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公开(公告)号:US20240409827A1
公开(公告)日:2024-12-12
申请号:US18695552
申请日:2022-10-12
Applicant: SHELL USA, INC.
IPC: C10G55/04 , B01D3/34 , B01D11/04 , B09B3/35 , B09B3/40 , B09B3/80 , B09B101/75 , C10B53/07 , C10B57/10 , C10G9/36
Abstract: The invention relates to a process for converting plastics waste into pyrolysis oil for feeding to a steam cracker including the steps of: pre-washing a stream of comminuted waste plastics in a washing liquid comprising washing water and caustic solution; separating the pre-washed comminuted waste plastics to provide a stream of polyolefin-enriched washed comminuted plastics waste; thermally cracking the stream of polyolefin-enriched washed comminuted plastics waste to produce a vaporised hydrocarbon stream; condensing the vaporised hydrocarbon stream into a liquid hydrocarbon stream and gaseous hydrocarbon stream; washing the liquid hydrocarbon stream with caustic solution; separating the liquid hydrocarbon stream from the caustic solution to produce a stream of caustic-washed liquid hydrocarbon and a stream of spent caustic solution; and rinsing the caustic-washed liquid hydrocarbon stream with water; separating the rinsed liquid hydrocarbon stream from the rinsing water to produce a stream of pyrolysis oil and a stream of spent water.
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公开(公告)号:US20240400916A1
公开(公告)日:2024-12-05
申请号:US18698938
申请日:2022-10-20
Applicant: OMV DOWNSTREAM GMBH
Inventor: Matthias MASTALIR
Abstract: A method for producing a hydrocarbon product from a hydrocarbon mixture containing at least 1 ppm of organically bound halogen includes providing the hydrocarbon mixture containing at least 1 ppm of organically bound halogen, heating the hydrocarbon mixture in order to obtain a gaseous hydrocarbon stream, bringing the gaseous hydrocarbon stream into contact with a composition containing at least one nitrogen compound in order to obtain a gaseous mixture, as a result of which organically bound halogen is converted into halide ions, and separating the halide ions in order to obtain the hydrocarbon product.
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公开(公告)号:US12152206B2
公开(公告)日:2024-11-26
申请号:US17792389
申请日:2020-01-13
Applicant: KELLOGG BROWN & ROOT LLC
Inventor: Samir Saxena , Yellaiahnaidu Mekala
Abstract: The present invention relates to debottleneck solution for delayed Coker unit. More particularly, this invention relates to bottoms of vacuum residuum routed to Coker unit through de-asphalting unit to avoid revamp of existing Coker for the processing of heavier feed stock when there is a change in crude slate. Another object of the invention, in particular, relates to improved delayed coking products, a process used in petroleum refineries to crack petroleum residue, thus converting it into gaseous and liquid product streams and leaving behind solid, carbonaceous petroleum coke.
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公开(公告)号:US20240182800A1
公开(公告)日:2024-06-06
申请号:US18512204
申请日:2023-11-17
Applicant: ExxonMobil Chemical Patents Inc.
Inventor: Rainer Kolb , Brian W. Satterley
CPC classification number: C10G55/04 , C10B53/07 , C10G2300/1003 , C10G2300/4006
Abstract: Methods for absorbing residual hydrocarbon liquids from plastic waste including obtaining hydrocarbon liquid-fouled plastic waste shreds, wherein the plastic waste shreds have a particle size of about 0.1 inches to about 3 inches; admixing the hydrocarbon liquid-fouled plastic waste shreds with absorbent elastomer granules, wherein the absorbent elastomer granules have a particle size of about 0.05 inches to about 2 inches; wherein the ratio of absorbent elastomer to hydrocarbon liquid-fouled plastic is about 1:4 to about 4:1 by weight; and agitating the mixture for a period of time.
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公开(公告)号:US20240158705A1
公开(公告)日:2024-05-16
申请号:US18388968
申请日:2023-11-13
Applicant: SK Innovation Co., Ltd.
Inventor: Sang Hwan Jo , Soo Kil Kang , Ik Hwan Na , Ho Won Lee , Jae Heum Jung , Se Rah Moon , Hee Young Jeon
CPC classification number: C10G55/04 , C10G1/002 , C10G1/10 , C10G9/04 , C10G55/06 , C10G70/043 , C10G2300/1003 , C10G2300/202 , C10G2300/4006 , C10G2300/4081
Abstract: The present disclosure provides a method and device for refining waste plastic pyrolysis oil, the method including (S1) subjecting a waste plastic pyrolysis oil feedstock to a heat treatment by charging the waste plastic pyrolysis oil feedstock into a rotary kiln reactor and increasing a temperature of the rotary kiln reactor to form a product; (S2) recovering a gas component from the product of step (S1); (S3) separating a high boiling point wax component from the recovered gas component and re-supplying the separated high boiling point wax component to the rotary kiln reactor in step (S1); and (S4) recovering refined oil from the gas component from which the high boiling point wax component is removed.
