公开(公告)号：EP4491698A2

公开(公告)日：2025-01-15

申请号：EP24215447.4

申请日：2020-12-23

Applicant: Chevron U.S.A. Inc.

Inventor： TIMKEN, Hye-Kyung C ,  MCCORD, Cameron

IPC: C10G51/04

Abstract: Provided in one embodiment 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 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 pyrolysis oil and optionally wax comprising a naphtha/diesel and heavy fraction, and char. The pyrolysis oil is passed to a refinery FCC unit from which a liquid petroleum gas C 3 olefin/paraffin mixture fraction is recovered, as well as a C 4 olefin/paraffin mixture fraction. In one embodiment, the pyrolysis oil is first passed to a FCC feed pretreater. The liquid petroleum gas C 3 olefin/paraffin mixture fraction is passed to a steam cracker for ethylene production. The C 4 olefin/paraffin mixture fraction is passed to a refinery alkylation unit, from which a n-butane and naphtha feed for a stream cracker to produce ethylene is recovered.

公开(公告)号：EP4433555A1

公开(公告)日：2024-09-25

申请号：EP22830660.1

申请日：2022-11-29

Applicant: Saudi Arabian Oil Company ,  King Abdullah University Of Science And Technology

Inventor： ALMAJNOUNI, Khalid Ali ,  ALABBAD, Shatha Ali ,  ALGHADEER, Abdulelah ,  ALI, Ola ,  OSORIO, Isidoro Morales ,  BOURANE, Abdennour ,  XU, Wei ,  SABATE, Jorge, Gascon ,  VITTENET, Jullian ,  ALABDULLAH, Mohammed ,  RODRIGUEZ-GOMEZ, Alberto ,  KILLINGWORTH, Marcus, John

IPC: C10G9/36 ,  C10G11/00 ,  C10G51/04 ,  B01J8/08

CPC classification number: C10G9/36 ,  C10G11/00 ,  C10G51/04 ,  B01J2208/0058420130101 ,  B01J8/1809 ,  B01J8/24 ,  B01J8/12

公开(公告)号：EP4323474A1

公开(公告)日：2024-02-21

申请号：EP22720213.2

申请日：2022-04-12

Applicant: Chevron Phillips Chemical Company LP

Inventor： ABBOTT, Ronald G. ,  MURRAY, Bruce D. ,  MORRISON, Scott G. ,  PRICE, Bradley T.

IPC: C10G1/10 ,  C10G9/36 ,  C10G1/00 ,  C10G50/00 ,  C10G57/02 ,  C10G1/08 ,  C10G11/18 ,  C10G51/04 ,  C10G63/04

公开(公告)号：EP3470137A1

公开(公告)日：2019-04-17

申请号：EP18199193.6

申请日：2018-10-08

Applicant: IFP Energies nouvelles

Inventor： AMBLARD, Benjamin ,  MARQUES, JOAO ,  LE COZ, Jean-François

IPC: B01J19/24 ,  B01J19/26 ,  C10G47/26 ,  C10G51/04 ,  C10G65/10 ,  C10G65/12 ,  C10G67/04

Abstract: L'invention concerne un dispositif pour l'écoulement descendant d'un liquide hydrocarboné contenant des particules solides en fond d'un équipement (1) comprenant une partie supérieure cylindrique (11) de diamètre D1, une partie inférieure tronconique (12) d'angle d'inclinaison α compris entre 5° et 85°par rapport à l'axe vertical (z) de ladite partie supérieure cylindrique, une conduite de sortie (9) de diamètre D2, caractérisé en ce qu'il comprend au moins une injection (5) de liquide recyclé et/ou d'appoint dans la partie tronconique (12) de l'équipement (1) ; au moins une injection (6) de liquide recyclé et/ou d'appoint dans la partie cylindrique (11) de l'équipement (1) ; la ou lesdites injections (5) situées dans ladite partie tronconique étant inclinées par rapport à la paroi de la partie inférieure tronconique d'un angle β1 dans le plan vertical (xz) et d'un angle β2 dans le plan horizontal (xy); la ou lesdites injections (6) situées dans ladite partie cylindrique étant inclinées par rapport à la paroi de la partie supérieure cylindrique d'un angle θ1 dans le plan vertical (xz) et d'un angle θ2 dans le plan horizontal (xy), les angles β1 et θ1 étant compris entre 5° et 175°, les angles β2 et θ2 étant compris entre 90° et 270°. L'invention concerne également un procédé de conversion de charges hydrocarbonées mettant en oeuvre ledit dispositif.

