Catalytic depolymerisation of polymeric materials

1. A process for converting a molten polymeric material, comprising:

providing a molten polymeric material having at least one carbon-carbon double bond; and

contacting the molten polymeric material with a catalyst material in a reaction zone to cleave at least one carbon-carbon double bond and produce a reaction product,

wherein the catalyst material includes [Fe—Cu—Mo—P]/Al 2 O 3 prepared by binding a ferrous-copper complex to an alumina support to generate an intermediate material, and reacting the intermediate material with an Mo- and P-containing heteropolyacid.

2. The process as claimed in claim 1 , wherein the contacting further comprises:

heating the reaction zone to a temperature suitable for cleaving at least one carbon-carbon double bond to produce the reaction product and suspending the heating when the pressure within the reaction zone reaches a predetermined pressure.

3. The process as claimed in claim 2 ,

wherein the predetermined pressure is correlated with at least one property of the reaction product.

4. The process as claimed in claim 1 , wherein providing the molten polymeric material comprises heating a polymeric material to produce the molten polymeric material.

5. The process as claimed in claim 2 , wherein the reaction product comprises waxes and grease base stocks, further comprising:

varying the predetermined pressure to produce different grades of waxes and grease base stocks.

6. The process as claimed in claim 1 ,

wherein the molten polymeric material further comprises at least one second polymeric material, wherein the second polymeric material is selected from the group consisting of polyethylene, polypropylene, polyethylene terephthalate, ethylene-vinyl acetate, polyphenylene ether, polyvinyl chloride, polystyrene, lignin, nylon, cellulose, and mixtures thereof.

7. The process as claimed in claim 1 , wherein the molten polymeric material further comprises polyethylene.

8. The process as claimed in claim 1 , wherein the molten polymeric material further comprises polypropylene.

9. The process as claimed in claim 1 ,

wherein the molten polymeric material includes waste polymeric material.

10. The process as claimed in claim 1 , wherein cleaving the at least one carbon-carbon double bond comprises depolymerisation.

11. A process for converting polymeric material to make waxes or grease base stocks through catalytic depolymerisation, comprising:

preheating the polymeric material to form a molten polymeric material;

catalytically depolymerizing the molten polymeric material in a high pressure reactor in the presence of a catalyst material at a temperature in the range of 300° C. to 600° C. until a pressure in the high pressure reactor reaches a predetermined value in the range of 50 psig to 350 psig, wherein the high pressure reactor comprises heaters and wherein the temperature is maintained using the heaters; and

turning off the heaters and stopping the catalytic depolymerisation when the pressure in the high pressure reactor reaches the predetermined value and wherein the molten polymeric material is converted to a wax or a grease base stock,

wherein the catalyst material is [Fe—Cu—Mo—P]/Al 2 O 3 prepared by binding a ferrous-copper complex to an alumina support to generate an intermediate material, and reacting the intermediate material with an Mo- and P-containing heteropolyacid.

12. The process as claimed in claim 11 , further comprising:

draining the wax or grease base stock into a container when the wax or grease base stock is liquid and is at a temperature above the flash point of the wax or grease base stock, respectively.

13. The process as claimed in claim 11 , wherein preheating the polymeric material to form the molten polymeric material comprises:

preheating the polymeric material using an extruder to form the molten polymeric material, wherein the extruder is in fluid communication with the high pressure reactor for feeding the molten polymeric material to the high pressure reactor.

14. The process as claimed in claim 13 , further comprising:

continuously feeding the molten polymeric material into the high pressure reactor.

15. The process as claimed in claim 11 , further comprising:

varying the predetermined value of the pressure in the high pressure reactor to produce different grades of waxes and grease base stocks.

16. The process as claimed in claim 12 , further comprising:

inducing coalescence of pigment particles/impurities in the drained wax or drained grease base stock using a high to low pressure cycle, wherein

(i) the pigment particles/impurities and (ii) the drained wax or drained grease base stock settle in the container as separate layers.

17. The process as claimed in claim 11 ,

wherein the polymeric material includes polyethylene, polypropylene, polyethylene terephthalate, ethylene-vinyl acetate, polyphenylene ether, polyvinyl chloride, polystyrene, lignin, nylon, or cellulose.

18. The process as claimed in claim 11 ,

wherein the polymeric material is polyethylene.

19. The process as claimed in claim 11 ,

wherein the polymeric material is polypropylene.

20. The process as claimed in claim 11 ,

wherein the polymeric material includes waste polymeric material.

21. A process for converting primary granules of polymeric material to make waxes or grease base stocks through catalytic depolymerisation, comprising:

preheating the primary granules of polymeric material to form molten primary granules of polymeric material;

catalytically depolymerizing the molten primary granules of polymeric material in a high pressure reactor in the presence of a catalyst material at a temperature in the range of 300° C. to 600° C. until a pressure in the high pressure reactor reaches a predetermined value in the range of 50 psig to 350 psig, wherein the high pressure reactor comprises heaters and wherein the temperature is maintained using the heaters; and

turning off the heaters and stopping the catalytic depolymerisation when the pressure in the high pressure reactor reaches the predetermined value and wherein the molten primary granules of polymeric material are converted to a wax or a grease base stock,

wherein the catalyst material is [Fe—Cu—Mo—P]/Al 2 O 3 prepared by binding a ferrous-copper complex to an alumina support to generate an intermediate material, and reacting the intermediate material with an Mo- and P-containing heteropolyacid.

22. The process of claim 21 , further comprising:

draining the wax or grease base stock into a container when the wax or grease base stock is liquid and is at a temperature above the flash point of the wax or grease base stock, respectively;

inducing coalescence of pigment particles/impurities in the drained wax or drained grease base stock using a high to low pressure cycle, wherein (i) the pigment particles/impurities and (ii) the drained wax or drained grease base stock settle in the container as separate layers.

23. The process of claim 21 , wherein preheating the primary granules of polymeric material to form the molten primary granules of polymeric material comprises:

preheating the primary granules of polymeric material using an extruder to form the molten primary granules of polymeric material, wherein the extruder is in fluid communication with the high pressure reactor for feeding the molten primary granules of polymeric material to the high pressure reactor; and

continuously feeding the molten primary granules of polymeric material into the high pressure reactor.