Mechanical polyolefin recycling process

1 . A mechanical polyolefin recycling process, comprising, in the given order:

a) providing a precursor mixed plastic recycling stream (A);

b) sieving the precursor mixed plastic recycling stream (A) to create a sieved mixed plastic recycling stream (B) having only articles with a longest dimension in the range from 30 to 400 mm;

c) sorting the sieved mixed plastic recycling stream (B) by means of one or more optical sorters wherein the sieved mixed plastic recycling stream (B) is at least sorted by colour and optionally also by polyolefin type and/or article form, thereby generating one or more single-colour sorted polyolefin recycling stream(s) (C) and a mixed-colour sorted polyolefin recycling stream (CM), wherein each of the one or more single-colour sorted polyolefin recycling stream(s) (C) and the mixed-colour sorted polyolefin recycling stream (CM) are subjected separately to steps d) and beyond;

d) shredding the sorted polyolefin recycling stream (C or CM) to form a flaked polyolefin recycling stream (D);

e) washing the flaked polyolefin recycling stream (D) with a first aqueous washing solution (W1) without the input of thermal energy, thereby generating a first suspended polyolefin recycling stream (E);

f) removing at least part of the first aqueous washing solution (W1) from the first suspended polyolefin recycling stream (E) to obtain a first washed polyolefin recycling stream (F);

g) washing the first washed polyolefin recycling stream (F) with a second aqueous washing solution (W2) thereby generating a second suspended polyolefin recycling stream (G), wherein sufficient thermal energy is introduced to the second suspended polyolefin recycling stream (G) to provide a temperature in the range from 65 to 95° C. during the washing;

h) removing the second aqueous washing solution (W2) and any material not floating on the surface of the second aqueous washing solution from the second suspended polyolefin recycling stream (G) to obtain a second washed polyolefin recycling stream (H);

i) drying the second washed polyolefin recycling stream (H), thereby obtaining a dried polyolefin recycling stream (I);

j) optionally separating the dried polyolefin recycling stream (I) into a light fraction and a heavy fraction polyolefin recycling stream (J);

k) further sorting the heavy fraction polyolefin recycling stream (J) or, in the case that step j) is absent, the dried polyolefin recycling stream (I) by means of one or more optical sorters sorting for one or more target polyolefins by removing any flakes containing material other than the one or more target polyolefins, yielding a purified polyolefin recycling stream (K);

l) Optionally melt extruding, preferably pelletizing, the purified polyolefin recycling stream (K) to form an extruded recycled polyolefin product (L); and

m) optionally aerating the recycled polyolefin product (L) or, in the case that step l) is absent, the purified polyolefin recycling stream (K) to remove volatile organic compounds, thereby generating an aerated recycled polyolefin product (M), being either an aerated extruded recycled polyolefin product (M1) or aerated recycled polyolefin flakes (M2),

wherein the order of steps l) and m) can be interchanged, such that the purified polyolefin recycling stream (K) is first aerated to form aerated recycled polyolefin flakes (M2) that are subsequently extruded to form an extruded aerated recycled polyolefin product (M3).

2 . The process according to any claim 1 , wherein the optical sorters of step c) sort via a method selected from the group consisting of camera systems (operating in the visible range of the EM-spectrum), visible reflectance spectroscopy, near-IR spectroscopic analysis, mid-IR spectroscopic analysis, high-speed laser spectroscopic analysis, Raman spectroscopic analysis, and Fourier-transform infrared (FT IR) spectroscopic analysis.

3 . The mechanical polyolefin recycling process according to claim 1 , wherein the shredding of step d) is a wet shredding process, wherein the sorted polyolefin recycling stream (C) is first contacted with an aqueous solution (W0) to provide a suspended sorted polyolefin recycling stream, which is thereafter subjected to shredding.

4 . The mechanical polyolefin recycling process according to claim 1 , wherein the second aqueous washing solution (W2) is an alkaline aqueous washing solution.

5 . The mechanical polyolefin recycling process according to claim 4 , wherein the alkaline aqueous solution has a pH in the range from 9.0 to 14.0.

6 . The mechanical polyolefin recycling process according to claim 4 , wherein the amount of the base in the alkaline aqueous solution is in the range from 0.05 to 10 wt.-%, relative to the total weight of the alkaline aqueous solution.

7 . The mechanical polyolefin recycling process according to claim 1 , wherein at least part of the second aqueous washing solution (W2) removed in step h) is recycled for use as the first aqueous washing solution (W1) and/or the aqueous solution (W0), if present.

8 . The mechanical polyolefin recycling process according to claim 1 , wherein the first aqueous washing solution (W1) and/or the aqueous solution (W0), if present have a pH in the range from 8.0 to 14.0.

9 . The process according to claim 1 , wherein the precursor mixed plastic recycling stream (A) originates from post-consumer waste, post-industrial waste, or a combination thereof.

10 . The process according to claim 1 , wherein one of the one or more single-colour sorted polyolefin recycling stream(s) (C1) is either a single-colour sorted polyethylene recycling stream or a single-colour sorted polypropylene recycling stream.

