公开(公告)号：US20240263091A1

公开(公告)日：2024-08-08

申请号：US18163541

申请日：2023-02-02

申请人： Saudi Arabian Oil Company

发明人： Mansour Ali Al-Herz ,  Ali Al Jawad ,  Qi Xu ,  Aaron Akah ,  Musaed Salem Al-Ghrami ,  Raed Hasan Abudawoud

IPC分类号： C10G69/14 ,  C10G69/04

CPC分类号： C10G69/14 ,  C10G69/04 ,  C10G2300/1033 ,  C10G2300/301 ,  C10G2300/308 ,  C10G2300/4006 ,  C10G2400/20

摘要： A method of processing a hydrocarbon feed may comprise fractionating the hydrocarbon feed into a light stream, a middle stream and a heavy stream; hydrotreating the heavy stream to form a hydrotreated heavy stream; feeding the light stream to a first Fluid Catalytic Cracking (FCC) reaction zone; feeding the middle stream to a second FCC reaction zone; and feeding the hydrotreated heavy stream to a third FCC reaction zone, thereby producing a heavy product stream comprising light olefins; and feeding one or more of the product streams to one or more fractionators, thereby producing one or more finished product streams and one or more recycle streams comprising one or more of light cycle oil (LCO), heavy cycle oil (HCO), and slurry oil; and hydrotreating one or more of the recycle streams to form the hydrotreated heavy stream.

公开(公告)号：US20240018434A1

公开(公告)日：2024-01-18

申请号：US17866035

申请日：2022-07-15

申请人： Saudi Arabian Oil Company

发明人： Qi Xu ,  Aaron Chi Akah ,  Musaed Salem Al-Ghrami ,  Zhonglin Zhang

IPC分类号： C10G69/14 ,  C10G9/36 ,  C10G21/00 ,  C10G11/20 ,  C10G49/22 ,  C10J3/00 ,  C07C6/12 ,  C01B3/24 ,  C10G35/04 ,  C10G7/08

CPC分类号： C10G69/14 ,  C10G9/36 ,  C10G21/003 ,  C10G11/20 ,  C10G49/22 ,  C10J3/00 ,  C07C6/123 ,  C01B3/24 ,  C10G35/04 ,  C10G7/08 ,  C10J2300/16 ,  C01B2203/1241 ,  C01B2203/065 ,  C10G2300/1033 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/301 ,  C10G2300/4081 ,  C10G2300/42 ,  C10G2400/30 ,  C10G2400/20

摘要： An integrated process for upgrading a hydrocarbon oil feed stream includes solvent deasphalting the hydrocarbon oil stream; processing the heavy residual hydrocarbons in a gasification unit to form syngas and gasification residue; hydrotreating the deasphalted oil stream to form a C3-C4 hydrocarbon stream, a light C5+ hydrocarbon stream, and a heavy C5+ hydrocarbon stream; dehydrogenating the C3-C4 hydrocarbon stream to form propylene and butylene; steam enhanced catalytically cracking the light C5+ hydrocarbon stream; steam enhanced catalytically cracking the heavy C5+ hydrocarbon stream; passing at least a portion of the light steam enhanced catalytically cracked stream, the heavy steam enhanced catalytically cracked stream, or both to a product separator to produce a olefin product stream, a naphtha product stream, and a BTX product stream; and processing the naphtha product stream in the aromatics complex to produce benzene and xylenes.

公开(公告)号：US20240018433A1

公开(公告)日：2024-01-18

申请号：US17866029

申请日：2022-07-15

申请人： Saudi Arabian Oil Company

发明人： Qi Xu ,  Aaron Chi Akah ,  Musaed Salem Al-Ghrami ,  Zhonglin Zhang

IPC分类号： C10G69/14 ,  C10G21/00 ,  C10G9/00 ,  C10G9/36 ,  C10G35/04 ,  C10G49/00 ,  C01B3/24 ,  C10G69/12 ,  C10G7/08 ,  C10G11/20

CPC分类号： C10G69/14 ,  C10G21/003 ,  C10G9/005 ,  C10G9/36 ,  C10G35/04 ,  C10G49/007 ,  C01B3/24 ,  C10G69/123 ,  C10G7/08 ,  C10G11/20 ,  C01B2203/065 ,  C01B2203/1241 ,  C10G2300/1033 ,  C10G2300/4018 ,  C10G2300/301 ,  C10G2400/20 ,  C10G2400/30 ,  C10G2300/4081 ,  C01B2203/1628

