Process of using a submerged combustion melter to produce hollow glass fiber or solid glass fiber having entrained bubbles, and burners and systems to make such fibers

Patent metadata

Field	Value
Publication number	US-9926219-B2
Application number	US-201615272703-A
Country	US
Kind code	B2
Filing date	Sep 22, 2016
Priority date	Jul 3, 2012
Publication date	Mar 27, 2018
Grant date	Mar 27, 2018

Abstract

Processes and systems for producing glass fibers having regions devoid of glass using submerged combustion melters, including feeding a vitrifiable feed material into a feed inlet of a melting zone of a melter vessel, and heating the vitrifiable material with at least one burner directing combustion products of an oxidant and a first fuel into the melting zone under a level of the molten material in the zone. One or more of the burners is configured to impart heat and turbulence to the molten material, producing a turbulent molten material comprising a plurality of bubbles suspended in the molten material, the bubbles comprising at least some of the combustion products, and optionally other gas species introduced by the burners. The molten material and bubbles are drawn through a bushing fluidly connected to a forehearth to produce a glass fiber comprising a plurality of interior regions substantially devoid of glass.

First claim

What is claimed is:

1. An adjustable submerged combustion burner comprising:
a first conduit comprising a first end, a second end, a longitudinal bore having a longitudinal axis, and an external surface, the first end comprising threads on the external surface,
a second conduit substantially concentric with the first conduit, the second conduit comprising a first end, a second end, and an internal surface,
the first and second conduits configured to form a primary annulus between the external surface of the first conduit and the internal surface of the second conduit;
a body having an upper surface, a lower surface, a circumferential surface abutting a portion of the internal surface of the second conduit, and a generally cylindrical central hub concentric with the longitudinal axis, the structure adjustable axially in relation to and threadedly attached to the threads of the first end of the first conduit via the hub, the hub defining a central passage having an exit at the upper surface, the body comprising one or more non-central through passages extending from the lower to the upper surface, the non-central passages configured such that flow of one or more fluids through the non-central passages causes the fluids to intersect with a flow of one or more other fluids in a mixing region above the upper surface of the body;
a third substantially concentric conduit comprising a first end, a second end, and an internal surface, the internal surface of the third conduit forming, with an exterior surface of the second conduit, a secondary annulus external to the primary annulus;
the first end of the third conduit extending beyond the first end of the second conduit, the first end of the second conduit extending beyond the first end of the first conduit, and the secondary annulus is capped by a half-toroid end cap connecting the first end of the second conduit and the first end of the third conduit; and
the second end of the second conduit sealed around the first conduit, and the second end of the third conduit sealed around the second conduit, forming a cavity for fluid to circulate.

2. The apparatus of claim 1 wherein the non-central passages are generally linear and angled at an angle β measured from the longitudinal axis, the β angle ranging from about 10 degrees to about 45 degrees.

3. The apparatus of claim 1 wherein the non-central passages comprise a vertical section and an angled section, the vertical section beginning at the lower surface of the structure and intersecting the angled section, the angled section ending at the upper surface of the structure.

4. The apparatus of claim 1 wherein the non-central passages are non-linear.

5. The apparatus of claim 1 wherein a number of non-central passages ranges from about 2 to about 20.

6. A process comprising:
a) feeding at least one partially or wholly vitrifiable feed material into a feed inlet of a melting zone of a melter vessel comprising a floor, a ceiling, and a wall connecting the floor and ceiling at a perimeter of the floor and ceiling, the melter vessel comprising a feed opening in the wall or ceiling and an exit end comprising a melter exit structure for discharging molten material formed in the melting zone;
b) heating the at least one partially or wholly vitrifiable material with at least one burner directing combustion products of an oxidant and a first fuel into the melting zone under a level of the molten material in the zone, one or more of the burners of claim 1 configured to impart heat and turbulence to at least some of the molten material in the melting zone, producing a turbulent molten material comprising a plurality of bubbles suspended in the molten material, the bubbles comprising at least some of the combustion products;
c) discharging the molten material comprising bubbles from the melter vessel through the melter exit structure into a forehearth; and
d) drawing the molten material comprising bubbles through a bushing fluidly connected to the forehearth to produce a glass fiber comprising a plurality of interior regions substantially devoid of glass.

