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公开(公告)号:US20230048572A1
公开(公告)日:2023-02-16
申请号:US17964754
申请日:2022-10-12
Applicant: Chevron U.S.A. Inc.
Inventor: Hye-Kyung Timken
IPC: C10G1/10 , C07C4/04 , C10G45/58 , C08F10/02 , C10M177/00 , C10M105/04 , C10B53/07 , C10G1/00
Abstract: Provided is a continuous process for converting waste plastic into recycle for polyethylene polymerization. In one embodiment, the process comprises selecting waste plastics containing polyethylene and/or polypropylene and passing the waste plastics through a pyrolysis reactor to thermally crack at least a portion of the polyolefin waste and produce a pyrolyzed effluent. The pyrolyzed effluent is separated into offgas, a naphtha/diesel fraction, a heavy fraction, and char. The naphtha/diesel fraction is passed to a crude unit distillation column in a refinery where a straight run naphtha (C5-C8) fraction or a propane/butane (C3-C4) fraction is recovered. The straight run naphtha fraction (C5-C8) or the propane/butane (C3-C4) fraction is passed to a steam cracker for ethylene production. The heavy fraction from the pyrolysis unit can also be passed to an isomerization dewaxing unit to produce a base oil.
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公开(公告)号:US20230027439A1
公开(公告)日:2023-01-26
申请号:US17946194
申请日:2022-09-16
Applicant: UPM-KYMMENE CORPORATION
Inventor: Andrea GUTIERREZ , Pekka JOKELA , Roel WESTERHOF , Sascha KERSTEN , Bert HEESINK
Abstract: The disclosure relates to a process for converting lignocellulosic feedstock (10) to renewable product (80), wherein the process comprises the following steps; treating (100) lignocellulosic feedstock (10) with aqueous solution (20) to obtain a mixture (30); heating (110) the mixture (30) of step (a) to a temperature between 290 and 340° C., under a pressure from 90 to 120 bar, to obtain a first product mix (40); separating aqueous phase (53) and oil phase (50), and optionally gas (51) and solids (52), of the first product mix (40) of step (b); and heating (130) the oil phase (50) of step (c) and solvent (60). The heating (130) is optionally followed by fractionation (200) to obtain a light fraction (90) and a heavy fraction (91) and optionally a bottom residue fraction (92) and/or a gaseous fraction.
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公开(公告)号:US20230002688A1
公开(公告)日:2023-01-05
申请号:US17781078
申请日:2020-11-16
Applicant: IFP Energies Nouvelles
Inventor: Wilfried WEISS , Jerome BONNARDOT
IPC: C10G65/06 , C10G1/00 , C10G1/10 , C10G49/00 , C10G69/06 , C10G25/00 , C10G49/04 , C10G9/36 , C10G45/38 , C10G67/06
Abstract: A process for treating a plastics pyrolysis oil: a) selective hydrogenation of feedstock in the presence of hydrogen and at least one selective hydrogenation catalyst, at 100 to 150° C., a partial pressure of hydrogen of 1.0 to 10.0 MPa abs. and an hourly space velocity of 1.0 to 10.0 h−1, to obtain a hydrogenated effluent; b) hydrotreatment of hydrogenated effluent in the presence of hydrogen and at least one hydrotreatment catalyst, at 250 to 370° C., a partial pressure of hydrogen of 1.0 to 10.0 MPa abs. and an hourly space velocity of 1.0 to 10.0 h−1, to obtain a hydrotreatment effluent; c) separation of hydrotreatment effluent obtained from b) in the presence of an aqueous stream, at a temperature of 50 to 370° C., to obtain at least one gaseous effluent, an aqueous liquid effluent and a hydrocarbon liquid effluent.
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公开(公告)号:US11530358B2
公开(公告)日:2022-12-20
申请号:US16630803
申请日:2018-07-04
Applicant: ENVIROLLEA INC.
Inventor: Louis Bertrand , Lucie B. Wheeler
IPC: C10G1/00 , C10G3/00 , F23G5/00 , F27B7/08 , C10G1/02 , F23G5/027 , F23G5/033 , F23G5/20 , F23G7/05 , F27B7/14 , F27B7/28 , F23G7/00
Abstract: Processes for producing liquid fuels from a mainly organic starting material with a reduced content in water and/or with a reduced content in solids are disclosed. The mainly organic starting material can be at least partially liquified and optionally further dewatered. The obtained at least partially liquid fraction can be thereafter used as feeding stream that is submitted to a pyrolysis treatment resulting in a solid gas fraction allowing the recovering of a liquid fuels after a controlled liquid solid separation treatment. There are also provided various other processes for producing liquid fuel from waste hydrocarbon and/or organic material as well as reactors, apparatuses, uses and managing systems thereof.
