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公开(公告)号:US20230312862A1
公开(公告)日:2023-10-05
申请号:US18128306
申请日:2023-03-30
Applicant: Chevron U.S.A. Inc.
Inventor: Tengfei LIU , Joel E. SCHMIDT , Hye-Kyung C. TIMKEN , Richard L. GROVE , Kaidong CHEN
IPC: C08J11/14 , C08F110/02
CPC classification number: C08J11/14 , C08F110/02 , C08J2323/06
Abstract: Provided is a continuous process for converting waste plastic into recycle for polyethylene polymerization. The process comprises selecting waste plastics containing polyethylene and/or polypropylene and preparing a stable blend of petroleum and the selected plastic. The amount of plastic in the blend comprises no more than 20 wt. % of the blend. The blend is passed to a refinery FCC unit. A liquid petroleum gas LPG olefin/paraffin mixture and naphtha are recovered from the FCC unit and passed to a steam cracker to make ethylene.
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公开(公告)号:US20240392096A1
公开(公告)日:2024-11-28
申请号:US18671065
申请日:2024-05-22
Applicant: Chevron U.S.A. Inc.
Inventor: Joel Edward SCHMIDT , Richard L. GROVE , Robert MONTGOMERY , Tengfei LIU , Hye-Kyung Cho TIMKEN
IPC: C08J11/18
Abstract: Provided is a stable blend of a petroleum atmospheric tower bottoms (ATBs) 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. A process for preparing a stable 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 above the melting point of the plastic, but less than 500° F. Then cooling the plastic melt and petroleum feedstock liquid blend with mixing to a temperature below the melting point of the plastic.
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公开(公告)号:US20230312437A1
公开(公告)日:2023-10-05
申请号:US18128336
申请日:2023-03-30
Applicant: Chevron U.S.A. Inc.
Inventor: Joel E. SCHMIDT , Hye-Kyung C. TIMKEN , Tengfei LIU , Richard L. GROVE , Kaidong CHEN
CPC classification number: C07C4/22 , C10G1/002 , C08J11/12 , C10G2300/1003 , C10G2300/305 , C10G2300/205 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/08 , C08J2323/12 , C10G2300/202 , C10G2300/308 , C10G2300/301
Abstract: Provided is a continuous process for converting waste plastic into recycle for polypropylene polymerization. The process comprises selecting waste plastics containing polyethylene and/or polypropylene and preparing a stable blend of petroleum and the selected plastic. The amount of plastic in the blend comprises no more than 20 wt. % of the blend. The blend is passed to a refinery FCC unit. A liquid petroleum gas C3 olefin/paraffin mixture is recovered from the FCC unit. The C3 paraffins and C3 olefins are separated into different fractions with the C3 olefin fraction passed to a propylene polymerization reactor, and the C3 paraffin fraction passed optionally to a dehydrogenation unit to produce additional propylene.
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