摘要： An integrated process for upgrading a hydrocarbon oil feed stream utilizing a delayed coker, steam enhanced catalytic cracker, and an aromatics complex includes solvent deasphalting the hydrocarbon oil stream; delayed coking the heavy residual hydrocarbons; hydrotreating the delayed coker product stream and the deasphalted oil stream to form a C3-C4 hydrocarbon stream, a light C5+ hydrocarbon stream, and a heavy C5+ hydrocarbon stream; dehydrogenating the C3-C4 hydrocarbon stream to form propylene and butylene; steam enhanced catalytically cracking the light C5+ hydrocarbon stream; steam enhanced catalytically cracking the heavy C5+ hydrocarbon stream; passing at least a portion of the light steam enhanced catalytically cracked stream, the heavy steam enhanced catalytically cracked stream, or both to a product separator to produce a olefin product stream, a naphtha product stream, and a BTX product stream; and processing the naphtha product stream in the aromatics complex to produce benzene and xylenes.

公开(公告)号：US20240018431A1

公开(公告)日：2024-01-18

申请号：US17865981

申请日：2022-07-15

申请人： Saudi Arabian Oil Company

发明人： Qi Xu ,  Aaron Chi Akah ,  Musaed Salem Al-Ghrami ,  Zhonglin Zhang

IPC分类号： C10G69/14 ,  C10G11/20 ,  C10G21/00 ,  C10G49/22 ,  C10G35/04 ,  C10G9/36 ,  C07C6/12 ,  C01B3/24 ,  C10G7/08

CPC分类号： C10G69/14 ,  C10G11/20 ,  C10G21/003 ,  C10G49/22 ,  C10G35/04 ,  C10G9/36 ,  C07C6/123 ,  C01B3/24 ,  C10G7/08 ,  C10G2400/30 ,  C10G2400/20 ,  C10G2300/301 ,  C10G2300/42 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/1033 ,  C01B2203/065 ,  C01B2203/1241 ,  C10G2300/4081

摘要： In accordance with one or more embodiments herein, an integrated process for upgrading a hydrocarbon oil feed stream utilizing a delayed coker, steam enhanced catalytic cracker, and an aromatics complex includes solvent deasphalting the hydrocarbon oil stream; delayed coking the heavy residual hydrocarbons; hydrotreating the delayed coker product stream and the deasphalted oil stream to form a light C5+ hydrocarbon stream and a heavy C5+ hydrocarbon stream; steam enhanced catalytically cracking the light C5+ hydrocarbon stream; steam enhanced catalytically cracking the heavy C5+ hydrocarbon stream; passing at least a portion of the light steam enhanced catalytically cracked stream, the heavy steam enhanced catalytically cracked stream, or both to a product separator to produce a olefin product stream, a naphtha product stream, and a BTX product stream; and processing the naphtha product stream in the aromatics complex to produce benzene and xylenes.

公开(公告)号：US11802250B1

公开(公告)日：2023-10-31

申请号：US18054169

申请日：2022-11-10

申请人： CHEVRON PHILLIPS CHEMICAL COMPANY LP

发明人： Bruce D. Murray ,  Scott G. Morrison ,  Kenneth Fountain ,  Steven R. Horlacher ,  Vincent D. Mcgahee ,  Reza Khankal ,  David Dockter

IPC分类号： C10G69/14 ,  C10G69/12 ,  C10G67/16 ,  C10G69/08 ,  C10G1/10 ,  C10G1/00

CPC分类号： C10G69/14 ,  C10G1/002 ,  C10G1/10 ,  C10G67/16 ,  C10G69/08 ,  C10G69/126 ,  C10G2300/1003 ,  C10G2400/20 ,  C10G2400/30

摘要： A system for processing plastic waste may include a feed line, a feed fractionator, a hydrotreater, a catalytic reforming unit, a heavy oil cracker, and a steam cracker. A pyrolyzed plastics feed is separated into light, medium, and heavy hydrocarbon streams. The hydrotreater removes sulfur, and the catalytic reforming unit produces a circular aromatic-rich stream. The heavy oil cracker generates cracked streams. The steam cracker produces a circular olefin stream from a cracked stream. A system for processing plastic waste may include the feed line, the feed fractionator, the hydrotreater, a medium hydrocarbon fractionator, the catalytic reforming unit, a full-range reforming unit, the heavy oil cracker, and the steam cracker. The medium hydrocarbon fractionator produces two hydrocarbon streams. The full-range naphtha reforming unit produces a second circular aromatic-rich stream.

