Processes and systems for producing light olefins and aromatics from a mixed plastics stream

Patent metadata

Field	Value
Publication number	US-11760939-B2
Application number	US-202318095892-A
Country	US
Kind code	B2
Filing date	Jan 11, 2023
Priority date	Feb 16, 2022
Publication date	Sep 19, 2023
Grant date	Sep 19, 2023

Abstract

Methods and systems for producing aromatics and light olefins from a mixed plastics stream are described. The method may include feeding a plastic feedstock to a dechlorination operation to melt the plastic feedstock to release HCl and generate a liquid plastic stream; feeding the liquid plastic stream to a pyrolysis reactor, the pyrolysis reactor to generate hydrocarbon vapors; feeding the hydrocarbon vapors to an acid gas removal reactor with a solid inorganic alkali salt disposed within the reaction vessel to remove residual HCl and sulfur-containing compounds from the hydrocarbon vapors to generate a plastic derived oil; and feeding the plastic derived oil to a steam enhanced catalytic cracking reactor to generate a product stream comprising light olefins having a carbon number of C2-C4 and aromatics. The associated system for processing mixed plastics into aromatics and light olefins is also described.

First claim

What is claimed is:

1. A system for processing mixed plastics into aromatics and light olefins, the system comprising:
an inlet stream comprising mixed plastics;
a dechlorination unit, the dechlorination unit in fluid communication with the inlet stream and operable to:
(i) raise the temperature of the inlet stream to a temperature between 250 and 350° C. to melt the mixed plastics and generate a liquid plastic stream; and
(ii) scrub HCl released from the inlet stream;

a pyrolysis reactor, the pyrolysis reactor in fluid communication with the liquid plastic stream discharged from the dechlorination unit and operable to raise the temperate of the liquid plastic stream to a temperature of 300 to 1,000° C. to generate hydrocarbon vapors;
an acid gas removal reactor, the acid gas removal reactor in fluid communication with the pyrolysis reactor and operable to remove residual HCl and sulfur-containing compounds from the hydrocarbon vapors to generate a plastic derived oil, where the acid gas removal reactor comprises a reaction vessel with a solid inorganic alkali salt disposed within the reaction vessel; and
a steam enhanced catalytic cracking reactor, the steam enhanced catalytic cracking reactor in fluid communication with the acid gas removal reactor and operable to crack the plastic derived oil at 600 to 700° C. to generate a product stream comprising light olefins having a carbon number of C 2 -C 4 and aromatics.

2. The system of claim 1 , where the inlet stream comprises two or more plastics selected from olefins, carbonates, aromatic polymers, sulfones, fluorinated hydrocarbon polymers, chlorinated hydrocarbon polymers, and acrylonitriles or two or more plastics selected from HDPE, LDPE, PP, LLDPE, PS, PVC, and PET.

3. The system of claim 1 , where the dechlorination unit comprises water or a sodium hydroxide solution to scrub the HCl released from the liquid plastic stream.

4. The system of claim 1 , where the solid inorganic alkali salt comprises sodium bicarbonate, sodium carbonate, sodium hydroxide, lime, or a combination thereof.

5. The system of claim 1 , where the plastic derived oil comprises less than 3 ppmw total chlorine-containing compounds.

6. The system of claim 1 , where the plastic derived oil comprises less than 500 ppmw of sulfur-containing compounds.

7. The system of claim 1 , where the system further comprises a secondary hydrocarbon stream in fluid communication with the plastic derived oil such that the plastic derived oil is combined with the secondary hydrocarbon stream for delivery into the steam enhanced catalytic cracking reactor as a single combined stream, where the secondary hydrocarbon stream selected from hydrocracker bottoms, virgin or hydrotreated vacuum gas oil, deasphalted oil (DAO), coker gas oil, cycle oil, visbroken oil, atmospheric residue.

8. The system of claim 1 , where the system further comprises a separation unit in fluid communication with the steam enhanced catalytic cracking reactor operable to generate a light olefin product stream comprising olefins having a carbon number of C 2 -C 4 and an aromatics product stream comprising aromatics from the product stream.

9. The system of claim 1 , where the product stream comprises at least 60 wt. % of light olefins and naphtha, the naphtha representing hydrocarbons with boiling points from 25 to 221° C.

10. The system of claim 9 , where the product stream comprises at least 40 wt. % of light olefins.

11. The system of claim 9 , where the product stream comprises less than 20 wt. % of hydrocarbons having a boiling point greater than 221° C.

Assignees

• Saudi Arabian Oil Co

Inventors

• Akah Aaron Chi

Classifications

• C10G11/00 Primary

  Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils (cracking in direct contact with molten metals or salts C10G9/34) · CPC title

• C10G1/10 Primary

  from rubber or rubber waste · CPC title

• C10G1/002

  in combination with oil conversion- or refining processes · CPC title

• C10G19/073

  with solid alkaline material · CPC title

• B01D2253/108

  Zeolites · CPC title