US4166091A — Production of plexifilament strands

Claim 1

Independent Claim 192 words

In the process for producing plexifilament strands from an organic, synthetic, substantially water-insoluble fiber-forming polymer which either of itself or its water-association complex has a melting point between 100° and 300° C., by flash-extruding the polymer in a volatile liquid at a temperature above the melting point of the polymer into a region of substantially lower temperature and pressure where the liquid flash-vaporizes; the improvement for avoiding the use of organic solvents while providing for extremely rapid spinning which comprises dispersing said polymer in water to form a substantially uniform dispersion containing between about 25 percent and 45 percent by weight of polymer based on the total weight of dispersion, heating the dispersion to a temperature between about 200° C. and about 300° C. to melt the polymer or its water-association complex while maintaining the dispersion uniform and under a pressure at which the water is liquid, the rate of heating being such that the time of heating does not exceed about 30 minutes, and promptly flash-extruding the dispersion in liquid water from an orifice into a region of substantially lower temperature and pressure to form a continuous strand of fibrillated plexifilaments.

Claim 2

Dependent Claim 192 words

In the process for producing plexifilament strands from an organic, synthetic, substantially water-insoluble fiber-forming polymer which either of itself or its water-association complex has a melting point between 100° and 300° C., by flash-extruding the polymer in a volatile liquid at a temperature above the melting point of the polymer into a region of substantially lower temperature and pressure where the liquid flash-vaporizes; the improvement for avoiding the use of organic solvents while providing for extremely rapid spinning which comprises dispersing said polymer in water to form a substantially uniform dispersion containing between about 25 percent and 45 percent by weight of polymer based on the total weight of dispersion, heating the dispersion to a temperature between about 200° C. and about 300° C. to melt the polymer or its water-association complex while maintaining the dispersion uniform and under a pressure at which the water is liquid, the rate of heating being such that the time of heating does not exceed about 30 minutes, and promptly flash-extruding the dispersion in liquid water from an orifice into a region of substantially lower temperature and pressure to form a continuous strand of fibrillated plexifilaments.

Claim 3

Dependent Claim 43 words

The process of claim 1, wherein said dispersion contains between about 1 percent and 25 percent by weight, based on the weight of the polymer, of a water-insoluble nucleating agent stabilizer selected from the group consisting of alumina, silica, titania, and inorganic silicates.

Claim 4

Dependent Claim 27 words

The process of claim 1, wherein said dispersion contains between about 30 percent and 45 percent by weight of polymer based on the total weight of dispersion.

Claim 5

Dependent Claim 21 words

The process of claim 3, wherein said dispersion is heated to a temperature between about 240° C. and about 290° C.

Claim 6

Dependent Claim 20 words

The process of claim 4, wherein said dispersion is heated under a pressure between about 500 and about 1500 psig.

Claim 7

Dependent Claim 28 words

The process of claim 5, wherein the dispersion contains between about 3 percent and 25 percent by weight of aluminum silicate, based on the weight of the polymer.

Claim 8

Dependent Claim 26 words

The process of claim 5 wherein the dispersion contains between about 3 percent and 25 percent by weight of silica, based on the weight of polymer.

Claim 9

Dependent Claim 186 words

In the process for producing plexifilament strands from polyacrylonitrile or copolymers of acrylonitrile and monoethylenically unsaturated monomers copolymerizable with acrylonitrile, by flash-extruding the polymer in a volatile liquid at a temperature above the melting point of the polymer into a region of substantially lower temperature and pressure where the liquid flash-vaporizes; the improvement for avoiding the use of organic solvents while providing for extremely rapid spinning which comprises dispersing an acrylonitrile polymer, either itself or its water-association complex having a melting point between 100° C. and 300° C., in water to form a substantially uniform dispersion containing between about 25 percent and 45 percent by weight of polymer based on the total weight of dispersion, heating the dispersion to a temperature between about 200° C. and 300° C. while maintaining the dispersion uniform and under a pressure at which the water is a liquid, the rate of heating being such that the time of heating does not exceed about 30 minutes, and promptly flash-extruding the dispersion from an orifice into a region of substantially lower temperature and pressure to form a continuous strand of fibrillated plexifilaments.

Claim 10

Dependent Claim 186 words

In the process for producing plexifilament strands from polyacrylonitrile or copolymers of acrylonitrile and monoethylenically unsaturated monomers copolymerizable with acrylonitrile, by flash-extruding the polymer in a volatile liquid at a temperature above the melting point of the polymer into a region of substantially lower temperature and pressure where the liquid flash-vaporizes; the improvement for avoiding the use of organic solvents while providing for extremely rapid spinning which comprises dispersing an acrylonitrile polymer, either itself or its water-association complex having a melting point between 100° C. and 300° C., in water to form a substantially uniform dispersion containing between about 25 percent and 45 percent by weight of polymer based on the total weight of dispersion, heating the dispersion to a temperature between about 200° C. and 300° C. while maintaining the dispersion uniform and under a pressure at which the water is a liquid, the rate of heating being such that the time of heating does not exceed about 30 minutes, and promptly flash-extruding the dispersion from an orifice into a region of substantially lower temperature and pressure to form a continuous strand of fibrillated plexifilaments.

Claim 11

Dependent Claim 43 words

The process of claim 8, wherein the dispersion contains between about 3 percent and 25 percent by weight, based on the weight of the polymer, of a water-insoluble nucleating agent stabilizer selected from the group consisting of alumina, silica, titania, and inorganic silicates.

Claim 12

Dependent Claim 27 words

The process of claim 9, wherein said dispersion contains between about 30 percent and 45 percent by weight of polymer based on the total weight of dispersion.

Claim 13

Dependent Claim 21 words

The process of claim 10, wherein said dispersion is heated to a temperature between about 240° C. and about 290° C.

Claim 14

Dependent Claim 18 words

The process of claim 11, wherein the pH of the dispersion is adjusted to make the dispersion acidic.

Claim 15

Dependent Claim 26 words

The process of claim 12, wherein the dispersion contains between 10 percent and 15 percent by weight of aluminum silicate, based on the weight of polymer.

Claim 16

Dependent Claim 25 words

The process of claim 12, wherein the dispersion contains between 10 percent and 15 percent by weight of silica, based on the weight of polymer.

Annuity Stage	Window Opens	Payment Deadline	Surcharge Period Until	Estimated Fee	Status
3.5 Years (Year 4)	1982-08-27	1983-02-26	1983-08-28	$2000.00	Window Closed / Lapsed
7.5 Years (Year 8)	1986-08-27	1987-02-26	1987-08-28	$3760.00	Window Closed / Lapsed
11.5 Years (Year 12)	1990-08-27	1991-02-26	1991-08-28	$7700.00	Window Closed / Lapsed

Production of plexifilament strands

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