Process for producing polycarbonate resin particles

Claim 2

A process for producing polycarbonate resin particles from a methylene chloride solution of a polycarbonate resin obtained by the polycondensation of a dihydroxydiaryl compound and phosgene, which comprises: continuously supplying said methylene chloride solution of polycarbonate resin into a particle-forming vessel further containing an agitated aqueous medium consisting of a suspension of polycarbonate resin particles; heating the agitated mixture while maintaining the same in a suspended state to effect evaporation of methylene chloride, thereby resulting in the formation of polycarbonate resin particles; subjecting at least a portion of the resulting aqueous slurry withdrawn from the particle-forming vessel which contains the polycarbonate resin particles, to a wet pulverization treatment; and recycling at least a portion of the pulverized polycarbonate resin particles to the particle-forming vessel.

Claim 3

The process according to claim 1, wherein the particle-forming vessel is maintained at a temperature of from 37° to 60° C. for the evaporation of methylene chloride.

Claim 4

The process according to claim 1, wherein the methylene chloride solution of the polycarbonate resin is preheated to a temperature of from 37° to 150° C. before it is supplied to the particle-forming vessel.

Claim 5

The process according to claim 1, wherein the amount of the polycarbonate resin particles in the aqueous slurry in the particle-forming vessel is from 5 to 50% by weight relative to the aqueous slurry.

Claim 6

The process according to claim 1, wherein the amount of the polycarbonate resin particles recycled to the particle-forming vessel is from 50 to 99.5% by weight of the total polycarbonate resin particles withdrawn from the particle-forming vessel.

Claim 7

A process for producing polycarbonate resin particles from a methylene chloride solution of a polycarbonate resin obtained by the polycondensation of a dihydroxydiaryl compound and phosgene, which comprises: continuously supplying said methylene chloride solution of said polycarbonate resin and water into a preconditioning vessel under agitation conditions to form a mixture of an oil-in-water type suspension; continuously supplying the mixture to a particle-forming vessel with the contents of the vessel being agitated; heating the agitated mixture in the suspended state to evaporate methylene chloride, thereby forming an aqueous slurry containing polycarbonate resin particles; subjecting at least a portion of the resulting aqueous slurry withdrawn from the particle-forming vessel, which contains the polycarbonate resin particles, to a wet pulverization treatment; and recycling at least a portion of the pulverized polycarbonate resin particles to the particle-forming vessel.

Claim 8

A process for producing polycarbonate resin particles from a methylene chloride solution of a polycarbonate resin obtained by the polycondensation of a dihydroxydiaryl compound and phosgene, which comprises: continuously supplying said methylene chloride solution of said polycarbonate resin and water into a preconditioning vessel under agitation conditions to form a mixture of an oil-in-water type suspension; continuously supplying the mixture to a particle-forming vessel with the contents of the vessel being agitated; heating the agitated mixture in the suspended state to evaporate methylene chloride, thereby forming an aqueous slurry containing polycarbonate resin particles; subjecting at least a portion of the resulting aqueous slurry withdrawn from the particle-forming vessel, which contains the polycarbonate resin particles, to a wet pulverization treatment; and recycling at least a portion of the pulverized polycarbonate resin particles to the particle-forming vessel.

Claim 9

A process for producing polycarbonate resin particles from a methylene chloride solution of a polycarbonate resin obtained by the polycondensation of a dihydroxydiaryl compound and phosgene, which comprises: continuously supplying said methylene chloride solution of the polycarbonate resin into a particle-forming vessel further containing an agitated aqueous medium consisting of a suspension of polycarbonate resin particles; heating the agitated mixture while maintaining the same in a suspended state in order to evaporate methylene chloride, thereby resulting in the formation of an aqueous slurry containing polycarbonate resin particles; subjecting at least a portion of the resulting aqueous slurry withdrawn from the particle-forming vessel, which contains the polycarbonate resin particles, to a wet pulverization treatment; recycling at least a portion of the slurry containing the pulverized particles to the particle-forming vessel; introducing the remainder of the aqueous slurry containing pulverized particles to an evaporation vessel; and heating said remainder of said aqueous slurry to a temperature higher than the temperature of the particle-forming vessel to complete the evaporation of methylene chloride from the polycarbonate resin particles.

Claim 10

A process for producing polycarbonate resin particles from a methylene chloride solution of a polycarbonate resin obtained by the polycondensation of a dihydroxydiaryl compound and phosgene, which comprises: continuously supplying said methylene chloride solution of the polycarbonate resin into a particle-forming vessel further containing an agitated aqueous medium consisting of a suspension of polycarbonate resin particles; heating the agitated mixture while maintaining the same in a suspended state in order to evaporate methylene chloride, thereby resulting in the formation of an aqueous slurry containing polycarbonate resin particles; subjecting at least a portion of the resulting aqueous slurry withdrawn from the particle-forming vessel, which contains the polycarbonate resin particles, to a wet pulverization treatment; recycling at least a portion of the slurry containing the pulverized particles to the particle-forming vessel; introducing the remainder of the aqueous slurry containing pulverized particles to an evaporation vessel; and heating said remainder of said aqueous slurry to a temperature higher than the temperature of the particle-forming vessel to complete the evaporation of methylene chloride from the polycarbonate resin particles.

Claim 11

The process of claim 1, wherein the concentration of polycarbonate resin in said methylene chloride solution ranges from 3 to 35% by weight.

Claim 12

The process of claim 1, wherein the pulverization treatment prepares polycarbonate resin particles of a size ranging from 0.1 to 4 mm.

Claim 13

The process of claim 6, wherein the volume ratio of methylene chloride solution to water in said preconditioning vessel ranges from 1:0.1-4.

Claim 14

The process of claim 10, wherein said ratio ranges from 1:0.2-3.

Claim 15

The process of claim 6, wherein the temperature within said preconditioning vessel ranges from 37° to 60° C., and the temperature within said particle-forming vessel is within the same range.

Claim 16

The process of claim 6, wherein said wet pulverization results in polycarbonate resin particles of a size ranging from 0.1 to 4 mm.

Claim 17

The process of claim 7, wherein the temperature within said evaporation vessel is within the range of 60° to 100° C.