Slurry granulation-steam stripping process for solvent removal

Claim 2

A continuous process for recovering a thermoplastic polycarbonate or polyphenylene oxide resin from a solution of said resin in a solvent comprising introducing said solution into a first vessel through atomizing means along with steam, below the surface of the liquid contained in said first vessel; removing solvent vapor and water vapor overhead resulting in a bottom product water slurry of polymer-solvent granules maintained at about 1 to 50 weight percent solids with makeup hot water; removing said bottom product slurry from said first vessel; removing hot water from said slurry, resulting in polymer granules with absorbed solvent and water introducing said granules along with superheated steam into a second vessel wherein remaining solvent and water are volatilized from said granules while being carried through said second vessel by said superheated steam; separating polymer granules from the steam-solvent vapor mixture using separating means; recycling said steam-solvent vapor mixture for injection to the first vessel for steam jacket heating of the first vessel or for preheating the polymer solution before injection into the first vessel; and recovery granular polymer product from said separating means.

Claim 3

The process of claim 1 wherein polymer granules are reduced in size after recovery from said first vessel and before introduction into said second vessel.

Claim 4

The process of claim 1 wherein the contents of the first vessel are mechanically agitated during operation.

Claim 5

The process of claim 1 wherein the temperature of the first vessel is less than 120° C.

Claim 6

The process of claim 1 wherein the second vessel is maintained at between 125° C. and 250° C.

Claim 7

The process of claim 1 wherein steam and polymer solution are introduced independently through multiple nozzles.

Claim 8

The process of claim 1 wherein the first vessel is maintained at between about 0.1 and 2.0 atmospheres pressure.

Claim 9

The process of claim 1 wherein the second vessel is maintained at between 0.3 and 2.0 atmospheres pressure.

Claim 10

The process of claim 1 wherein the thermoplastic resin is polycarbonate.

Claim 11

The process of claim 1 wherein the solvent is methylene chloride.

Claim 12

The process of claim 1 wherein the thermoplastic resin is polyphenylene oxide.

Claim 13

The process of claim 1 wherein the solvent is toluene.

Claim 14

The process of claim 1 wherein the thermoplastic resin solution contains up to about 50 percent by weight resin.

Claim 15

The process of claim 1 wherein the second vessel is heated by a steam jacket.

Claim 16

The process of claim 1 wherein the first vessel is heated by a steam jacket using recycled steam from said second vessel.

Claim 17

The process of claim 1 wherein the polymer granules are milled to reduce their size between the first and second stages.

Claim 18

A continuous process for recovering polycarbonate resin from a solution of said resin in methylene chloride comprising the following steps: (a) introducing the polycarbonate-methylene chloride solution into a vessel, below the surface of the liquid contained therein, by means of a nozzle to form a dispersion of said solution in water maintained at about 70° C.; (b) removing a mixture of methylene chloride vapor and water vapor as an overhead product from said first vessel, passing said overhead product through a heat exchanger for preheating polycarbonate solution feed and finally passing said overhead product to a methylene chloride recovery apparatus; (c) recovering a bottom product from said first vessel comprising a water slurry of polycarbonate granules containing absorbed methylene chloride and water and passing said bottom product to a centrifugal dewatering stage where hot water is removed for recycling as makeup water and for heating purposes in said first vessel; (d) passing said polycarbonate granules along with superheated steam at 200° C. into a second vessel wherein remaining absorbed methylene chloride and water are volatilized from said polycarbonate granules while being carried through said second vessel; (e) passing said polycarbonate granules along with the steam-methylene chloride vapor mixture from said second vessel into a cyclone separator; (f) recovering said steam-methylene chloride vapor mixture for recycling to said first vessel for recovery of its heating value for steam stripping and for possible preheating of the polycarbonate feed solution entering said first vessel; and (g) recovering said polycarbonate granules from said cyclone separator.

Claim 19

A continuous process for recovering polycarbonate resin from a solution of said resin in methylene chloride comprising the following steps: (a) introducing the polycarbonate-methylene chloride solution into a vessel, below the surface of the liquid contained therein, by means of a nozzle to form a dispersion of said solution in water maintained at about 70° C.; (b) removing a mixture of methylene chloride vapor and water vapor as an overhead product from said first vessel, passing said overhead product through a heat exchanger for preheating polycarbonate solution feed and finally passing said overhead product to a methylene chloride recovery apparatus; (c) recovering a bottom product from said first vessel comprising a water slurry of polycarbonate granules containing absorbed methylene chloride and water and passing said bottom product to a centrifugal dewatering stage where hot water is removed for recycling as makeup water and for heating purposes in said first vessel; (d) passing said polycarbonate granules along with superheated steam at 200° C. into a second vessel wherein remaining absorbed methylene chloride and water are volatilized from said polycarbonate granules while being carried through said second vessel; (e) passing said polycarbonate granules along with the steam-methylene chloride vapor mixture from said second vessel into a cyclone separator; (f) recovering said steam-methylene chloride vapor mixture for recycling to said first vessel for recovery of its heating value for steam stripping and for possible preheating of the polycarbonate feed solution entering said first vessel; and (g) recovering said polycarbonate granules from said cyclone separator.