公开(公告)号：US20180057758A1

公开(公告)日：2018-03-01

申请号：US15683071

申请日：2017-08-22

申请人： Saudi Arabian Oil Company

发明人： Sameer A. Al-Ghamdi ,  Essam Al-Sayed ,  Ibrahim Abba ,  Abdennour Bourane ,  Alberto Lozano Ballesteros

IPC分类号： C10G51/06 ,  C10G69/14 ,  C10G67/00

CPC分类号： C10G51/06 ,  C10G9/36 ,  C10G11/18 ,  C10G45/02 ,  C10G47/30 ,  C10G67/00 ,  C10G69/14 ,  C10G2300/301 ,  C10G2400/20

摘要： According to an embodiment disclosed, a feedstock hydrocarbon may be processed by a method which may include separating the feedstock hydrocarbon into a lesser boiling point hydrocarbon fraction and a greater boiling point hydrocarbon fraction, cracking the greater boiling point hydrocarbon fraction in a high-severity fluid catalytic cracking reactor unit to form a catalytically cracked effluent, cracking the lesser boiling point hydrocarbon fraction in a steam cracker unit to form a steam cracked effluent, and separating one or both of the catalytically cracked effluent or the steam cracked effluent to form two or more petrochemical products. In one or more embodiments, the feedstock hydrocarbon may include crude oil and one of the petrochemical products may include light olefins.

公开(公告)号：US09447338B2

公开(公告)日：2016-09-20

申请号：US14521171

申请日：2014-10-22

申请人： KiOR, Inc.

发明人： Maria Magdalena Ramirez Corredores ,  Vicente Sanchez Iglesias

IPC分类号： C10L1/00 ,  C10L1/18 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G69/14 ,  C10L1/02 ,  C10L1/04 ,  C10G3/00 ,  C10B49/22 ,  C10B53/02

CPC分类号： C10L1/00 ,  C10B49/22 ,  C10B53/02 ,  C10G3/42 ,  C10G3/50 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G69/14 ,  C10G2300/302 ,  C10L1/02 ,  C10L1/04 ,  C10L1/1817 ,  C10L2200/0469 ,  C10L2290/543 ,  Y02E50/14 ,  Y02P30/20

摘要： Renewable fuels are produced in commercial quantities and with enhanced efficiency by integrating a bio-oil production system with a conventional petroleum refinery so that the bio-oil is co-processed with a petroleum-derived stream in the refinery. The techniques used to integrate the bio-oil production system and conventional petroleum refineries are selected based on the quality of the bio-oil and the desired product slate from the refinery.

摘要翻译： 通过将生物油生产系统与传统的炼油厂相结合，可再生燃料以商业数量生产并提高效率，使生物油与炼油厂的石油衍生物流共同加工。 用于整合生物油生产系统和传统炼油厂的技术是根据生物油的质量和来自炼油厂的期望产品板岩来选择的。

公开(公告)号：US20150368571A1

公开(公告)日：2015-12-24

申请号：US14309623

申请日：2014-06-19

申请人： UOP LLC

发明人： Robert Mehlberg ,  Robert Jason Lee Noe ,  Antoine Negiz ,  Steven F. Zink

IPC分类号： C10G69/08

CPC分类号： C10G69/08 ,  C10G35/04 ,  C10G45/68 ,  C10G69/04 ,  C10G69/14 ,  C10G2400/30

摘要： A method and apparatus for processing hydrocarbons are described. The method includes fractionating a hydrocarbon stream to form at least two fractions. The first fraction is reformed to form a reformate stream, and the reformate stream is introduced into an aromatics processing zone to produce aromatic products. At least a portion of the second fraction is cracked in a fluid catalytic cracking unit. A selectively hydrogenated light naphtha stream is formed by separating the cracked hydrocarbon stream into at least two streams and selectively hydrogenating the light naphtha stream, or selectively hydrogenating the cracked hydrocarbon stream and separating the hydrogenated cracked hydrocarbon stream into at least two streams. Aromatics are extracted from the selectively hydrogenated light naphtha stream forming an extract stream and a raffinate stream. The extract stream is hydrotreated, sent to the aromatics processing zone to produce additional aromatic products.