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公开(公告)号:US11518702B2
公开(公告)日:2022-12-06
申请号:US16979639
申请日:2019-03-13
Applicant: Nulife Greentech Inc.
Inventor: Jerry Kristian , Brock Eidem , Peter Voldeng
IPC: C02F11/18 , C01B32/50 , B01D3/14 , B01D3/42 , C01B33/12 , C10G1/02 , C10L9/08 , C10G1/00 , C01B25/26 , C10G7/04
Abstract: Commercially beneficial carbon-containing fractions can be recovered from hydrothermal liquefaction reactions in various types of processors. Feedstock slurry from waste solids is placed into a pressurized processor where it is maintained at temperature and pressure for a predetermined period. On discharge from the processor the processed discharge is separated into liquid and solid fractions. Gaseous fractions including carbon dioxide can also be removed or off-taken from the processor. New molecular structures are created in this reaction, resulting in fractions including biogas, biofuels, biosolids and biocrude. Silica, phosphates, potash and low concentration nitrogen based fertilizer, along with carbonaceous material can also be recovered.
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公开(公告)号:US20220363616A1
公开(公告)日:2022-11-17
申请号:US17755638
申请日:2020-11-06
Applicant: Eastman Chemical Company
Inventor: David Eugene Slivensky , Daryl Bitting , Kenny Randolph Parker , Michael Gary Polasek , William Lewis Trapp , Xianchun Wu
IPC: C07C29/141 , C07C29/88 , C10G1/00 , C10G9/00
Abstract: A recycle content propanol and method of making a recycle content propanol wherein the recycle content is derived directly or indirectly from the cracking of recycle content pyrolysis oil and/or gas. The cracking of the pyrolysis oil can be conducted in a gas furnace or a split furnace.
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公开(公告)号:US11492556B2
公开(公告)日:2022-11-08
申请号:US16627131
申请日:2018-06-28
Applicant: Neste Oyj
Inventor: Ville Paasikallio , Blanka Toukoniitty , Jukka-Pekka Pasanen
Abstract: The present disclosure relates to co-processing at least a fossil-based feed, pyrolysis liquid and a distillation residue from tall oil distillation in an oil refinery conversion process.
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公开(公告)号:US11479711B2
公开(公告)日:2022-10-25
申请号:US17201709
申请日:2021-03-15
Applicant: Locus Oil IP Company, LLC
Inventor: Sean Farmer , Ken Alibek , Sharmistha Mazumder , Kent Adams , Tyler Dixon , Yajie Chen , Karthik N. Karathur , Nicholas Callow , Blake Ott , Anthony Nerris
Abstract: The invention provides environmentally-friendly compositions and methods for reducing the viscosity of crude oil using microorganisms and/or biosurfactants produced by microorganisms.
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公开(公告)号:US20220259502A1
公开(公告)日:2022-08-18
申请号:US17668937
申请日:2022-02-10
Applicant: Barry Liss
Inventor: Barry Liss
Abstract: A method for thermally converting plastics and biomass, and especially non-recyclable waste plastic and or biomass, to primarily liquid phase hydrocarbons is a three step process comprised of hydrothermal treatment, steam cracking and coking. Plastic or plastic and biomass feedstocks are reduced in particle size to inch minus or smaller and suspended in a liquid slurry. The slurry is pumped to high pressure and heated to a temperature high enough to initiate de-polymerization. The resulting partially de-polymerized slurry is sent to a multi-phase separation system via a pressure reduction valve and thereafter subjected to steam cracking to further reduce the average molecular weight of the hydrocarbon components. The resulting gas phase hydrocarbon mixture is quenched, and naphtha, middle distillate, and heavy oils are condensed out. The residual heavy oil phase is further reduced in pressure and sent to a coker from which additional liquid hydrocarbon product is recovered.
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公开(公告)号:US20220228070A1
公开(公告)日:2022-07-21
申请号:US17648073
申请日:2022-01-14
Applicant: LUMMUS TECHNOLOGY LLC
Inventor: Sudipto Chakraborty , Daniel T. Fernald , David Lee Guymon , Ron Herbanek , Richard John Jibb , Johnny Doyle Combs , Boddie Lynn Lindsey
Abstract: Process and systems for converting waste plastics include feeding a waste plastic to a melt tank, and in the melt tank, heating the waste plastic to form a molten plastic. The molten plastic is withdrawn from the melt tank and fed to a pyrolysis reactor. In the pyrolysis reactor, the molten plastic is heated to a pyrolysis temperature, producing a pyrolysis oil product and a liquid pitch product. The pyrolysis oil is then separated into a pyrolysis gas fraction, a light pyrolysis oil fraction, a medium pyrolysis oil fraction, and a heavy pyrolysis oil fraction.
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