公开(公告)号：EP2074193A4

公开(公告)日：2013-03-13

申请号：EP06825642

申请日：2006-10-05

Applicant: UOP LLC

Inventor： MARKER TERRY L

IPC: C10G1/00 ,  C07C4/02 ,  C10G1/04 ,  C10G11/00 ,  C10G17/00 ,  C10G17/02 ,  C10G21/00 ,  C10G25/02 ,  C10G51/04 ,  C10G55/06 ,  C10G57/00

CPC classification number: C10G55/06 ,  C10G3/49 ,  C10G3/57 ,  C10G3/62 ,  C10G17/02 ,  C10G25/02 ,  C10G2300/1011 ,  C10G2300/201 ,  C10G2400/02 ,  C10G2400/20 ,  C10G2400/22 ,  Y02P30/20

公开(公告)号：EP2318482A2

公开(公告)日：2011-05-11

申请号：EP09808863.6

申请日：2009-08-21

Applicant: Sud-Chemie Inc.

Inventor： SUN, Mingyong ,  BRYAN, Marty ,  BLANKENSHIP, Steve ,  URBANCIC, Michael, A.

IPC: C10G11/18 ,  C10G51/04 ,  B01J23/46 ,  B01J21/02 ,  B01J21/06

CPC classification number: C07C7/167 ,  B01J23/462 ,  B01J23/48 ,  B01J23/60 ,  B01J23/62 ,  B01J23/6447 ,  B01J23/8926 ,  B01J35/008 ,  B01J35/1009 ,  B01J35/1014 ,  B01J35/1019 ,  B01J37/20 ,  Y02P20/52 ,  C07C11/04

Abstract: A method for purification of ethylene-containing feed streams from steam crackers or fluid catalytic crackers (FCC), wherein the feed streams further comprises hydrogen, carbon monoxide, acetylenes, oxygen, nitrogen oxides, is disclosed. The method comprises contacting an ethylene-comprising gas stream with a Ru-based catalyst at reaction temperatures of at least 120°C. The process results in an ethylene- containing feed stream wherein the ethylene is essentially free of acetylenes, nitrogen oxides and oxygen. The purifying of the feed stream occurs with minimal loss of ethylene.

公开(公告)号：EP2307526A2

公开(公告)日：2011-04-13

申请号：EP09788992.7

申请日：2009-07-24

Applicant: ExxonMobil Research and Engineering Company

Inventor： GORBATY, Martin, L. ,  COOK, Bruce, R. ,  FERRUGHELLI, David, T. ,  ENGLISH, Jason, B. ,  LOWENTHAL, Steven, S.

IPC: C10G51/04 ,  C10G11/18 ,  C10G9/00 ,  B01D3/32

CPC classification number: C10G11/18 ,  B01D3/141 ,  B01D3/32 ,  C10G9/00 ,  C10G2300/1044 ,  C10G2300/1074 ,  C10G2300/4081

Abstract: This invention relates to a process for the selective conversion of vacuum gas oil. The vacuum gas oil is treated in a two step process. The first is thermal conversion and the second is catalytic cracking of the products of thermal conversion. The product slate can be varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step. The combined products from thermal and catalytic cracking are separated in a divided wall fractionator.

公开(公告)号：EP2267101A2

公开(公告)日：2010-12-29

申请号：EP10180884.8

申请日：2003-05-22

Applicant: Total Petrochemicals Research Feluy

Inventor： Grootjans, Jacques f.j. ,  Vanrysselberghe, Valérie ,  Vermeiren, Walter

IPC: C10G51/04 ,  C10G11/05

CPC classification number: C10G11/05 ,  C10G51/04 ,  C10G2300/1044 ,  C10G2300/1088 ,  C10G2300/4018 ,  C10G2300/807 ,  C10G2400/20

