Process for preparing polymer powders

Claim 2

A process for preparing powders of thermoplastic polymers comprising dissolving 1 to 40 weight percent of thermoplastic polymer in a solvent of paraffin or cycloparaffin hydrocarbons having 5 to 12 carbon atoms at a temperature greater than 100° C up to about 165° C under autogenous conditions, cooling said solution under autogenous conditions to a temperature less than 90° C, subjecting said solution during said cooling to high shear agitation to produce particulate polymer, said high shear agitation being characterized by turbine agitators in a vessel being 1/3 to 2/3 the diameter of the vessel operated at from 20 to 300 rpm's and being rotated with 0.5 to 10 horse power per 1000 gallons of material agitated, short of emulsification to produce particulate polymer, precipitating said thermoplastic polymer during said cooling and high shear agitation, recovering a slurry of polymer particles and solvent, atomizing said slurry into a vaporization zone, feeding a drying gas at a temperature in the range of 80 to 180° C into said vaporization zone and recovering particulate polymer product having a substantial amount of said solvent removed therefrom.

Claim 3

The process according to claim 1 wherein the temperature of said solution is adjusted to maintain an autogenous pressure of less than 100 psig.

Claim 4

The process according to claim 2 wherein said autogenous pressure is maintained at less than 50 psig.

Claim 5

The process according to claim 1 wherein said solvent is n-pentane, isopentane, isooctane, cyclohexane, methylcyclohexane, heptane, nonane or mixtures thereof.

Claim 6

The process according to claim 1 wherein the solvent is n-heptane.

Claim 7

The process according to claim 1 wherein the temperature of the drying gas is adjusted to maintain the temperature in the vaporization zone in the range of 30° to 80° C.

Claim 8

The process according to claim 6 wherein the drying gas has a temperature in the range of 90° to 160° C.

Claim 9

The process according to claim 6 wherein the drying gas is an inert gas.

Claim 10

The process according to claim 8 wherein the drying gas is nitrogen.

Claim 11

The process according to claim 1 wherein at least 5 weight % of said polymer is dissolved in said solvent.

Claim 12

The process according to claim 10 wherein said precipitating is continued until the amount of thermoplastic left in solution produces a viscosity in the solvent no greater than 5 centipoise at the temperature of atomization.

Claim 13

The process according to claim 1 wherein said recovered particulate polymer is dried to produce a powder, having substantially all of the particles thereof less than 100 microns.

Claim 14

The process according to claim 1 wherein said slurry is atomized through a centrifugal atomizer.

Claim 15

A process for preparing fine free flowing powders of thermoplastic polymers comprising dissolving 5 to 20 weight % of said thermoplastic resin in a solvent of paraffin or cycloparaffin hydrocarbons having 5 to 12 carbon atoms at temperatures in the range of 100° to 140° C under autogenous pressure, cooling said solution under autogenous pressure to a temperature of below 90° C, intensely agitating said cooling solution to provide high shear conditions therein, said high shear agitation being characterized by turbine agitators in a vessel being 1/3 to 2/3 the diameter of the vessel operated at from 20 to 300 rpm's and being rotated with 0.5 to 10 gallons of material agitated, short of emulsification to produce particulate polymer, continuing said cooling to a temperature and for a sufficient period of time to precipitate said polymer and to leave less than the amount of said polymer in solution which will inhibit formation of droplets during atomization and drying, recovering a slurry of particulate polymer and solvent, atomizing said slurry through an atomizer into a vaporization zone, adding drying gas to said vaporization zone at a temperature in the range of 90° to 160° C and at a rate to maintain the temperature of said vaporization zone in the range of 30° to 80° C, recovering a partially dry particulate polymer material from said vaporization zone, drying said partially dry particulate polymer material and recovering a powder, wherein said solvent has a vapor pressure of 50 to 400 mm of mercury at the temperature of said vaporization zone and said amount of polymer in solution is that amount which produces a viscosity in said solvent of no greater than 5 centipoise at the temperature of atomization.

