Chloride removal for plastic waste conversion

Patent metadata

Field	Value
Publication number	US-12552999-B2
Application number	US-202218554093-A
Country	US
Kind code	B2
Filing date	Mar 18, 2022
Priority date	Apr 14, 2021
Publication date	Feb 17, 2026
Grant date	Feb 17, 2026

Abstract

Systems and methods are provided for reducing or minimizing the chloride content of products generated during co-processing of a plastic feedstock (such as plastic waste) in a refinery process. The reduction in chloride is achieved by mixing the plastic feedstock with one or more additional feedstocks for co-processing in a mixing and/or holding vessel that is maintained at a dechlorination temperature that allows for decomposition of chlorine from the plastic feedstock to form HCl, while reducing or minimizing other conversion of the plastic feedstock and/or the additional feedstock. A purge gas can be passed through the mixing/holding vessel to remove the evolved HCl from the vessel. Because the dechlorination temperature is selected to reduce or minimize conversion of the feedstocks in the mixture, the amount of carbon-containing products that are removed with the purge gas can be reduced or minimized. The dechlorinated mixture of plastic feedstock and additional feedstock(s) can then be processed in a convenient refinery process, such as a thermal cracking process (e.g., coking, visbreaking, other types of pyrolysis) or a catalytic conversion process (e.g., fluid catalytic cracking).

First claim

What is claimed is:

1 . A method for co-processing a plastic feedstock, comprising:
mixing a plastic feedstock comprising plastic particles having an average diameter of 10 cm or less with one or more additional feedstocks to form a feedstock mixture, the plastic feedstock comprising a chlorine-containing polymer, the feedstock mixture comprising 1.0 wt % to 50 wt % of the plastic feedstock relative to a weight of the feedstock mixture, the one or more additional feedstocks comprising a T5 distillation point that is greater than a dechlorination temperature of 170° C. to 250° C.; maintaining the feedstock mixture in a vessel at the dechlorination temperature for 1.0 minute to 240 minutes to form a dechlorinated mixture of feedstocks; passing a purge stream comprising a purge gas comprising oxygen, light ends stream comprising C4-hydrocarbons, or any combination thereof through the vessel containing the feedstock mixture to form a purge exhaust stream comprising at least a portion of the purge gas; and processing the dechlorinated mixture of feedstocks in a co-processing stage for conversion of at least a portion of the dechlorinated mixture of feedstocks to form a conversion effluent.

2 . The method of claim 1 , wherein the co-processing stage comprises at least one of a pyrolysis stage, a delayed coking stage, a fluidized coking stage, and a visbreaking stage.

3 . The method of claim 1 , wherein the co-processing stage comprises a fluid catalytic cracking stage.

4 . The method of claim 1 , further comprising separating the conversion effluent to form at least one product fraction and at least one recycle fraction, the method further comprising combining the at least one recycle fraction with a) the one or more additional feedstocks prior to entering the vessel, b) the feedstock mixture in the vessel, c) the dechlorinated mixture of feedstocks after leaving the vessel and prior to processing the dechlorinated mixture of feedstocks in the co-processing stage, or d) a combination of two or more of a)-c).

5 . The method of claim 1 , wherein the dechlorination temperature is 170° C. to 230° C.

6 . The method of claim 1 , wherein the dechlorinated mixture of feedstocks comprises 1000 wppm or less of Cl relative to a weight of the dechlorinated mixture of feedstocks.

7 . The method of claim 1 , wherein the feedstock mixture is maintained at the dechlorination temperature while being exposed to one or more decomposition additives, or a combination thereof.

8 . The method of claim 1 , wherein maintaining the feedstock mixture in the vessel further comprises forming HCl, and wherein the purge exhaust stream further comprises at least a portion of the formed HCl.

9 . The method of claim 1 , wherein the plastic feedstock comprises a biomass-derived portion, the plastic feedstock comprising 1.0 wt % to 30 wt % of the feedstock mixture.

10 . The method of claim 1 , wherein the one or more additional feedstocks comprise a T5 distillation point greater than 260° C., or wherein the one or more additional feedstocks comprise an initial boiling point greater than 260° C.

11 . The method of claim 1 , wherein the purge exhaust stream comprises 5.0 wt % or less of volatile organic compounds relative to weight of the feedstock mixture.

