Process for the preparation of polymers from polymer slurries

1. A process for purifying a high molecular weight (Mw) polymer in a reaction mass containing less than 20% by weight of contaminants, after the reaction mass is discharged from a polymerization reactor, the process comprising the steps of,

(1) feeding the reaction mass including the polymer having (Mw/Mc)>1, wherein Mc is the critical molecular weight of entanglement, and unwanted contaminants to a disentangling means;

(2) extensively shear-thinning the reaction mass to produce modified polymer in a shear-thinned reaction mass until the polymer in the reaction mass has a viscosity at least 5% lower than that of the polymer fed to the inlet;

(3) feeding the sheer-thinned reaction mass including modified polymer to a polymer recovering means;

(4) removing the unwanted contaminants; and,

(5) recovering decontaminated, modified, undegraded, substantially pure polymer having a melt flow index at least 10% lower than that of unmodified polymer, and, having substantially the same molecular weight Mw as that of the polymer before it is modified.

2. A process for purifying a high molecular weight (Mw) polymer in a reaction mass containing in excess of about 20% by weight of contaminants, after the reaction mass is discharged from a polymerization reactor, comprising the steps of:

(1) feeding the reaction mass including the polymer having (Mw/Mc)>1, wherein Mc is the critical molecular weight of entanglement, and unwanted contaminants including solvent(s), unreacted monomer(s) and byproduct(s), to a pretreatment means to yield pretreated polymer in a pretreated stream;

(2) feeding the pretreated stream to a disentangling means;

(3) extensively shear-thinning the pretreated stream to produce modified polymer in a shear-thinned reaction mass until the polymer in the pretreated stream has a viscosity at least 5% lower than that of the polymer fed to the inlet;

(4) feeding the sheer-thinned pretreated stream including modified polymer to a polymer recovering means;

(5) removing remaining unwanted contaminants; and,

(6) recovering decontaminated, undegraded, modified substantially pure polymer having a melt flow index at least 10% lower than that of unmodified polymer, and, substantially the same molecular weight as that of the unmodified polymer.

3. A process for purifying a high molecular weight (Mw) polymer in a reaction mass containing in excess of about 20% by weight of contaminants, after the reaction mass is discharged from a polymerization reactor, comprising the steps of:

(1) feeding the reaction mass including polymer having (Mw/Mc)>1, wherein Mc is the critical molecular weight of entanglement, and having at least one reactive chain end, unreacted monomer(s) and unwanted contaminants including solvent(s), and byproduct(s), to a disentangling means;

(2) extensively shear-thinning the reaction mass to produce modified polymer having a viscosity at least 10% lower than that of the polymer fed to the inlet, and, concurrently removing unwanted volatile contaminants from within the disentangling means through vents therein;

(3) feeding shear-thinned reaction mass to a polymer-recovering means; and,

(4) recovering devolatilized substantially pure modified polymer having a melt flow index at least 10% lower than that of unmodified polymer, and, substantially the same molecular weight as that of the polymer before it is modified.

4. A process for purifying a polymer comprising the steps of:

(1) providing a reaction mass from a polymerization reactor, said reaction mass comprising a polymer and contaminants;

(2) feeding the reaction mass to a processor;

(3) extensively shear-thinning the reaction mass to produce a modified polymer by reducing the viscosity of the polymer; and

(4) recovering modified polymer.

5. The process of claim 4 , wherein in the recovering step the recovered modified polymer has a melt flow index at least 5% lower than the melt flow index of the polymer before it is modified.

6. The process of claim 4 , wherein in the recovering step the recovered modified polymer has a melt flow index at least 10% lower than the melt flow index of the polymer before it is modified.

7. The process of claim 4 , wherein the polymer in said reaction mass has a Mw/Mc≧1.

8. The process of claim 4 , wherein the polymer in said reaction mass has a molecular weight in excess of 5,000.

9. The process of claim 4 , wherein the polymer in said reaction mass has a molecular weight in excess of 5,000 and is selected from the group consisting of a condensation polymer, a solution polymerized polymer, a bulk polymerized polymer and a melt polymerized polymer.

10. The process of claim 4 , wherein, after the extensively shear-thinning step and before the recovering step, the process comprises the additional steps of:

removing at least a portion of the contaminants from the reaction mass;

recycling at least a portion of the reaction mass to a processor; and

extensively shear-thinning the reaction mass to reduce the viscosity of the polymer;

wherein in the recovering step the recovered modified polymer has a melt flow index at least 10% lower than the melt flow index of the polymer before it is modified.

11. The process of claim 4 , wherein, after the extensively shear-thinning step and before the recovering step, the process comprises the additional steps of:

removing at least a portion of the contaminants from the reaction mass;

recycling at least a portion of the modified polymer into a polymerization reactor, said polymerization reactor including at least one monomer; and

reacting the modified polymer with the at least one monomer to increase the molecular weight of the modified polymer.

12. The process of claim 11 , wherein in the recovering step the recovered modified polymer has a molecular weight at least 5% higher than the molecular weight of the polymer provided in step (1).

13. The process of claim 11 , wherein in the recovering step the recovered modified polymer has a molecular weight at least 10% higher than the molecular weight of the polymer provided in step (1).

14. The process of claim 4 , wherein before the feeding step the process comprises the additional step of pretreating the reaction mass in a pretreatment means to reduce the amount of contaminants.

15. The process of claim 4 where the processor has vents and at least some contaminants are volatile contaminants, and where the process includes the step of, during the extensively shear-thinning step, venting at least some volatile contaminants.

16. The process of claim 15 , wherein in the recovering step the recovered modified polymer has a molecular weight at least 5% higher than the molecular weight of the polymer provided in step (1).

17. The process of claim 15 , wherein in the recovering step the recovered modified polymer has a molecular weight at least 10% higher than the molecular weight of the polymer provided in step (1).

18. The process of claim 15 , wherein in the recovering step the recovered modified polymer has a melt flow index at least 10% lower than the melt flow index of the polymer before it is modified.

19. A modified polymer produced according to claim 4 , wherein the recovered modified polymer has less than about 1,000 ppm of contaminants.

20. A modified polymer produced according to claim 4 , wherein the recovered modified polymer has less than about 500 ppm of contaminants.

21. A modified polymer produced according to claim 4 , wherein the recovered modified polymer has less than about 100 ppm of contaminants.