# US 4,399,084 A · Process for producing a fibrous assembly

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- Number: US 4,399,084 A
- Document ID: US4399084A
- Status: Granted
- Kind: A
- Application number: 06/293,269
- Filed: 1981-08-17
- Granted: 1983-08-16
- Earliest claimed: 1980-08-18
- Assignees: Teijin Limited
- Inventors: Yasuhiko Sagawa; Susumu Norota; Tsutomu Kiriyama; Shingo Emi; Tadasi Imoto; Tetsuo Yamauchi
- Web page: https://patentgrep.com/patent/US4399084A

## CPC

- D01D 5/20: with varying denier along their length
- D01D 4/02: Spinnerettes (alloys therefor C22C)
- D01D 5/088: Cooling filaments, threads or the like, leaving the spinnerettes
- D01F 6/605: {from aromatic polyamides}
- D01D: MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01F: CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS

## Abstract

The present invention provides a process for producing a fibrous assembly, which comprises extruding a melt of a fiber-forming polymer through a mesh spinneret, said spinneret including many closely arranged small openings and having an opening ratio (.alpha.), represented by the following formula, of at least about 10% ##EQU1## V.sub.a is the total apparent volume of the spinneret which is taken within a unit area of its mesh portion, and V.sub.f is the total volume of partitioning members defining the small openings which is taken within a unit area of the mesh portion of the spinneret; said extrusion being carried out while generating Joule heat in the partitioning members of the spinneret and cooling the vicinity of the extrusion surface of the spinneret by supplying a cooling fluid, whereby the melt is stably converted into fine streams by the partitioning members; and taking up and solidifying the fine streams; and also provides the process wherein the extrusion surface of the spinneret is turned upward so that the normal vector of the extruding surface is reverse to the direction of gravity, and the fine streams extruded from the extrusion surface are taken up against gravity. The present invention provides a molding apparatus for production of a fibrous assembly having a mesh spinneret which has many closely arranged small openings having an opening ratio .alpha. defined by the above formula of at least 10% and the extrusion surface of the spinneret being turned upwardly such that the normal vector of the extrusion surface is reverse to the direction of gravity.

## Claims

### Claim 1

A process for producing a fibrous assembly, which comprises extruding a melt of a fiber-forming polymer through a mesh spinneret, said spinneret including many closely arranged small openings and having an opening ratio (.alpha.), represented by the following formula, of at least about 10% ##EQU9## V.sub.a (cm.sup.3) is the total apparent volume of the spinneret which is taken within one square centimeter of the mesh portion of the spinneret, and V.sub.f (cm.sup.3) is the total volume of partitioning members defining the small openings which is taken within one square centimeter of the mesh portion of the spinneret; said extrusion being carried out while generating Joule heat in the partitioning members of the spinneret and cooling the vicinity of the extrusion surface of the spinneret by supplying a cooling fluid, whereby the melt is stably converted into fine streams by the partitioning members; and taking up and solidifying the fine streams.

### Claim 2 (depends on 1)

The process of claim 1 wherein the mesh spinneret is a mesh spinneret having many small openings defined by partitioning members of small width having elevations and depressions on its extrusion surface, said small openings being such that the polymer melt extruded through one small opening of the spinneret can move toward and away from the polymer melt extruded from an other small opening adjacent to said one opening or vice versa through depressions of the partitioning members.

### Claim 3 (depends on 1)

The process of claim 1 wherein the mesh spinneret has an opening ratio (.alpha.) of about 20 to about 90%.

### Claim 4 (depends on 1)

The process of claim 1 wherein the number of the small openings per cm.sup.2 of the extrusion surface is at least about 5.

### Claim 5 (depends on 4)

The process of claim 4 wherein the number of the small openings per cm.sup.2 of the extrusion surface is about 10 to about 10,000.

### Claim 6 (depends on 1)

The process of claim 1 wherein the mesh portion of the mesh spinneret has a thickness of not more than about 5 mm.

### Claim 7 (depends on 1)

The process of claim 1 wherein Joule heat is generated electrically at the partitioning members of the mesh portion of the spinneret.

### Claim 8 (depends on 1)

The process of claim 1 wherein the amount of electricity passed is about 0.5 to about 5,000 watts per cm.sup.2 of the mesh portion of the spinneret.

### Claim 9 (depends on 1)

The process of claim 1 wherein a melt of the fiber-forming polymer is supplied to the mesh spinneret and extruded through the small openings defined by the partitioning members which generate Joule heat.

### Claim 10 (depends on 1)

The process of claim 1 wherein a solid powder of the fiber-forming polymer is fed into the mesh spinneret, and while melting the solid powder by the heat given by the partitioning members generating Joule heat, the molten polymer is extruded through the small openings defined by the partitioning members.

### Claim 11 (depends on 1)

The process of claim 1 wherein the molten fiber-forming polymer is extruded from the spinneret while supplying Joule heat from the partitioning members of the mesh portion such that the temperature of the molten fiber-forming polymer becomes maximum near that surface of the mesh spinneret which is opposite to the extrusion surface of the mesh portion, and while cooliing the vicinity of the extruding surface of the spinneret by supplying a cooling fluid.

### Claim 12 (depends on 1)

The process of claim 1 wherein the amount of the molten fiber-forming polymer extruded is about 0.1 to about 20 g min. per cm.sup.2 of the mesh spinneret.

### Claim 13 (depends on 1)

The process of claim 1 wherein the extrusion surface of the spinneret is turned upward so that the normal vector of the extruding surface is reverse to the direction gravity, and the fine streams extruded from the extrusion surface are taken up against gravity.

### Claim 14 (depends on 13)

The process of claim 13 wherein the fine streams extruded from the extruding surface are taken up in a direction normal to the extruding surface, or in a direction which is deviated by an angle of at most about 30 degrees from the normal direction of the extruding surface.

### Claim 15 (depends on 1)

A process for producing a drawn fibrous assembly, which comprises passing the undrawn fibrous assembly obtained by the process of claim 1 over a frictional guide, and taking it up at a speed higher than the speed at which it is passed over the guide.

### Claim 16 (depends on 15)

The process of claim 15 wherein the taking up of the fibrous assembly is carried out after it has been passed through a heating zone and drawn substantially in the heating zone.