12 . The method of claim 11 , the method further comprising performing contaminant removal on the purge exhaust stream.

13 . The method of claim 1 , wherein the chlorine-containing polymer comprises PVC, PVDC, chlorinated PVC, or a combination thereof.

14 . The method of claim 1 , wherein the plastic feedstock comprises 1.0 wt % to 30 wt % of the chlorine-containing polymer.

15 . The method of claim 1 , wherein the method further comprises forming the plastic feedstock by physically processing plastic particles to reduce a median particle size of the plastic particles to 10 cm or less; or wherein the method further comprises forming the plastic particles by physically processing bulk plastic; or a combination thereof.

16 . The method of claim 1 , further comprising mixing the dechlorinated mixture with a supplemental feedstock prior to the processing, the dechlorinated mixture comprising 2500 wppm or less of chlorine prior to mixing the dechlorinated mixture with the supplemental feedstock, the dechlorinated mixture comprising 1000 wppm or less of chlorine after mixing the dechlorinated mixture with the supplemental feedstock.

17 . A system for co-processing of a plastic feedstock, comprising:
a physical processing stage comprising a plastic inlet and a physically processed plastic outlet; a mixing vessel comprising a plastic feedstock inlet, at least one additional feedstock inlet, a purge gas inlet coupled to an oxygen source for injection to the mixing vessel containing a feedstock, a purge exhaust, and a dechlorinated feedstock outlet, the plastic feedstock inlet being in solids flow communication with the physically processed plastic outlet; and a fluid catalytic cracking stage in fluid communication with the dechlorinated feedstock outlet.

18 . A system for co-processing of a plastic feedstock, comprising:
a physical processing stage comprising a plastic inlet and a physically processed plastic outlet; a mixing vessel comprising a plastic feedstock inlet, at least one additional feedstock inlet, a purge gas inlet, a purge exhaust, and a dechlorinated feedstock outlet, the plastic feedstock inlet being in solids flow communication with the physically processed plastic outlet; and a pyrolysis stage in fluid communication with the dechlorinated feedstock outlet.

19 . The system of claim 18 , wherein the pyrolysis stage comprises at least one of a fluidized coking stage and a delayed coking stage.

20 . The system of claim 18 , wherein the pyrolysis stage comprises a pyrolysis outlet, and wherein the at least one additional feedstock inlet is in fluid communication with the pyrolysis outlet.

21 . A method for co-processing a plastic feedstock, comprising:
mixing a plastic feedstock comprising plastic particles having an average diameter of 10 cm or less with one or more additional feedstocks to form a feedstock mixture, the plastic feedstock comprising a chlorine-containing polymer, the feedstock mixture comprising 1.0 wt % to 50 wt % of the plastic feedstock relative to a weight of the feedstock mixture, the one or more additional feedstocks comprising a T10 distillation point that is greater than a dechlorination temperature of 170° C. to 300° C.; maintaining the feedstock mixture in a vessel at the dechlorination temperature for 1.0 minute to 240 minutes to form a dechlorinated mixture of feedstocks; passing a purge stream comprising a purge gas comprising oxygen in an amount from about 0.1 time to 10 times a molar amount of chlorine present in the chlorine-containing polymer through the vessel containing the feedstock mixture to form a purge exhaust stream comprising at least a portion of the purge gas; and processing the dechlorinated mixture of feedstocks in a co-processing stage for conversion of at least a portion of the dechlorinated mixture of feedstocks to form a conversion effluent, the processing in the co-processing stage comprising a) a temperature of 475° C. or higher, b) a temperature that is greater than the dechlorination temperature by 200° C. or more, or c) a combination of a) and b).

22 . The method of claim 21 , wherein the one or more additional feedstocks comprise a T5 distillation point that is

Assignees

• Exxonmobil Chemical Patents Inc

Inventors

• Patel Bryan A
• Buchanan Clara M
• Maduskar Saurabh S
• Raich Brenda A
• Bernatz Fritz A
• Diaz Cody M

Classifications

• C10G2300/4006

  Temperature · CPC title

• C10G2300/201

  Impurities · CPC title

• C08J2327/08

  Homopolymers or copolymers of vinylidene chloride · CPC title

• C08J2327/06

  Homopolymers or copolymers of vinyl chloride · CPC title

• C08J11/10

  by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation (depolymerisation to the original monomer C07) · CPC title