Claim 16

A process for preparing fine free flowing powders of thermoplastic polymers comprising dissolving 5 to 20 weight % of said thermoplastic resin in a solvent of paraffin or cycloparaffin hydrocarbons having 5 to 12 carbon atoms at temperatures in the range of 100° to 140° C under autogenous pressure, cooling said solution under autogenous pressure to a temperature of below 90° C, intensely agitating said cooling solution to provide high shear conditions therein, said high shear agitation being characterized by turbine agitators in a vessel being 1/3 to 2/3 the diameter of the vessel operated at from 20 to 300 rpm's and being rotated with 0.5 to 10 gallons of material agitated, short of emulsification to produce particulate polymer, continuing said cooling to a temperature and for a sufficient period of time to precipitate said polymer and to leave less than the amount of said polymer in solution which will inhibit formation of droplets during atomization and drying, recovering a slurry of particulate polymer and solvent, atomizing said slurry through an atomizer into a vaporization zone, adding drying gas to said vaporization zone at a temperature in the range of 90° to 160° C and at a rate to maintain the temperature of said vaporization zone in the range of 30° to 80° C, recovering a partially dry particulate polymer material from said vaporization zone, drying said partially dry particulate polymer material and recovering a powder, wherein said solvent has a vapor pressure of 50 to 400 mm of mercury at the temperature of said vaporization zone and said amount of polymer in solution is that amount which produces a viscosity in said solvent of no greater than 5 centipoise at the temperature of atomization.

Claim 17

The process according to claim 14 wherein the polymer comprises grafted polyolefins.

Claim 18

The process according to claim 15 wherein the said grafted polyolefin is acrylic acid grafted.

Claim 19

The process according to claim 15 wherein the said grafted polyolefin is glycidyl acrylate grafted.

Claim 20

A process for preparing powders of thermoplastic polymer comprising dissolving 1 to 40 weight percent of thermoplastic polymer in a solvent of paraffin or cycloparaffin hydrocarbons having 5 to 12 carbon atoms at a temperature greater than 100° C up to about 165° C under autogenous conditions, cooling said solution under autogenous conditions to a temperature less than 90° C, subjecting said solution during said cooling to high shear agitation, precipitating said thermoplastic polymer during said cooling and high shear agitation, said high shear agitation being characterized by turbine agitators in a vessel being 1/3 to 2/3 the diameter of the vessel, operated at from 200 to 300 rpm's and being rotated with 0.5 to 10 horse power per 1000 gallons of material agitated, short of emulsification to produce particulate polymer, recovering a slurry of polymer particles and solvent, atomizing said slurry into a vaporization zone, feeding a drying gas at a temperature in the range of 80 to 180° C into said vaporization zone, and recovering particulate polymer product having a substantial amount of said solvent removed therefrom.

Claim 21

A process for preparing powders of thermoplastic polymer comprising dissolving 1 to 40 weight percent of thermoplastic polymer in a solvent of paraffin or cycloparaffin hydrocarbons having 5 to 12 carbon atoms at a temperature greater than 100° C up to about 165° C under autogenous conditions, cooling said solution under autogenous conditions to a temperature less than 90° C, subjecting said solution during said cooling to high shear agitation, precipitating said thermoplastic polymer during said cooling and high shear agitation, said high shear agitation being characterized by turbine agitators in a vessel being 1/3 to 2/3 the diameter of the vessel, operated at from 200 to 300 rpm's and being rotated with 0.5 to 10 horse power per 1000 gallons of material agitated, short of emulsification to produce particulate polymer, recovering a slurry of polymer particles and solvent, atomizing said slurry into a vaporization zone, feeding a drying gas at a temperature in the range of 80 to 180° C into said vaporization zone, and recovering particulate polymer product having a substantial amount of said solvent removed therefrom.