Abstract A process for preparing acrylonitrile polymer plexifilamentary strands comprises dispersing in water 25 to 45% by weight of an acrylic polymer containing at least 91% by weight acrylonitrile units and up to 9% by weight of one or more copolymeric units and having an intrinsic viscosity of 0.6 to 2.0, 7 to 23 μeq./g. enolizable groups after mild acid treatment, 15 to 70 μeq./g. thioether ends derived from a water insoluble mercaptan and less than 3 μeq./g. oxidizable hydrolysis fragments, heating the dispersion to a temperature of 200° to 300° C. while maintaining the dispersion under sufficient pressure to maintain the water in the liquid state, the time of heating not exceeding about 30 minutes, and promptly flash-extruding the dispersion through an orifice into a region of substantially lower temperature and pressure to form a continuous strand of filbrillated plexifilaments.
Process for producing plexifilament strands of an acrylonitrile polymer which comprises dispersing in water 25 to 45% by weight of an acrylonitrile polymer containing at least 91% by weight acrylonitrile units and up to 9% by weight copolymeric units having an intrinsic viscosity of 0.6 to 2.0, 7 to 23 μeq./g. enolizable groups after mild acid treatment, 15 to 70 μeq./g. thioether ends derived from a water insoluble mercaptan and less than 3 μeq./g. oxidizable hydrolysis fragments, heating the dispersion to a temperature of 200° to 300° C. while maintaining the dispersion under sufficient pressure to maintain the water in the liquid state, the time of such heating not exceeding about 30 minutes, and promptly flash-extruding the dispersion through an orifice into a region of substantially lower temperature and pressure to form a continuous strand of fibrillated plexifilaments.
Claim 2
Dependent Claim
138 words
Process for producing plexifilament strands of an acrylonitrile polymer which comprises dispersing in water 25 to 45% by weight of an acrylonitrile polymer containing at least 91% by weight acrylonitrile units and up to 9% by weight copolymeric units having an intrinsic viscosity of 0.6 to 2.0, 7 to 23 μeq./g. enolizable groups after mild acid treatment, 15 to 70 μeq./g. thioether ends derived from a water insoluble mercaptan and less than 3 μeq./g. oxidizable hydrolysis fragments, heating the dispersion to a temperature of 200° to 300° C. while maintaining the dispersion under sufficient pressure to maintain the water in the liquid state, the time of such heating not exceeding about 30 minutes, and promptly flash-extruding the dispersion through an orifice into a region of substantially lower temperature and pressure to form a continuous strand of fibrillated plexifilaments.
Claim 3
Dependent Claim
12 words
Process of claim 1 wherein the intrinsic viscosity is 0.8 to 1.5.
Claim 4
Dependent Claim
12 words
Process of claim 1 wherein the intrinsic viscosity is 0.9 to 1.1.