Process and apparatus for producing non-woven webs of strong filaments

• US 6,013,223 A
• Filed: 05/28/1998
• Issued: 01/11/2000
• Est. Priority Date: 05/28/1998
• Status: Expired due to Term

• Current Assignee: Reifenhauser GmbH & Co
• Original Assignee: Biax-Fiberfilm Corporation
• Inventors: Schwarz, Eckhard C.A.
• Primary Examiner(s): Tentoni, Leo B.
• Application Number:
  US09/085,464
• Time in Patent Office: 593 Days
• Field of Search: 264/103, 264/210.8, 264/211.14, 264/211.17, 264/555, 425/66, 425/72.2, 425/378.2, 425/379.1, 425/382.2, 425/464
• US Class Current: 264/555
• CPC Class Codes: D01D 5/0985 by means of a flowing gas (e.g. melt-blowing)

Abstract

An apparatus and process for extruding fiberforming thermoplastic polymers through spinning nozzles arranged in multiple rows are forming a non-woven web of high strength fibers. The molten fibers are accelerated by expanding hot gas flowing parallel to the extrusion nozzles and the fibers to a first velocity and cooled below their melting point, and subsequently accelerated to a higher velocity by an air jet fed with compressed cold air. The resulting fibers have a high degree of molecular orientation and tenacity and are collected on a moving collecting surface as a non-woven web.

Claims

1. An improved apparatus for producing fibers of a high degree of molecular orientation of the type wherein a fiberforming thermoplastic polymer is formed into a fiber stream and wherein said fibers are collected on a receiver surface in the path of said fiber stream to form a non-woven mat, the improvement of which comprises:

a polymer feed chamber for receiving said molten polymer,

nozzle mounts having a plurality of nozzle means mounted in a spinnerette plate arranged in multiple rows for receiving said molten polymer from said polymer feed chamber for forming fine fiber, and having;

a) a multiplicity of nozzles arranged in at least two rows;

b) a gas cavity having a height of at least two times the outside diameter of said nozzles;

c) a gas plate to receive said nozzles, said gas plate having a hole pattern identical to said nozzle mounts and having holes which are larger than the outside diameter of said nozzles to pass gas from said gas cavity around said nozzles at high velocity to flow and expand parallel to said nozzles having ends protruding through said gas plate and the flow of said fibers exiting said nozzle ends,

d) a jet drawing means, placed at a distance from said nozzles in the path of said fiber stream, receiving said fiber stream, and having air slots directing a flow of high velocity cold air away from said nozzles, said high velocity cold air accelerating said fiber stream away from said nozzles at a high velocity.

2. The apparatus of claim 1 wherein the holes in said gas plate are between 1.05 to 1.3 times the diameter of said nozzles.

3. The apparatus of claim 1 wherein the cross sectional opening for the hot gas to pass through said gas plate around each nozzle is at least 0.2 square millimeter.

4. The apparatus of claim 1 where said jet drawing means is mounted at least six centimeters away from said nozzle ends.

5. The apparatus of claim 4 where said jet drawing means has two air slots between which said fiber stream passes, said air slot having a width of between 0.1 and 3 millimeters.

6. The apparatus of claim 5 where said air slots are at least five millimeters apart.

7. A process for forming a non-woven mat of fibers having high molecular orientation and strength, comprising the steps of:

a) introducing a molten polymer into a feed chamber for receiving said polymer, said feed chamber communicating with a miltiplicity of extruding nozzles means mounted in a spinnerette plate and arranged in multiple rows,

b) extruding the molten polymer through said nozzles to form fine fibers,

c) simultaneously introducing a gas stream into a gas cavity said gas cavity being bounded on one side by said spinnerette plate and bounded on an opposite side by a gas plate and said nozzles pass through said gas chamber and said gas plate having holes in a pattern identical to the pattern of said spinnerette plate in which said nozzles are mounted, said holes having a diameter larger than said nozzles, said nozzles protruding through said holes in said gas plate, said gas is passed around said nozzles through said gas plate at a high velocity so as to flow and expand parallel to said fiber stream and attenuate and cool said molten fibers exiting said nozzles below their melt temperature,

d) fiurther attenuating said fibers by a jet drawing means supplied by pressurized cold air, said jet drawing means being positioned in the path of said fiber stream, receiving said fiber stream and accelerating it to a velocity higher than the gas velocity exiting through the holes of said gas plate,

e) collecting said fibers on a receiver in the path of said fibers to form a non-woven mat.

8. The process of claim 7 where the gas temperature in said gas chamber is between 10 to 60°

C. higher than the melt temperature of said polymer.

9. The process of claim 7 where the gas velocity exiting said gas plate is between 10 and 250 meter per second.

10. The process of claim 7 where the gas exiting said jet drawing means has a velocity of between 50 and 330 meter per second.

11. The process of claim 7 where the gas exiting said jet drawing means has a velocity of at least 20 meter per second higher than the hot gas exiting through said gas plate holes around said nozzles.