Abstract: A process for steam cracking a hydrocarbon feedstock containing olefins to provide increased light olefins in the steam cracked effluent, the process comprising passing a first hydrocarbon feedstock containing one or more olefines through a reactor containing a crystalline silicate to produce an intermediate effluent with an olefin content of lower molecular weight than that of the feedstock, fractionating the intermediate effluent to provide a lower carbon fraction and a higher carbon fraction, and passing the higher carbon fraction, as a second hydrocarbon feedstock, through a steam cracker to produce a steam cracked effluent. There is also provided a process for steam cracking a hydrocarbon feedstock containing olefins to provide increased light olefins in the steam cracked effluent, the process comprising passing a first hydrocarbon feedstock containing one or more olefins, which comprises at least one of a hydrotreated raw C 4 feedstock, LCCS, a raffinate 2 feedstock, a raffinate 1 feedstock, a raffinate 2 feedstock from a methyl tert-butyl ether (MTBE) or an ethyl tert-butyl ether (ETBE) unit, a raffinate from an olefins metathesis unit, in particular for the production of propylene from ethylene and butene, or a hydrotreated olefin-containing stream from an FCC unit, a visbreaker or a delayed coker, through a reactor containing a crystalline silicate to produce an intermediate effluent with an olefin content of lower molecular weight than that of the feedstock, and passing the intermediate effluent as a second hydrocarbon feedstock through a steam cracker to produce a steam cracked effluent. There is further provided a process for steam cracking a hydrocarbon feedstock containing olefins to provide increased light olefins in the steam cracked effluent, the process comprising steam cracking a first hydrocarbon feedstock comprising a paraffin-containing hydrocarbon feedstock and steam cracking a second hydrocarbon feedstock which contains C 4 and higher hydrocarbons, the second hydrocarbon feedstock containing one or more olefins and comprising a bottom fraction of an intermediate effluent produced by catalytic cracking of a third hydrocarbon feedstock in a reactor containing a crystalline silicate to produce the intermediate effluent having an olefin content of lower molecular weight than that of the third feedstock, and combining the two steam-cracked effluents to provide a common effluent.

Abstract translation: 一种用于蒸汽裂解含有烯烃的烃原料以在蒸汽裂解流出物中提供增加的轻质烯烃的方法，该方法包括使含有一种或多种烯烃的第一烃原料通过含有结晶硅酸盐的反应器，以产生具有烯烃含量的中间流出物 的分子量低于原料，分馏中间体流出物以提供低碳馏分和较高的碳馏分，并将作为第二烃原料的较高碳馏分通过蒸汽裂化器通过，以产生蒸汽裂解的流出物。 还提供了一种用于蒸汽裂解含有烯烃的烃原料以在蒸汽裂解的流出物中提供增加的轻质烯烃的方法，该方法包括使含有一种或多种烯烃的第一烃原料通过，所述第一烃原料包含加氢处理的原料C 4 原料，LCCS，萃余液2原料，萃余液1原料，来自甲基叔丁基醚（MTBE）或乙基叔丁基醚（ETBE）单元的萃余液2原料，特别是烯烃复分解单元的萃余液 用于通过含有结晶硅酸盐的反应器从乙烯和丁烯生产丙烯或来自FCC装置的加氢处理的含烯烃流，减粘裂化器或延迟焦化器，以生产具有低于分子量的烯烃含量的中间体流出物 并且将作为第二烃原料的中间流出物通过蒸汽裂化器通过以产生蒸汽裂解的流出物。 进一步提供了一种用于蒸汽裂解含有烯烃的烃原料以在蒸汽裂解流出物中提供增加的轻质烯烃的方法，该方法包括蒸汽裂化包含含链烷烃的烃原料的第一烃​​原料和蒸汽裂化第二烃原料，其含有 C 4和更高级烃，所述第二烃原料含有一种或多种烯烃，并且包含通过在含有结晶硅酸盐的反应器中催化裂化第三烃原料产生的中间流出物的底部馏分，以产生具有烯烃含量的中间体流出物 低于第三种原料的分子量，并且将两种蒸汽裂解废水混合以提供常见的流出物。

公开(公告)号：EP1021497B1

公开(公告)日：2004-09-22

申请号：EP98934435.3

申请日：1998-07-17

Applicant: ExxonMobil Research and Engineering Company

Inventor： SERRAND, Willibald ,  HAMMOND, David, G. ,  JACOBSON, Mitchell ,  PAGEL, John, F. ,  POOLE, Martin, C.