11 . The process according to claim 1 , wherein the sorting of step c) sorts the filtered mixed plastic recycling stream (B) into at least a first single-colour sorted polyolefin recycling stream (C1) containing a first target polyolefin (PO1), a second single-colour sorted polyolefin recycling stream (C2) containing a second target polyolefin (PO2) and a mixed-colour sorted polyolefin recycling stream (CM), wherein the first target polyolefin (PO1) and the second polyolefin (PO2) differ in at least one property selected from colour, polyolefin type and article form, wherein the first single-colour sorted polyolefin recycling stream (C1), the second single-colour sorted polyolefin recycling stream (C2), and the mixed-colour sorted polyolefin recycling stream (CM) are individually subjected to steps d) and beyond.

12 . The mechanical polyolefin recycling process according to claim 11 , wherein the sorting of step c) comprises:

c1) sorting the filtered polyolefin recycling stream (B) using a first optical sorter to obtain a fraction (C4) that contains two target polyolefins (PO1 and PO2) and a mixed-colour recycling stream (C5);

c2) sorting the fraction containing two target polyolefins (C4) using a second optical sorter to obtain a first target fraction (C6) containing the first target polyolefin (PO1) and a second target fraction (C7) containing the second target polyolefin (PO2);

c3) further purifying the first target fraction (C6) and the second target fraction (C7) using a third optical sorter, thereby removing any articles not containing the first target polyolefin (PO1) from the first target fraction (C6) and any articles not containing the second target polyolefin (PO2) from the second target fraction (C7), thereby obtaining a first single-colour sorted polyolefin recycling stream (C1) and a second single-colour sorted polyolefin recycling stream (C2), which are individually subjected to steps d) and beyond, and a further mixed-colour recycling stream (C8);

c4) feeding mixed-colour recycling stream (C5) and further mixed-colour recycling stream (C8) into a fourth optical sorter to remove any articles containing the first target polyolefin (PO1) or the second target polyolefin (PO2), thereby generating a reclaimed fraction (C9) and a mixed-colour polyolefin recycling stream (C3); and

c5) feeding the reclaimed fraction (C9) back into the first optical sorter during step c1),

wherein the mixed-colour polyolefin recycling stream (C3) is either subjected to steps d) and beyond as the mixed-colour sorted polyolefin recycling stream (CM) or subjected to a further iteration of step c), thereby separating the mixed-colour polyolefin recycling stream (C3) into a further first single-colour sorted polyolefin recycling stream (C1), a further second single-colour sorted polyolefin recycling stream (C2), and a further mixed-colour polyolefin recycling stream (C3).

13 . The mechanical polyolefin recycling process according to claim 11 , wherein the first target polyolefin (PO1) and the second target polyolefin (PO2) are the same colour but contain different polyolefin types or wherein the first target polyolefin (PO1) and the second target polyolefin (PO2) contain the same polyolefin type but are different colours.

14 . The mechanical polyolefin recycling process according to claim 13 , wherein the first target polyolefin (PO1) is a polypropylene having a first desired colour and the second target polyolefin (PO2) is a polypropylene having a second desired colour different to the first desired colour, or

wherein the first target polyolefin (PO1) is a polyethylene having a first desired colour and the second target polyolefin (PO2) is a polyethylene having a second desired colour different to the first desired colour.

15 . The mechanical polyolefin recycling process according to claim 1 , wherein the sorting of step c) involves first sorting the sieved mixed plastic recycling stream (B) by polyolefin type, thereby generating a mixed-colour single polyolefin recycling stream (CS), which is subsequently sorted by colour to generate the one or more single-colour sorted polyolefin recycling stream(s) (C) and a mixed-colour sorted polyolefin recycling stream (CM), wherein each single-colour sorted polyolefin recycling stream (C) and the mixed-colour sorted polyolefin recycling stream (CM) contain the same polyolefin.

16 . The mechanical polyolefin recycling process according to claim 1 , wherein the melt extruding of step l) is a pelletizing step, the extruded recycled polyolefin product (L) is a pelletized recycled polyolefin product (L), the aerated extruded recycled polyolefin product (M1) is an aerated pelletized recycled polyolefin product (M1), or

wherein the wherein the order of steps l) and m) are interchanged, the melt extruding of step l) is a pelletizing step, and the extruded aerated recycled polyolefin product (M3) is a pelletized aerated recycled polyolefin product (M3).

17 . The mechanical polyolefin recycling process according to claim 1 , wherein additives (Ad) are added in the melt state during the melt extruding of step l).

18 . The mechanical polyolefin recycling process according to claim 4 , wherein the second aqueous washing solution (W2) is an aqueous solution of a base selected from the group consisting of calcium hydroxide, potassium hydroxide, magnesium hydroxide, lithium hydroxide, sodium bicarbonate, sodium hydroxide and mixtures thereof.

19 . The mechanical polyolefin recycling process according to claim 15 , wherein the same polyolefin is selected from polyethylene and polypropylene.