Process for PVC-containing mixed plastic waste pyrolysis

Patent metadata

Field	Value
Publication number	US-12024680-B2
Application number	US-202117367336-A
Country	US
Kind code	B2
Filing date	Jul 3, 2021
Priority date	Jul 10, 2020
Publication date	Jul 2, 2024
Grant date	Jul 2, 2024

Abstract

A process for pyrolysis of a mixed plastic stream that contains polyvinyl chloride (PVC) is provided in which the chloride from PVC is removed from an initial melting reactor that heats the mixed plastic stream to a sufficient temperature to produce HCl but at a low enough temperature to avoid production of organochlorides. Chloride is primarily removed in a vapor stream from the initial melting reactor, while additional chloride removal may be removed downstream from the melting reactor by the use of sorbent addition to the pyrolysis reactor and by subsequent adsorbent beds.

First claim

The invention claimed is:

1. A process for producing a pyrolysis oil out of a mixed plastic waste stream comprising
a. sending the mixed plastic waste stream comprising at least two types of plastic including chlorine-containing plastics and other plastics to a melting reactor to produce a first vapor stream and a first liquid stream;
b. sending said first liquid stream to a pyrolysis reactor to be heated to produce a product comprising vapor, liquid, and solid particles;
c. withdrawing a second vapor stream, a second liquid stream, and a residue stream comprising the solid particles from said pyrolysis reactor;
d. circulating a part of the second liquid stream to said melting reactor and sending a part of the second liquid stream to be heated and returned to said pyrolysis reactor as a heated second liquid stream; and
e. cooling and separating the second vapor stream into a third vapor stream and a third liquid stream and then passing the third liquid stream through an adsorbent bed to remove residual chloride to produce said pyrolysis oil.

2. The process of claim 1 further comprising adding a sorbent to said pyrolysis reactor to adsorb chloride-containing molecules.

3. The process of claim 2 wherein said sorbent is a ground alkaline material present in about a 2.5-4 molar ratio to the chloride-containing molecules in said pyrolysis reactor and in an amount of <3% wt relative to plastic melt.

4. The process of claim 1 wherein said first vapor stream is sent to a gas cleaning zone.

5. The process of claim 4 wherein said gas cleaning zone comprises a catalyst bed to remove dioxin compounds and a vessel containing caustic compounds to neutralize HCl.

6. The process of claim 1 wherein said melting reactor is operated at a temperature from about 280° C. (536° F.) to about 330° C. (626° F.), said pyrolysis reactor is operated at a temperature from about 380° C. (716° F.) to about 450° C. (842° F.) and said adsorbent bed is operated at a temperature from about 100° C. (212° F.) to about 300° C. (572° F.).

7. The process of claim 1 wherein said melting reactor is operated at a pressure from about 0.069 MPa-gauge (10 psig) to about 1.38 M Pa-gauge (200 psig) and a liquid hourly space velocity from about 0.1 hr −1 to about 2 hr −1 and is operated under a nitrogen blanket or a dedicated nitrogen sweeping rate of about 1.7 Nm 3 /m 3 (10 scf/bbl) to about 170 Nm 3 /m 3 (1,000 scf/bbl); said pyrolysis reactor is operated at a pressure from about 0.069 M Pa-gauge (10 psig) to about 1.38 MPa-gauge (200 psig) and a liquid hourly space velocity from about 0.1 hr −1 to about 2 hr −1 and is operated under a nitrogen blanket or a dedicated nitrogen sweeping stream at a rate of about 17 Nm 3 /m 3 (100 scf/bbl) to about 850 Nm 3 /m 3 (5,000 scf/bbl); and said adsorbent bed is operated pressure from about 0.069 MPa-gauge (10 psig) to about 2.07 MPa-gauge (300 psig) and a liquid hourly space velocity from about 0.05 hr −1 to about 5 hr −1 .

8. The process of claim 1 wherein said third liquid stream comprises less than about 200 ppmw chloride.

9. The process of claim 1 wherein a heat of reaction in said pyrolysis reactor is about 2-3 times higher than a heat of reaction in said melting reactor.

10. The process of claim 9 wherein the heat of reaction in the melting reactor is supplied by the part of the second liquid stream.

11. The process of claim 9 wherein the heat of reaction in the pyrolysis reactor is supplied by the heated part of the second liquid stream.

12. A process for pyrolysis of a mixed plastic waste stream comprising:
a. sending the mixed plastic waste stream to a melting reactor to produce a first vapor stream and a first liquid stream;
b. sending the first liquid stream to a pyrolysis reactor to be heated to produce a product comprising vapor, liquid, and solid particles, wherein the solid particles move in a downward direction within said pyrolysis reactor;
c. withdrawing a second vapor stream, a second liquid stream, and a residue stream comprising the solid particles from said pyrolysis reactor, wherein a mass ratio between said second vapor stream and said residue stream is 2.3 to 9;
d. cooling and separating said second vapor stream into a third vapor stream and a third liquid stream and then treating said third liquid stream in at least one adsorbent bed to remove chlorine containing impurities;
e. mixing a portion of the second liquid stream with the mixed plastic waste stream in the melting reactor providing temperatures needed to produce the first vapor stream; and
f. sending a portion of the second liquid stream to an external heater to produce a heated stream and sending the heated stream back to mix with the first liquid stream before said mixed stream enters said pyrolysis reactor.

13. The process of claim 12 further comprising sending said first vapor stream to an incinerator and then to a gas cleaning zone to remove chlorine compounds, and wherein the incinerator is the external heater which heats the portion of said second liquid stream as a reaction heat supply for said pyrolysis reactor.

14. The process of claim 13 wherein said gas cleaning zone comprises a catalyst bed to remove dioxin compounds and a vessel containing caustic compounds to neutralize HCl.

15. The process of claim 12 further comprising sending an adsorbent to said pyrolysis reactor to remove chlorine compounds.

16. The process of claim 15 wherein said adsorbent is an alkaline material present in about a 2-3 molar ratio to the chloride compounds in said pyrolysis reactor.

17. The process of claim 15 wherein said adsorbent further functions as a flocculation material for carbonaceous char particles formed during operation of the pyrolysis reactor.

18. A process for pyrolysis of a mixed plastic waste stream comprising:
a. sending the mixed plastic waste stream to a melting reactor to produce a first vapor stream and a first liquid stream;
b. sending the first liquid stream to a pyrolysis reactor to be heated to produce a product comprising vapor, liquid, and solid particles, wherein the solid particles move in a downward direction within said pyrolysis reactor;
c. withdrawing a second vapor stream, a second liquid stream, and a residue stream comprising the solid particles from said pyrolysis reactor;
d. sending a portion of said second liquid stream to a heat exchanger and recycled to said pyrolysis reactor and sending a second portion of said second liquid stream to said melting reactor; and
e. cooling and separating said second vapor stream into a third vapor stream and a third liquid stream and then treating said third liquid stream in at least one adsorbent bed to remove chlorine containing impurities.

Assignees

• Uop Llc

Inventors

• Sun Ping
• Tyska Jeffrey
• Montalbano Joseph A

Classifications

• B01D15/00

  Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor · CPC title

• Y02P20/143

  the feedstock being recycled material, e.g. plastics · CPC title

• F23G5/027

  pyrolising or gasifying stage (pyrolisation of sludge C02F11/00; destructive distillation of carbonaceous materials C10B53/00) · CPC title

• B01D2257/204

  Inorganic halogen compounds · CPC title

• C10G2300/1003

  Waste materials · CPC title