatos Haralambos
• Gok Gurkan
• Dardas Zissis A

Classifications

• H01J37/32192

  Microwave generated discharge (H01J37/32357, H01J37/32366, H01J37/32394, H01J37/32403 take precedence) · CPC title

• H01J37/3277

  of continuous material · CPC title

• C23C16/511

  using microwave discharges · CPC title

• C04B35/62884

  by gas phase techniques · CPC title

• F27B9/021

  having two or more parallel tracks · CPC title