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公开(公告)号：US20220227892A1
公开(公告)日：2022-07-21
申请号：US17595565
申请日：2020-05-22
Applicant: Eastman Chemical Company
Inventor： David Eugene Slivensky , Daryl Bitting , Kenny Randolph Parker , Michael Gary Polasek , William Lewis Trapp , Xianchun Wu , Wenlai Feng , Thomas Joseph Pecorini , Michael Eugene Donelson , Haining An
Abstract: A process for preparing a recycle content cellulose ester and a recycle content cellulose ester composition comprising at least one cellulose ester having at least one substituent on an anhydroglucose unit (AU) derived from a recycle ethylene composition are provided.
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公开(公告)号：US20220220391A1
公开(公告)日：2022-07-14
申请号：US17595514
申请日：2020-05-22
Applicant: Eastman Chemical Company
Inventor： David Eugene Slivensky , Daryl Bitting , Kenny Randolph Parker , Michael Gary Polasek , William Lewis Trapp , Xianchun Wu
Abstract: The present application discloses a recycle content cracked effluent composition having a certain compositional profile produced by cracking a cracker feed comprising a recycle content pyrolysis oil composition, and methods of producing the recycle content cracked effluent composition.
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公开(公告)号：US20220220389A1
公开(公告)日：2022-07-14
申请号：US17595515
申请日：2020-05-22
Applicant: Eastman Chemical Company
Inventor： David Eugene Slivensky , Daryl Bitting , Kenny Randolph Parker , Michael Gary Polasek , William Lewis Trapp , Xianchun Wu
Abstract: The present application discloses a recycle content (C2-3)alkene product (r-(C2-3)alkene) having a certain compositional profile a obtained from cracking recycle content pyrolysis oil composition and processes for obtaining the recycle content (C2-3)alkene product having a certain compositional profile.
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公开(公告)号：US12215283B2
公开(公告)日：2025-02-04
申请号：US17594370
申请日：2020-05-22
Applicant: Eastman Chemical Company
Inventor： Daryl Bitting , Kenny Randolph Parker , Michael Gary Polasek , David Eugene Sllivensky , Xianchun Wu , Jerome Leonard Stavinoha, Jr.
Abstract: Recycle content pyoil is cracked in a cracker furnace to make olefins and the coil outlet temperature of the r-pyoil fed coils can be lowered by adding r-pyoil to the cracker feedstock, or alternatively, the coil outlet temperature of the r-pyoil fed tubes can rise if the mass flow rates of the combined cracker stream containing r-pyoil are kept the same or lowered. Further, increasing the hydrocarbon mass flow rate by addition of r-pyoil can be achieved to also increase the output of ethylene and propylene in the cracker effluent. The cracker furnace can accept ethane and/or propane feedstocks in vapor form along with a liquid and/or vapor feed of r-pyoil.
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公开(公告)号：US20240424540A1
公开(公告)日：2024-12-26
申请号：US18692913
申请日：2022-09-16
Applicant: Eastman Chemical Company
Inventor： Michael Gary Polasek , Daryl Bitting , Xianchun Wu , David Eugene Slivensky , Avery L. Anderson
IPC: B09B3/40 , B09B101/75 , F22B1/16
Abstract: A heat integration process and system for a chemical recycling facility is provided that can lower the carbon footprint and global warming potential of the facility. More particularly, one or more heat transfer media may be used to recover heat energy from a waste plastic pyrolysis effluent and redistribute the recovered heat energy throughout the chemical recycling facility. Thus, the global warming potential of the chemical recycling facility may be optimized and lowered due to the heat integration process and system herein.
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Patent Agency Ranking
公开(公告)号：US12173237B2
公开(公告)日：2024-12-24
申请号：US17755342
申请日：2020-10-29
Applicant: Eastman Chemical Company
Inventor： Michael Gary Polasek , Daryl Bitting , David Eugene Slivensky , Xianchun Wu
Abstract: Processes and systems for making recycle content hydrocarbons, including olefins, from recycled waste material. Recycle waste material may be pyrolyzed to form recycle content pyrolysis oil composition (r-pyoil), at least a portion of which may then be cracked to form a recycle content olefin composition (r-olefin). In some cases, a heavy fraction from the cracker effluent may be used to form a recycle content pyrolysis gasoline composition (r-pyrolysis gasoline).
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公开(公告)号：US20240368474A1
公开(公告)日：2024-11-07
申请号：US18567956
申请日：2022-06-24
Applicant: Eastman Chemical Company
Inventor： Xianchun Wu , Daryl Bitting , Kenny Randolph Parker , Michael Gary Polasek , David Eugene Slivensky
Abstract: Processes and facilities for providing recycled content hydrocarbon products (r-products) from recycled content pyrolysis oil (r-pyoil) and recycled content pyrolysis gas (r-pygas). Processing schemes provided herein maximize use of recycled content pyrolysis products to provide a variety of recycled content end products.
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公开(公告)号：US12018220B2
公开(公告)日：2024-06-25
申请号：US17593383
申请日：2020-05-22
Applicant: Eastman Chemical Company
Inventor： Daryl Bitting , Kenny Randolph Parker , Michael Gary Polasek , David Eugene Slivensky , Xianchun Wu , Jerome Leonard Stavinoha, Jr.
CPC classification number: C10G9/00 , C10G1/002 , C10G1/10 , C10G2300/1003 , C10G2400/20
Abstract: A predominantly C2 to C4 hydrocarbon cracker stream is combined with recycle content pyrolysis oil to form a combined cracker stream and the combined cracker stream is cracked in a cracker furnace to provide an olefin-containing effluent. The r-pyoil can be fed to a first coil while a second cracker feed with none of the r-pyoil or less of the r-pyoil is fed to a second coil, and both are cracked in a cracker furnace to form an olefin-containing effluent stream. Alternatively, the r-pyoil can be fed and distributed across multiple coils along with the non-recycle cracker feed. The furnace can be a gas fed furnace, or split cracker furnace. Further, a first cracker stream with r-pyoil in a first coil can have a lower total molar flow rate than a second cracker stream in a second coil in the same furnace.
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公开(公告)号：US11787754B2
公开(公告)日：2023-10-17
申请号：US17657978
申请日：2022-04-05
Applicant: Eastman Chemical Company
Inventor： Xianchun Wu , Daryl Bitting , Kenny Randolph Parker , Michael Gary Polasek , David Eugene Slivensky
Abstract: Processes and systems for making recycle content hydrocarbons, including olefins, are provided that integrate a cracker unit with one or more other processing units. For example, in some cases, a fluidized catalytic cracking unit may be used to crack recycle content pyrolysis oil and the effluent from the FCC may be further processed in a conventional cracker unit, including its downstream separation zone, to provide recycle content hydrocarbon product stream. In other cases, a pyrolysis unit and cracking unit may be co-located and may share at least one utility, service group, boundary, conduit, energy exchange zone, and/or geographical area.
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20.发明申请公开(公告)号：US20230089058A1
公开(公告)日：2023-03-23
申请号：US17932686
申请日：2022-09-16
Applicant: Eastman Chemical Company
Inventor： Michael Gary Polasek , Daryl Bitting , Xianchun Wu , David Eugene Slivensky
Abstract: Processes and facilities for producing recycled chemical products from waste plastic are described herein. The processes include treating process streams, such as a pyrolysis gas stream and/or at least a portion of a cracker furnace effluent stream, in a caustic scrubber process to remove certain components, such as carbon dioxide. The spent caustic solution from the caustic scrubber process is then recycled and reused in other caustic processes within the facility, which can include a halogen neutralization process from removing halogens from a liquification process off-gas.
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