Process for creating an ethylene elastomer

1. A process for continuously making terpolymers and tetrapolymers, comprising ethylene monomers, alpha olefin monomers, and non-conjugated polyene monomers, comprising:

a. introducing a saturated hydrocarbon stream;

b. introducing an alpha olefin monomer to the saturated hydrocarbon stream at a rate sufficient to achieve alpha olefin content in a final product of 14 percent to 50 percent of total weight, wherein the alpha olefin monomer comprises from 3 carbon atoms to 20 carbon atoms;

c. introducing hydrogen gas to the saturated hydrocarbon stream at a rate sufficient to control the molecular weight of the final product;

d. introducing a first non-conjugated polyene to the saturated hydrocarbon stream at a rate sufficient to achieve desired first non-conjugated polyene content in the final product;

e. optionally introducing a second non-conjugated polyene to the saturated hydrocarbon stream at a rate sufficient to achieve desired second non-conjugated polyene content in the final product;

f. introducing an ethylene monomer to the saturated hydrocarbon stream at a rate sufficient to initiate the polymerization reaction and achieve ethylene content in the final product of 35 percent to 80 percent of total weight;

g. cooling the saturated hydrocarbon stream, the alpha olefin monomer, hydrogen gas, the first non-conjugated polyene, the second non-conjugated polyene if used, and the ethylene to below 35 degrees Celsius to create a cooled mixture;

h. concurrently introducing a Ziegler-Natta catalyst, a co-catalyst, and optionally a promoter into a continuous flow reactor, wherein:

(i) the Ziegler-Natta catalyst comprises a transition metal or a transition metal compound;

(ii) the co-catalyst comprises a metal alkyl comprising a halogen element; and

(iii) the promoter if used comprises an oxidizing agent capable of oxidizing the transition metal, and the oxidizing agent is capable of generating at least one halogen free-radical per mole of promoter;

i. reacting the cooled mixture, the Ziegler-Natta catalyst, the co-catalyst, the promoter if used, the first non-conjugated polyene, and the second non-conjugated polyene if used for 30 minutes to 60 minutes, at a temperature from 35 degrees Celsius to 65 degrees Celsius, and a pressure from 190 psig to 230 psig; and

j. forming a resultant terpolymer or a resultant tetrapolymer as the final product with the following characteristics:

(i) polymer chain branching as characterized by a tangent delta ranging from 0.286 to 5.0;

(ii) a non-linear relationship between viscosity and shear as characterized by the tangent delta from 0.286 to 5.0;

(iii) a weight average molecular weight of 80,000 to 2,500,000;

(iv) a Mooney viscosity ranging from (ML 1+4@ 125 degrees Celsius) 9 to (ML 1+4@ 150 degrees Celsius) 160;

(v) an ethylene to alpha olefin ratio ranging from 40:60 to 80:20;

(vi) a molecular weight distribution ranging from 1.8 to 8;

(vii) a combined weight content of ethylene and alpha olefin of 70 percent to 99.98 percent based upon the total weight of the resultant terpolymer or resultant tetrapolymer;

(viii) a first non-conjugated polyene content of 0.01 percent to 25 percent by weight content based upon the total weight of the resultant terpolymer or resultant tetrapolymer; and

(ix) a second non-conjugated polyene content if used of 0.01 percent to 5 percent by weight content based upon the total weight of the resultant terpolymer or the resultant tetrapolymer.

2. The process of claim 1 , wherein the Ziegler-Natta catalyst and the promoter if used are premixed before introduction to the continuous flow reactor.

3. The process of claim 1 , wherein the molar ratio of the co-catalyst to the sum of the catalyst and the promoter if used is from 1 to 50.

4. The process of claim 1 , wherein the saturated hydrocarbon stream is hexane.

5. The process of claim 1 , wherein the alpha olefin monomer is propylene.

6. The process of claim 1 , wherein the alpha olefin monomer is butylene.

7. The process of claim 1 , wherein the first non-conjugated polyene and the second non-conjugated polyene if used are both norbornene derivatives.

8. The process of claim 1 , wherein the Ziegler-Natta catalyst is a vanadium oxytrichloride or a vanadium vanadate.

9. The process of claim 1 , wherein the co-catalyst is Diethylaluminum chloride, Ethylaluminum sesquichloride, or Ethylaluminum dichloride.

10. The process of claim 1 , wherein the oxidizing agent is an ester comprising a halogen element.

11. The process of claim 1 , wherein the oxidizing agent is Butyl-2methyl, 4,4,4-trichlorobut-2-enoate.

12. The process of claim 1 , wherein reacting the cooled mixture, the Ziegler-Natta catalyst, the co-catalyst, the promoter if used, the first non-conjugated polyene, and the second non-conjugated polyene if used occurs in a slurry phase.

13. The process of claim 1 , wherein reacting the cooled mixture, the Ziegler-Natta catalyst, the co-catalyst, the promoter if used, the first non-conjugated polyene, and the second non-conjugated polyene if used occurs in a gas phase.

14. A terpolymer made by the process of claim 1 .

15. A terpolymer made by the process of claim 1 , wherein one of the components is Vinyl Norbornene.

16. A tetrapolymer made by the process of claim 1 .

17. A tetrapolymer made by the process of claim 1 , wherein one of the components is Vinyl Norbornene.

18. A thermoplastic vulcanizate comprising the final product made by the process of claim 1 .

19. The final product of claim 1 , further comprising an extender oil.

20. The process of claim 1 , wherein reacting the cooled mixture, the Ziegler-Natta catalyst, the co-catalyst, the promoter if used, the first non-conjugated polyene, and the second non-conjugated polyene if used occurs in a solution phase.