7. The process of claim 6 wherein the forehearth has a plurality of bushings producing fibers of the same outside diameter, the process comprising controlling flow of the molten material comprising bubbles through the forehearth and bushings so that fibers produced through the bushings are substantially consistent in volume of regions devoid of glass.

8. The process of claim 7 wherein the controlling comprises inclining the forehearth at an angle to horizontal of no more than about 30 degrees to horizontal, the angle causing a distal end of the forehearth furthest from the melter exit structure to be raised above a horizontal plane, while a proximal end of the forehearth remains at a level equal to that of the melter exit.

9. The process of claim 7 wherein the forehearth is substantially horizontal, and the controlling comprises the bushings drawing off the molten material comprising bubbles in a configuration where a bushing most proximal to the melter exit structure draws at a lowest level in the forehearth and succeeding bushings draw molten material comprising bubbles at progressively higher levels in the forehearth.

10. A process comprising:
a) feeding at least one partially or wholly vitrifiable material into a feed inlet of a melting zone of a melter vessel comprising a floor, a ceiling, and a wall connecting the floor and ceiling at a perimeter of the floor and ceiling, the melter vessel comprising a feed opening in the wall or ceiling and an exit end comprising a melter exit structure for discharging molten material formed in the melting zone;
b) heating the at least one partially or wholly vitrifiable material with at least one burner directing combustion products of an oxidant and a first fuel into the melting zone under a level of the molten material in the zone, one or more of the burners of claim 1 configured to impart heat and turbulence to at least some of the molten material in the melting zone, producing a turbulent molten material comprising a plurality of bubbles suspended in the molten material, the bubbles comprising at least some of the combustion products;
c) discharging the molten material comprising bubbles from the melter vessel through the melter exit structure into a forehearth;
d) drawing the molten material comprising bubbles through a plurality of bushings producing glass fibers each comprising a plurality of interior regions devoid of glass, the fibers having substantially same outside diameter; and
e) controlling flow of the molten material comprising bubbles through the forehearth and bushings so that fibers produced through the bushings are substantially consistent in volume of regions devoid of glass.

11. The process of claim 10 wherein the controlling comprises inclining forehearth at an angle to horizontal of no more than about 30 degrees, the angle causing a distal end of the forehearth to be raised above a horizontal plane, while a proximal end of the forehearth remains at a level equal to that of the melter exit.

12. A system comprising:
a) a melter vessel comprising a floor, a ceiling, and a wall connecting the floor and ceiling at a perimeter of the floor and ceiling, the melter vessel comprising a feed opening in the wall or ceiling and an exit end comprising a melter exit structure for discharging molten material formed in a turbulent melting zone, and one or more burners of claim 1 , at least one of which is positioned to direct combustion products into the turbulent melting zone under a level of turbulent molten material in the turbulent melting zone;
b) a forehearth fluidly connected to t

Assignees

• Johns Manville

Inventors

• Charbonneau Mark William
• Mchugh Kevin Patrick

Classifications

• F23D14/22

  with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other · CPC title

• C03B37/07

  Controlling or regulating ({C03B37/0253 takes precedence } ; controlling or regulating in general G05) · CPC title

• C03B37/022

  from molten glass in which the resultant product consists of different sorts of glass or is characterised by shape, e.g. hollow fibres {, undulated fibres, fibres presenting a rough surface (C03B37/025 takes precedence)} · CPC title

• C03B2211/60

  oxy-fuel burner construction · CPC title

• C03B7/02

  Forehearths, i.e. feeder channels · CPC title