IP Library › Granted Patent US 12,415,958
Granted Patent B2
US 12,415,958 · App. 18/349,343 · Granted Sep 16, 2025

Process for stable blend of waste plastic with petroleum feed for feeding to oil refinery units and process of preparing same

Inventors: Hye-Kyung C. Timken (San Ramon, CA); Joel E. Schmidt (San Ramon, CA); Tengfei Liu (San Ramon, CA)
Assignee: Chevron U.S.A. Inc.
C10G1/002C10G2300/1003
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Quick Facts
Patent No.
US 12,415,958
App. No.
18/349,343
Granted
Sep 16, 2025
Kind
B2
Abstract

Provided is a blend of a petroleum feedstock and 1-20 wt. % of plastic, based on the weight of the blend, with the plastic comprising polyethylene and/or polypropylene, and the plastic in the blend comprising finely dispersed microcrystalline particles having an average particle size of 10 micron to less than 100 microns and less than 100 ppm chloride. A process for preparing a blend of plastic and petroleum is provided, comprising mixing together a petroleum feed and a plastic comprising polyethylene and/or polypropylene and heating the mixture in the range of from 550° F. to 700° F. The blend mixture is then hot filtered and then optionally treated with a chloride removal guard bed. The resulting blend can then be cooled and stored or sent directly to a refinery conversion unit.

Claims (15)

1. A process for preparing a blend of plastic and petroleum comprising:

(a) creating a mixture of a petroleum based feed and plastic comprising polyethylene and/or polypropylene and heating the mixture in the range of about 550° F. to about 700° F. (288-371° C.);

(b) recovering a product from step (a) and hot filtering the product to remove contaminants and produce a filtered blend; and

(c) then treating the filtered blend recovered from (b) with a chloride removal guard bed catalyst.

2. The process of claim 1 , wherein the heating is conducted while stripping the liquid using a gas such as nitrogen, hydrogen, steam, or light offgas from a conversion unit.

3. The process of claim 1 , wherein the treating is conducted at a temperature of 250°-700° F. (121° to 371° C.) with a residence time of 5-240 minutes at a final treating temperature.

4. The process of claim 1 , wherein the amount of plastic mixed with the petroleum feed ranges from 1-20 wt. % of the blend.

5. The process of claim 1 , wherein the amount of plastic in the blend comprises from 1-10 wt. % of the blend.

6. The process of claim 1 , wherein the plastic comprises low density polyethylene.

7. The process of claim 1 , wherein the plastic comprises high density polyethylene.

8. The process of claim 1 , wherein the plastic comprises multi-layer films comprising a metal barrier layer, polyethylene and/or polypropylene.

9. The process of claim 8 , wherein the metal barrier layer is comprised of aluminum.

10. The process of claim 1 , wherein the blend comprises from 1-10 wt. % of the high density polyethylene.

11. The process of claim 1 , wherein the plastic comprises polypropylene having an average molecular weight, Mw, in the range of 5,000 to 150,000.

12. The process of claim 1 , wherein the plastic comprises polypropylene having an average molecular weight, Mw, in the range of 150,000 to 400,000.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 29, 2024
From: TIMKEN, HYE-KYUNG C.; SCHMIDT, JOEL E.; LIU, TENGFEI
To: CHEVRON U.S.A. INC.
Reel/Frame 066599/0699 →
Continuity (2)
Provisional Application 63387041 · Dec 12, 2022
Related Publication 20240191140A1 · Jun 13, 2024
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Cited By (1)
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