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公开(公告)号:US11976245B2
公开(公告)日:2024-05-07
申请号:US17453799
申请日:2021-11-05
Inventor: Essam Abdullah Al-Sayed , Ujjal Mukherjee , Kareemuddin Shaik , Pedro Santos , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald Venner , Raghu Narayan , Meredith Lansdown
IPC: C10G69/06 , B01J19/24 , C10G9/36 , C10G21/00 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/00
CPC classification number: C10G69/06 , B01J19/245 , C10G9/36 , C10G21/003 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/0057 , B01J2219/0004 , C10G2300/1044 , C10G2300/1048 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/308 , C10G2300/40 , C10G2300/4006 , C10G2300/4081 , C10G2300/807 , C10G2400/20 , C10G2400/22 , C10G2400/30
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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公开(公告)号:US20240076561A1
公开(公告)日:2024-03-07
申请号:US18261705
申请日:2021-11-22
Applicant: SABIC Global Technologies B.V.
Inventor: Thomas DIJKMANS , Safa FARAJZADEH BIBALAN , Johannes Maria MAAS , Gerardus Theodorus Cornelis KWAKKENBOS , Christoph ROOSEN , Philip Roydon EDWARDS
IPC: C10G55/04
CPC classification number: C10G55/04 , C10G2300/1044 , C10G2300/1081 , C10G2300/1096 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/802
Abstract: A system and a method for steam cracking hydrocarbons are disclosed. The system includes a steam cracking system comprising a first steam cracking furnace and a second steam cracking furnace. A hydrocarbon feed stream is fed into a convection section of a first steam cracking furnace. The preheated feed stream is mixed with steam and then separated into a light vapor stream and a heavy stream in a vapor-liquid separation unit. The light vapor stream is further steam cracked in a radiant section of the first steam cracking furnace. The heavy stream is further heated and steam cracked in the second steam cracking furnace.
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公开(公告)号:US20240076558A1
公开(公告)日:2024-03-07
申请号:US18273928
申请日:2022-01-24
Applicant: TotalEnergies OneTech , TOTALENERGIES RAFFINAGE CHIMIE
Inventor: Thomas COUSTHAM , Marfiza Victoria BERRIO NAVARRO , Hélène COULOMBEAU-LEROY , Sébastien LEPLAT , Quentin LESUEUR , Didrik HAUDEBOURG
CPC classification number: C10G21/16 , C10G1/002 , C10G1/10 , C10G21/12 , C10G21/20 , C10G55/04 , C10G2300/1003 , C10G2300/202 , C10G2300/44
Abstract: The invention relates to a method for purifying a pyrolysis oil originating from the pyrolysis of waste including plastics by liquid/liquid extraction. This extraction is performed by means of a polar solvent that is immiscible with pyrolysis oil, for which a recovery rate is obtained greater than or equal to 0.95, this recovery rate being defined as the ratio of the extract volume over the initial volume of solvent, this extract being a phase containing the solvent which is immiscible with pyrolysis oil, recovered after agitation then decantation of a mixture of one part by volume of solvent with twenty-five parts by volume of pyrolysis oil at atmospheric pressure and at a temperature of 20° C.
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公开(公告)号:US11891574B2
公开(公告)日:2024-02-06
申请号:US17441380
申请日:2020-04-14
Applicant: SHELL OIL COMPANY
Inventor: Jean-Paul Andre Marie Joseph Ghislain Lange , Luis Alberto Grau Lisnier , Willem Derks , Kai Jürgen Fischer
CPC classification number: C10G1/002 , C10G21/006 , C10G21/02 , C10G55/04 , C10G1/10
Abstract: The invention relates to a process for the recovery of aliphatic hydrocarbons from a liquid hydrocarbon feedstock stream, which comprises aliphatic hydrocarbons and additionally comprises aromatic hydrocarbons and/or polar components, said process comprising the steps of: feeding the liquid hydrocarbon feedstock stream to a first column; feeding a first solvent stream which comprises an organic solvent to the first column at a position which is higher than the position at which the liquid hydrocarbon feedstock stream is fed; contacting at least a portion of the liquid hydrocarbon feedstock stream with at least a portion of the first solvent stream; and recovering at least a portion of the aliphatic hydrocarbons by liquid-liquid extraction of aromatic hydrocarbons and/or polar components with organic solvent, resulting in a stream comprising recovered aliphatic hydrocarbons and optionally organic solvent and a bottom stream from the first column comprising organic solvent and aromatic hydrocarbons and/or polar components.
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公开(公告)号:US11840673B2
公开(公告)日:2023-12-12
申请号:US17843990
申请日:2022-06-18
Inventor: Ujjal Mukherjee , Essam Abdullah Al-Sayed , Pedro Santos , Kareemuddin Shaik , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald M. Venner , Abdul Rahman Zafer Akhras
IPC: C10G69/06 , B01J19/24 , C10L1/08 , C10G45/26 , C10G45/32 , C10G45/44 , C10G49/22 , C10G65/12 , C10G9/36 , C10G47/30 , C10G49/02 , C10G21/00 , C10G47/26 , C10G55/04 , B01D3/06 , B01D19/00
CPC classification number: C10G69/06 , B01J19/245 , C10G9/36 , C10G21/003 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/0057 , B01J2219/0004 , C10G2300/1044 , C10G2300/1048 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/308 , C10G2300/40 , C10G2300/4006 , C10G2300/4081 , C10G2300/807 , C10G2400/20 , C10G2400/22 , C10G2400/30
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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