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US4135903A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for producing fibers from heat-softening materials

Assignee: Nippon Sheet Glass Co Ltd
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Filing: 1976-08-18
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Granted: 1979-01-23
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Expires: 1996-08-18
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Abstract

Abstract Method and apparatus for producing fibers from a heat-softening material in which the heat-softening material is heated to a viscous melt, and directly and continuously flowed out while its sectional shape being rendered substantially circular. High speed gas streams having a component in the tangential direction of the circular sectional surface of the melt and a component which approaches the central axial line of the melt towards the flowing direction of the melt and then departs from the central axial line are jetted out onto the melt that has been flowed out. The high speed gas streams cause the melt to rotate around its central axial line and transform it into a substantially conical shape whose cross section gradually decreases towards its flowing direction in a first zone. In a second zone subsequent to the first zone, the melt is caused to advance in the form of fiber from the tip of the cone in the flowing direction and outwardly in the radial direction.

Inventors

  • 👤 Nobuyoshi Ohsato
  • 👤 Keihachiro Tanaka
  • 👤 Eiji Mizushima

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 16:50
CPC Classifications
C; C03; C03B; C03B37/00; C03B37/01; C03B37/06; D; D01; D01D; D01D5/00; D01D5/26

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 320 words
A method for producing fibers from a glass material, which comprises: heating the glass material in a melting crucible to form a viscous melt, and continuously causing the melt to flow from said crucible through at least one nozzle provided thereon; and jetting out at least three substantially straight-line high speed gas streams disposed at intervals around the melt in its peripheral direction, each of said streams having a component in the tangential direction along the cross-section of the melt and a component which gradually approaches the central axial line of the melt toward the flowing direction of the melt and then gradually departs from the central axial line, toward the melt which has flown out, whereby the melt is rotated about its central axial line and is formed into a substantially conical shape in a first zone which ranges from the flow-initiating part of the melt to the part at which the gas stream most closely approaches the central axial line of the melt, and in a second zone subsequent to the first zone, the melt being allowed to fly in fibrous form from the tip of the conical shape in a vortex form in the flowing direction and outwardly in the radial direction and wherein said straight-line high speed gas streams are inclined at an angle of 20 to 70° to the central axial line of the melt, the distance between the outlet of the melt-flowing nozzle and the focal point at which the high speed gas stream most closely approaches the central axial line of the melt being 0.2 to 10 times the effective hole diameter of the melt-flowing nozzle, and said straight-line high speed gas streams being arranged symmetrically with respect to the central axial line of the melt as a rotating symmmetrical axis, and at least two of the angles formed between the central axial lines of the adjoining gas streams being 95 to 135°.
Claim 2
Independent Claim 320 words
A method for producing fibers from a glass material, which comprises: heating the glass material in a melting crucible to form a viscous melt, and continuously causing the melt to flow from said crucible through at least one nozzle provided thereon; and jetting out at least three substantially straight-line high speed gas streams disposed at intervals around the melt in its peripheral direction, each of said streams having a component in the tangential direction along the cross-section of the melt and a component which gradually approaches the central axial line of the melt toward the flowing direction of the melt and then gradually departs from the central axial line, toward the melt which has flown out, whereby the melt is rotated about its central axial line and is formed into a substantially conical shape in a first zone which ranges from the flow-initiating part of the melt to the part at which the gas stream most closely approaches the central axial line of the melt, and in a second zone subsequent to the first zone, the melt being allowed to fly in fibrous form from the tip of the conical shape in a vortex form in the flowing direction and outwardly in the radial direction and wherein said straight-line high speed gas streams are inclined at an angle of 20 to 70° to the central axial line of the melt, the distance between the outlet of the melt-flowing nozzle and the focal point at which the high speed gas stream most closely approaches the central axial line of the melt being 0.2 to 10 times the effective hole diameter of the melt-flowing nozzle, and said straight-line high speed gas streams being arranged symmetrically with respect to the central axial line of the melt as a rotating symmmetrical axis, and at least two of the angles formed between the central axial lines of the adjoining gas streams being 95 to 135°.
Claim 3
Dependent Claim 27 words
The method of claim 1 wherein the melt is flown such that its sectional shape is substantially a circle with a diameter of 0.5 to 10 mm.
Claim 4
Dependent Claim 27 words
The method of claim 1 wherein the thinnest tip portion of the cone formed in the first zone has a diameter of about 0.1 to 1 mm.
Claim 5
Dependent Claim 21 words
The method of claim 1 wherein the effective hole diameter d 2 of the melt-flowing nozzle is 0.5 to 2.5 mm.
Claim 6
Dependent Claim 25 words
The method of claim 1 wherein the viscosity of the melt immediately before rotation in the first zone is adjusted to 10 to 200 poises.
Claim 7
Dependent Claim 18 words
The method of claim 5 wherein the viscosity of the melt is adjusted to 50 to 100 poises.
Claim 8
Dependent Claim 37 words
The method of claim 1 wherein another separate high speed gas stream for drawing is jetted along a central axial line of the melt onto the fibrous melt which has flown from the tip of the cone.
Claim 9
Dependent Claim 95 words
The method of claim 1 wherein each of the straight-line high speed gas streams is jetted out from a jet nozzle having an effective hole diameter d 1 , and the effective hole diameter d 1 and the drawn diameter D 2 defined by the straight-line high speed gas stream have a dimension that it selected from an area obtained by connecting points (0, 0), (3.0, 5.3), (3.0, 7.0), (2.4, 7.0), and (0, 2.0) in a diagram with d 1 (mm) on the axis of abscissas and D 2 (mm) on the axis of ordinates.
Claim 10
Dependent Claim 39 words
The method of claim 1 wherein the blow-out diameter D 1 defined by the straight-line high speed gas stream is in the following relation with respect to the drawn diameter D 2 , d.sub.2 < d.sub.1 ≦ 10 d.sub.2.
Claim 11
Dependent Claim 22 words
the method of claim 9 wherein the above relation is expressed by the following equation, 1.3 D.sub.2 ≦ D.sub.1 ≦ 3 D.sub.2.
Claim 12
Dependent Claim 36 words
the method of claim 1 wherein each of the straight-line high speed gas streams is jetted out from a jet nozzle whose length l is at least 5 times its effective hole diameter d 1 .

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-01-22 1982-07-24 1983-01-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-01-22 1986-07-24 1987-01-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-01-22 1990-07-24 1991-01-23 $7700.00 Window Closed / Lapsed

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