Preparation of thermoplastic polymer fibrilla and fibril

Claim 2

A process for preparing solid thermoplastic polymer fibrilla or fibril comprising: (a) discharging through a discharge means a two phase mixture of a thermoplastic polymer selected from the group consisting of low density polyethylene, medium density polyethylene, high density polyethylene, isotactic or syndiotactic polypropylene, isotactic polystyrene poly-4-methylpentene-1 and polybutene-1 or a blend of two or more such polymers and a solvent selected from the group consisting of pentane, hexane, cyclohexane, dichloromethane, methylchloride, trichlorotrifluoroethane, trichlorofluoromethane and mixtures thereof, where (1) the discharging is from a zone of both an elevated temperature and pressure range to a zone of lower temperature and pressure, (2) the elevated temperature range causes the formation of the two-phase mixture and maintains the two-phase mixture prior to discharge and after discharging permits vaporization of the solvent to cool the polymer to a temperature below the freezing point of the polymer, (3) the differences between both the elevated temperature and pressure range and both the lower temperature and pressure are effective to cause rapid evaporation of the solvent after the discharging, (4) one phase of the mixture is a polymer-rich phase and the other phase is a solvent-rich phase and concentrations between the two phases are in general equilibrium with each other, (5) the polymer is soluble in the solvent at a temperature above the polymer's melting point but is essentially insoluble in the solvent at a temperature below about the freezing point of the polymer; (b) and the mixture flowing has a Reynolds, Re, of less than 2 × 10 3 , and the means has a ratio of length of internal diameter, L/D, in the range between from about 0.5 to about 100 and that the relationship between the Re, L/D, polymer and solvent is such that according to the following equation: mean fibril length = 0.9122 (L/D) .sup.-0.0498 + 489.5(Re).sup.-1 (L/D) .sup.-0.2619 the resulting mean fibril length is between from about 0.8 millimeters to about 2.9 millimeters.

Claim 3

Process according to claim 1 wherein the standard deviation, υ, is related to the mean fibril length, μ according to the following equation: (υ).sup.0.740 = μ/[2.361-0.00060(Re)-0.0163 L/D ] and the resulting standard deviation of the fibril length distribution is between from about 0.4 millimeters to about 1.5 millimeters.

Claim 4

Process according to claim 1 wherein essentially none of the following are formed: plexifilaments, spherical particles and relatively large masses of non-filamentous foamed material.

Claim 5

Process according to claim 1 wherein the discharging means is a nozzle or orifice.

Claim 6

Process according to claim 4 wherein the mean fibril length is between from about 1 millimeter to about 2.5 millimeters.

Claim 7

In the process for preparing solid thermoplastic polymer fibrilla or fibril wherein a two phase mixture of a thermoplastic polymer or a blend of two or more such polymers and a solvent is discharged through discharging means having a ratio of length to internal diameter ratio, L/D, between from about 0.5 to 100, and wherein the mixture is discharged from a zone of both an elevated temperature and pressure range to a zone of lower temperature and pressure, and the elevated temperature range causes the formation of the two-phase mixture and maintains the two-phase mixture prior to discharge and after discharging permits vaporization of the solvent to cool the polymer to a temperature below the freezing point of the polymer, and the differences between both the elevated temperature and pressure range and both the lower temperature and pressure are effective to cause rapid evaporation of the solvent after the discharging, and wherein one phase of the mixture is a polymer-rich phase and the other phase is a solvent-rich phase and concentrations between the two phases are in general equilibrium with each other and wherein the polymer is soluble in the solvent at a temperature above the polymer's melting point but is essentially insoluble in the solvent at a temperature below about the freezing point of the polymer and whereby the formed solid thermoplastic polymer fibrilla or fibril is essentially free of solvent and has a mean length which makes it useful for mixing with cellulosic pulp, the improvement comprises that the thermoplastic polymer is selected from the group consisting of low density polyethylene, medium density polyethylene, high density polyethylene, isotactic or syndiotactic polypropylene, isotacticpolystyrene, poly-4-methylpentene-1 and polybutene-1 or a mixture thereof and the solvent is selected from the group consisting of pentane, hexane, cyclohexane, dichloromethane, methylchloride, trichlorotrifluoroethane, trichlorofluoromethane and mixtures thereof and that the Reynolds Number, Re, of the flowing mixture is less than 2 × 10 3 and the ratio of length to internal diameter, L/D, of the discharge means are such that according to the following equation; mean fibril length = 0.9122 (L/D) .sup.-0.0498 + 489.5(Re) .sup.-1 (L/D) -0.2619 the resulting mean fibril length is between from about 0.8 millimeters to about 2.9 millimeters.

Claim 8

In the process for preparing solid thermoplastic polymer fibrilla or fibril wherein a two phase mixture of a thermoplastic polymer or a blend of two or more such polymers and a solvent is discharged through discharging means having a ratio of length to internal diameter ratio, L/D, between from about 0.5 to 100, and wherein the mixture is discharged from a zone of both an elevated temperature and pressure range to a zone of lower temperature and pressure, and the elevated temperature range causes the formation of the two-phase mixture and maintains the two-phase mixture prior to discharge and after discharging permits vaporization of the solvent to cool the polymer to a temperature below the freezing point of the polymer, and the differences between both the elevated temperature and pressure range and both the lower temperature and pressure are effective to cause rapid evaporation of the solvent after the discharging, and wherein one phase of the mixture is a polymer-rich phase and the other phase is a solvent-rich phase and concentrations between the two phases are in general equilibrium with each other and wherein the polymer is soluble in the solvent at a temperature above the polymer's melting point but is essentially insoluble in the solvent at a temperature below about the freezing point of the polymer and whereby the formed solid thermoplastic polymer fibrilla or fibril is essentially free of solvent and has a mean length which makes it useful for mixing with cellulosic pulp, the improvement comprises that the thermoplastic polymer is selected from the group consisting of low density polyethylene, medium density polyethylene, high density polyethylene, isotactic or syndiotactic polypropylene, isotacticpolystyrene, poly-4-methylpentene-1 and polybutene-1 or a mixture thereof and the solvent is selected from the group consisting of pentane, hexane, cyclohexane, dichloromethane, methylchloride, trichlorotrifluoroethane, trichlorofluoromethane and mixtures thereof and that the Reynolds Number, Re, of the flowing mixture is less than 2 × 10 3 and the ratio of length to internal diameter, L/D, of the discharge means are such that according to the following equation; mean fibril length = 0.9122 (L/D) .sup.-0.0498 + 489.5(Re) .sup.-1 (L/D) -0.2619 the resulting mean fibril length is between from about 0.8 millimeters to about 2.9 millimeters.