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US4937020A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of very fine polymer fibres

Assignee: Bayer AG
•
Filing: 1989-01-03
•
Granted: 1990-06-26
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Expires: 2009-01-03
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Abstract

Abstract The polymer granular melt (1) is whirled out of a rotating nozzle head (6) through a plurality of exit holes (24) with fibre formation (32) and the fibres formed (9) are deposited on a collecting surface (12) in web form (15). This polymer melt is introduced into the nozzle head (6) under a preliminary pressure of 1 bar to 200 bar, preferably 1 bar to 50 bar. Furthermore, the fibres (32) are deflected by a high-speed gas stream (7, 8) in a radial direction at a radial distance of 10 mm to 200 mm from the exit holes (24) and, in the course of being deflected, are simultaneously drawn and stretched. The melt streams (32) exiting from the exit holes (24) can be additionally drawn by gas streams (26, 34) exiting in the vicinity of the exit holes (24) at the nozzle head (6) with a predominantly radial component before coming under the influence of the axial deflecting gas stream (7, 8).

Inventors

  • 👤 Wolfram Wagner
  • 👤 Peter R. Nyssen
  • 👤 Dirk Berkenhaus
  • 👤 Hans-Theo van Pey

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 12:44
CPC Classifications
D; D04; D04H; D04H3/00; D04H3/02; D01; D01D; D01D5/00; D01D5/18; D04H3/005; D04H3/009; D04H3/011; D04H3/08; D04H3/16

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 166 words
In a process for producing very fine polymer fibres of finite length having an average fibre diameter of 0.1 μm to 10 μm from thermoplastic polymers by whirling the molten polymer radially out of a rotating nozzle head through a plurality of exit holes with fibre formation and depositing the fibres formed on a collecting surface in web form, the improvement comprising: introducing the molten polymer into the nozzle head under a preliminary pressure of 1 bar to 200 bar, deflecting the fibres in the axial direction by a high-speed axial gas stream at a radial distance of 10 mm to 200 mm from the exit holes to simultaneously draw and stretch same in the course of being deflected and additionally drawing the melt streams exiting from the exit holes by radial gas streams exiting in the vicinity of the exit holes at the nozzle head with a predominantly radial component before coming under the influence of the axial gas stream having a predominantly axial component.
Claim 2
Dependent Claim 166 words
In a process for producing very fine polymer fibres of finite length having an average fibre diameter of 0.1 μm to 10 μm from thermoplastic polymers by whirling the molten polymer radially out of a rotating nozzle head through a plurality of exit holes with fibre formation and depositing the fibres formed on a collecting surface in web form, the improvement comprising: introducing the molten polymer into the nozzle head under a preliminary pressure of 1 bar to 200 bar, deflecting the fibres in the axial direction by a high-speed axial gas stream at a radial distance of 10 mm to 200 mm from the exit holes to simultaneously draw and stretch same in the course of being deflected and additionally drawing the melt streams exiting from the exit holes by radial gas streams exiting in the vicinity of the exit holes at the nozzle head with a predominantly radial component before coming under the influence of the axial gas stream having a predominantly axial component.
Claim 3
Dependent Claim 44 words
The process according to claim 1, wherein the radial gas streams each exit at an angle of 0° to 45°, relative to the direction of the melt exit passages and at a distance of 2 mm to 20 mm from the melt exit holes.
Claim 4
Dependent Claim 22 words
The process according to claim 2, wherein the radial gas streams exit at a flow speed of 100 m/s to 600 m/s.
Claim 5
Dependent Claim 38 words
The process according to claim 1, the fibres are deflected by the axial gas stream at a flow speed of 50 m/s to 500 m/s at an angle of +60° to -60° relative to the axis of rotation.
Claim 6
Dependent Claim 30 words
The process according to claim 1, wherein the melt streams are whirled out of the exit holes at an angle of 45° to 90° relative to the axis of rotation.
Claim 7
Dependent Claim 54 words
The process according to claim 1, further comprising producing, in addition to the acceleration of the melt stream caused in the nozzle head by the preliminary pressure on the polymer melt, a pressure of 1 bar to 200 bar in a chamber upstream of the melt exit holes by a sufficiently high centrifugal acceleration.
Claim 8
Dependent Claim 29 words
The process according to claim 1, wherein the ratio of the radial gas flow rate to the axial flow rate is set at a value between 0 to 5.
Claim 9
Dependent Claim 33 words
The process according to claim 1, further comprising heating the radial gas flow to a temperature which is equal to or greater than the temperature of the polymer melt at the exit holes.
Claim 10
Dependent Claim 21 words
The process according to claim 1, wherein the thermoplastic material is polyurethane, polyolefine, polyamide, polyesters, polyphenylene sulphide or thermotropic LC polymers.
Claim 11
Dependent Claim 22 words
The process according to claim 1, wherein the molten polymer is introduced under a preliminary pressure of 1 bar to 50 bar.
Claim 12
Dependent Claim 19 words
The process according to claim 2, wherein the radial gas streams exit at an angle of 5° to 20°.
Claim 13
Dependent Claim 25 words
The process according to claim 6, wherein the pressure in the chamber upstream of the melt exit holes is from 1 bar to 50 bar.
Claim 14
Dependent Claim 14 words
The process according to claim 7, wherein the ratio is between 0.4 to 2.

References Cited (Backward Citations)

US2931422A Cited
US3254977A Cited
US3928009A Cited
US4058386A Cited
US4237081A Cited
US4277436A Cited
US4246017A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-06-25 1993-12-25 1994-06-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-06-25 1997-12-25 1998-06-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-06-25 2001-12-25 2002-06-26 $7700.00 Window Closed / Lapsed

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