摘要翻译： 描述了用于处理碳氢化合物的方法和装置。 该方法包括分馏烃流以形成至少两个级分。 将第一馏分重整形成重整产物流，将重整产物流引入芳族化合物处理区以产生芳香族产物。 第二馏分的至少一部分在流化催化裂化装置中裂化。 通过将裂化的烃流分离成至少两股流并选择性地氢化轻质石脑油流，或选择性地氢化裂化的烃流并将氢化裂化的烃流分离成至少两股流形成选择性氢化的轻质石脑油流。 从形成提取物流和萃余液流的选择性氢化轻质石脑油流中提取芳族化合物。 将萃取物流加氢处理，送至芳族化合物处理区产生额外的芳香族产物。

公开(公告)号：US09163199B1

公开(公告)日：2015-10-20

申请号：US14741542

申请日：2015-06-17

申请人： UOP LLC

发明人： Stanley J. Frey ,  Daniel L. Ellig ,  Andrea G. Bozzano ,  Geoffrey W. Fichtl ,  Debarshi Majumder

IPC分类号： C07C2/64 ,  C07C5/22 ,  C11D1/14

CPC分类号： C11D1/143 ,  C07C1/2078 ,  C07C1/213 ,  C07C1/22 ,  C07C2/66 ,  C07C5/2729 ,  C07C5/277 ,  C07C5/333 ,  C07C7/00 ,  C07C7/163 ,  C07C303/02 ,  C07C303/04 ,  C07C309/29 ,  C07C2521/04 ,  C07C2521/06 ,  C07C2521/08 ,  C07C2523/28 ,  C07C2523/75 ,  C07C2523/755 ,  C07C2523/883 ,  C10G3/44 ,  C10G3/45 ,  C10G3/46 ,  C10G3/48 ,  C10G3/50 ,  C10G9/00 ,  C10G29/205 ,  C10G45/32 ,  C10G57/005 ,  C10G69/123 ,  C10G69/14 ,  C10G2300/1014 ,  C10G2400/30 ,  C11D1/22 ,  C11D3/3418 ,  C11D11/04 ,  C07C309/31 ,  C07C9/00 ,  C07C11/02 ,  C07C15/107

摘要： A linear alkyl benzene product and production of linear alkylbenzene from a natural oil are provided. A method comprises the step of deoxygenating the natural oils to form a stream comprising paraffins. The paraffins are dehydrogenated to provide mono-olefins. Then, benzene is alkylated with the mono-olefins under alkylation conditions to provide an alkylation effluent comprising alkylbenzenes and benzene. Thereafter, the alkylbenzenes are isolated to provide the alkylbenzene product.

摘要翻译： 提供直链烷基苯产物和由天然油生产线性烷基苯。 一种方法包括使天然油脱氧以形成包含石蜡的物流的步骤。 将链烷烃脱氢以提供单烯烃。 然后，在烷基化条件下用单烯烃烷基化苯以提供包含烷基苯和苯的烷基化流出物。 此后，分离烷基苯以提供烷基苯产物。

公开(公告)号：US20130338410A1

公开(公告)日：2013-12-19

申请号：US13523741

申请日：2012-06-14

申请人： Haiyan Wang ,  Michael J. McCall

发明人： Haiyan Wang ,  Michael J. McCall

IPC分类号： C10G1/00

CPC分类号： C10G63/02 ,  C10G3/46 ,  C10G3/50 ,  C10G9/00 ,  C10G17/02 ,  C10G25/02 ,  C10G29/205 ,  C10G35/04 ,  C10G45/68 ,  C10G67/00 ,  C10G67/06 ,  C10G67/08 ,  C10G69/00 ,  C10G69/123 ,  C10G69/14 ,  C10G2300/1011 ,  C10G2300/30 ,  Y02P30/20

摘要： A method for producing a linear alkylbenzene product from a bio-renewable feedstock having a mixture of naturally-derived hydrocarbons includes separating the mixture of naturally-derived hydrocarbons into a naphtha portion and a distillate portion, reforming the naphtha portion, and using a high purity aromatics recovery process on the reformed naphtha portion to produce benzene. The method further includes separating a normal paraffins portion from the distillate portion and dehydrogenating the normal paraffins portion to produce mono-olefins. Still further, the method includes reacting the benzene and the mono-olefins to produce the linear alkylbenzene product.

摘要翻译： 从具有天然衍生烃混合物的生物可再生原料生产线性烷基苯产物的方法包括将天然衍生的烃的混合物分离成石脑油馏分和馏出物部分，重整石脑油部分，并使用高纯度 改性石脑油部分的芳烃回收工艺生产苯。 该方法还包括从馏出物部分分离正链烷烃部分并使正链烷烃部分脱氢以生产单烯烃。 此外，该方法包括使苯和单烯烃反应以产生直链烷基苯产物。