Process for the preparation of polymers from waste plastic feedstocks

1. Process for the production of polymers from waste plastics feedstocks comprising the steps in an order of:

(a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock;

(b) providing a hydrocarbon stream B;

(c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s);

(d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D;

(e) supplying the cracked hydrocarbon stream D to a separation unit;

(f) performing a separation operation in the separation unit to obtain a product stream E comprising a monomer;

(g) supplying the product stream E to a polymerisation reactor; and

(h) performing a polymerisation reaction in the polymerisation reactor to obtain an polymer,

wherein the hydrocarbon stream B comprises:

≥25.0 and ≤80.0 wt %, of n-paraffins; and/or

≥5.0 and ≤40.0 wt %, of iso-paraffins; and/or

≥0.01 and ≤2.0 wt %, of olefins; and/or

≥5.0 and ≤40.0 wt %, of napthenes; and/or

≥5.0 and ≤15.0 wt %, of aromatics

with regard to the total weight of the hydrocarbon stream B.

2. Process according to claim 1 , wherein the hydrocarbon stream A has an initial boiling point of >25° C. and a final boiling point of <350° C., wherein the initial boiling point and the final boiling point are determined in accordance with ASTM D86 (2012).

3. Process according to claim 1 , wherein the hydrocarbon stream A has an atomic chlorine content of <800 ppm by weight as determined in accordance with ASTM UOP 779-08.

4. Process according to claim 1 , wherein the hydrocarbon stream A has an atomic nitrogen content of <1600 ppm by weight as determined in accordance with ASTM D5762 (2012).

5. Process according to claim 1 wherein the hydrocarbon stream A has a bromine number of <100 as determined in accordance with ASTM D1159-07 (2012).

6. Process according to claim 1 , wherein in step (c), the feed C comprises ≤50.0 wt %, of hydrocarbon stream A.

7. Process according to claim 1 , wherein the treatment of the waste plastics feedstock to obtain hydrocarbon stream A involves a pyrolysis treatment.

8. Process according to claim 1 , wherein the waste plastics feedstock comprises ≥90.0 wt % of polymeric material, with regard to the total weight of the waste plastics feedstock.

9. Process according to claim 1 , wherein the waste plastics feedstock comprises

<20.0 wt %, of polyesters; and/or

<20.0 wt %, of polyamides; and/or

<2.0 wt %, of polyvinyl chloride

with regard to the total weight of polymeric material in the waste plastics feedstock.

10. Process according to claim 1 , wherein the waste plastics feedstock comprises ≤10.0 wt % of ingredients being the sum of the content of glass, paper, metal, cardboard, compostable waste, wood, stone, textiles, rubber materials and superabsorbent hygiene products, with regard to the total weight of the waste plastics feedstock.

11. Process according to claim 1 , wherein the hydrocarbon stream A comprises:

≥25.0 and ≤50.0 wt %, of n-paraffins; and/or

≥5.0 and ≤20.0 wt %, of iso-paraffins; and/or

≥25.0 and ≤50.0 wt %, of olefins; and/or

≥5.0 and ≤20.0 wt %, of napthenes; and/or

≥5.0 and ≤15.0 wt %, of aromatics

with regard to the total weight of the hydrocarbon stream A.

12. Process according to claim 1 , wherein the feed C comprises a fraction of olefins F O,C of ≤2.0, with regard to the total weight of feed C.