IPC: C10G51/04 ,  C10G55/06 ,  C10G9/32 ,  C10B55/10

CPC classification number: C10G9/32 ,  C10B55/10 ,  C10G25/09 ,  C10G31/06 ,  C10G51/04 ,  C10G55/06 ,  C10G57/00

Abstract: A residuum feedstock is upgraded in a short vapor contact time thermal process unit (11) comprised of a horizontal moving bed of fluidized hot particles and is then fed to a fluid catalytic cracking reactor (17). Hot flue gases from the fluid catalytic cracking regenerator (27) are used to circulate solid particles and to provide process heat to the thermal process unit (11).

公开(公告)号：EP1357166A1

公开(公告)日：2003-10-29

申请号：EP03007551.9

申请日：2003-04-01

Applicant: Linde Aktiengesellschaft

Inventor： Bölt, Heinz ,  Fritz, Helmut ,  Glanz, Stephan, Dr.

IPC: C10G51/02 ,  C10G51/04 ,  C10G55/02 ,  C10G55/04 ,  C10G55/06 ,  C10G7/08 ,  C10G9/20 ,  C10G11/00 ,  C07C7/10

CPC classification number: C10G7/08 ,  C07C4/06 ,  C07C7/08 ,  C10G2400/20 ,  C07C11/02

Abstract: Es werden ein Verfahren und eine Vorrichtung zur Olefinherstellung beschrieben, wobei ein kohlenwasserstoffhaltiger Einsatz, z.B. Naphtha, in einer Behandlungsanlage (1), insbesondere einer Raffinerie oder Olefinanlage, in gewünschte Olefine, z.B. Ethylen und Propylen, umgesetzt wird. Dabei wird zumindest ein Teil der in der Behandlungsanlage (1) anfallenden Fraktionen, die längerkettige, insbesondere mindestens vier Kohlenstoffatome aufweisende, Olefine enthalten, einer Olefinkonversionsstufe (12) zugeführt. In der Olefinkonversionsstufe (12) wird zumindest ein Teil der längerkettigen Olefine in kürzerkettige Olefine umgesetzt. Als Olefinkonversionsstufe kann beispielsweise ein katalytischer Reaktor, insbesondere ein Festbettreaktor, eingesetzt werden. Um die Ausbeute an den gewünschten Olefinen zu erhöhen, wird vorgeschlagen, der Olefinkonversionsstufe (12) eine Paraffin-Olefin-Trennstufe (23) vorzuschalten. In dieser Paraffin-Olefin-Trennstufe (23) wird insbesondere durch Extraktivdestillation eine Auftrennung in Paraffine, z. B. Butan und Pentan, sowie Olefine, z. B. Buten und Penten, durchgeführt. Während die so gewonnenen Paraffine zur Behandlungsanlage (1), z. B. zum Spaltofen (3) der Olefinanlage, zurückgeführt werden, werden die Olefine zur Olefinkonversionsstufe (12) geführt.

Abstract translation: 具有将长链（至少4C）转化为短链烯烃的步骤（12）的烯烃生产使得转化阶段（12）之前是石蜡烯烃分离（23），其中至少部分分离 将石蜡再循环至初始阶段（1）或排出并进行评价，并将至少部分烯烃循环至转化阶段（12）。 烯烃生产涉及将阶段（1）（特别是炼油厂或烯烃设备）中的含烃进料转化成各种馏分，将含有长链（至少4C）烯烃的馏分转化成短链烯烃 其至少部分地再循环到阶段（1），使得转化阶段（12）之前是石蜡烯烃分离阶段（23），其中至少部分分离的石蜡被再循环到阶段（1）或拉伸 并且使用并且至少部分烯烃被再循环到转化级（12）。 对于上述含有烯烃生产装置的独立权利要求也包括分馏装置（6），并且在烯烃转化器（12）之前具有石蜡烯分离器（23），隔板（23）通过石蜡管线连接到 阶段（1）和通过烯烃管线转化为转化段（12）。