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1. 发明申请

WO2013166235A2 MAXIMIZING AROMATICS PRODUCTION FROM HYDROCRACKED NAPHTHA 审中-公开
标题翻译：最大限度地利用水力石墨制造芳香族化合物
公开(公告)号：WO2013166235A2
公开(公告)日：2013-11-07
申请号：PCT/US2013/039191
申请日：2013-05-02
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
发明人： AL THERWI, Fahad , AL EIDI, Mansoor , AL FUDAIL, Noaman
IPC分类号： C10G59/00 , C10G69/10 , C10L1/06
CPC分类号： C10G35/04 , C10G59/00 , C10G69/10 , C10G2400/30 , C10L1/06
摘要： A gasoline blending components production system useful for producing both aromatics and gasoline blending components from naphtha. The production system includes a light hydrocracked naphtha splitter, a medium hydrocracked naphtha splitter, a naphtha hydrotreater, an isomerization unit, a continuous catalytic reformer and aromatics complex. The production system is operable to produce both refined benzene and para -xylene products in addition to medium hydrocracked naphtha, isomerate, a C7s cut and a C9+ cut, which are useful for gasoline blending without additional treatment. A method for producing gasoline blending components while maximizing aromatic production includes introducing both stabilized hydrocracked naphtha to the light hydrocracked naphtha splitter and straight run naphtha to the naphtha hydrotreater. Operating the production system produces three types of hydrocracked naphtha: a light hydrocracked. naphtha, a medium hydrocracked naphtha and a heavy hydrocracked naphtha. Light and heavy hydrocracked naphtha are directed to the naphtha hydrotreater.
摘要翻译：一种汽油混合组分生产系统，可用于生产石脑油中的芳烃和汽油调和组分。生产系统包括轻质加氢裂化石脑油分离器，介质加氢裂化石脑油分离器，石脑油加氢处理器，异构化单元，连续催化重整器和芳族化合物。除了中等加氢裂化石脑油，异构体，C7s切割和C9 +切割之外，该生产系统可操作地生产精制苯和对二甲苯产物，其可用于汽油混合而无需额外处理。在最大化芳香族生产的同时制备汽油调和组分的方法包括将稳定的加氢裂化石脑油引入轻质加氢裂化石脑油分离器和直馏石脑油到石脑油加氢处理器。经营生产系统生产三种加氢裂化石脑油：轻加氢裂化。石脑油，中等加氢裂化石脑油和重质加氢裂化石脑油。轻质和重质加氢裂化石脑油被引导至石脑油加氢处理器。

2. 发明申请

WO01060950A1 DESULPHURISATION 审中-公开
标题翻译：脱硫
公开(公告)号：WO01060950A1
公开(公告)日：2001-08-23
申请号：PCT/GB2001/000564
申请日：2001-02-09
IPC分类号： C10G29/06 , C10G29/16 , C10G45/08 , C10G49/00 , C10G67/06 , C10G69/02 , C10G69/10
CPC分类号： C10G49/007 , C10G67/06 , C10G69/02 , C10G2300/202 , C10G2300/207 , C10G2300/807
摘要： Desulphurisation of a hydrocarbon feedstock by subjecting a portion of said feedstock to a pre-treatment step of partial oxidation, optionally in the presence of a catalyst, or adiabatic low temperature catalytic steam reforming, thereby forming a gas stream containing hydrogen, and then passing the resultant hydrogen-containing pre-treated gas stream, together with the remainder, of said hydrocarbon feedstock, through a bed of a hydro-desulphurisation catalyst and then through a bed of a particulated absorbent capable of absorbing hydrogen sulphide.
摘要翻译：通过使一部分所述原料进行部分氧化的预处理步骤，任选地在催化剂存在下进行，或绝热的低温催化蒸汽重整，从而形成含有氢的气流，然后通过通过加氢脱硫催化剂的床，然后通过能够吸收硫化氢的颗粒吸收剂的床，将所得的含氢预处理气流与所述烃原料的剩余部分连同。

3. 发明申请

WO2016073394A1 PROCESSES FOR MAXIMIZING HIGH QUALITY DISTILLATE 审中-公开
标题翻译：最大化高品质蒸馏过程
公开(公告)号：WO2016073394A1
公开(公告)日：2016-05-12
申请号：PCT/US2015/058703
申请日：2015-11-03
申请人： UOP LLC
发明人： THAKKAR, Vasant P.
IPC分类号： C10G65/12 , C10G69/02 , C10G69/10
CPC分类号： C10G67/02 , C10G45/02 , C10G45/08 , C10G45/12 , C10G45/58 , C10G45/64 , C10G2300/104 , C10G2300/1044 , C10G2300/1048 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/08
摘要： A process for producing a high quality distillate that meets the ultralow sulfur, cold flow, and distillation requirements. The feed stream is first hydrotreated and dewaxed in the same reactor to provide a hydrotreated and dewaxed effluent. The hydrotreated and dewaxed effluent is separated in a separation zone into a liquid and a vapor phase, the vapor phase comprising a hydrogen containing gas that can be recycled. The liquid phase is separated into at least a diesel stream and a heavy hydrocarbon stream. The heavy hydrocarbon stream is hydrocracked and the hydrocracked effluent may be passed to the reactor for hydrotreating and dewaxing or passed to the separation zone with the hydrotreated and dewaxed effluent.
摘要翻译：生产符合超低硫，冷流和蒸馏要求的高品质馏出物的方法。首先在同一反应器中将进料物流加氢处理和脱蜡以提供加氢处理和脱蜡的流出物。将加氢处理和脱蜡的流出物在分离区中分离成液体和气相，气相包含可再循环的含氢气体。液相被分离成至少柴油流和重质烃流。将重质烃流加氢裂化，并将加氢裂化的流出物送入反应器进行加氢处理和脱蜡，或者与加氢处理和脱蜡的流出物一起进入分离区。

4. 发明申请

WO2016054323A1 PROCESS FOR PRODUCING AROMATICS FROM WIDE-BOILING TEMPERATURE HYDROCARBON FEEDSTOCKS 审中-公开
标题翻译：从锅炉温度上升的原料生产芳烃的方法
公开(公告)号：WO2016054323A1
公开(公告)日：2016-04-07
申请号：PCT/US2015/053412
申请日：2015-10-01
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
发明人： ABUDAWOUD, Raed , AL-AMER, Mohammed
IPC分类号： C10G69/08 , C10G69/10 , C10G59/02 , C10G63/02
CPC分类号： C10G69/02 , C10G59/02 , C10G63/02 , C10G69/08 , C10G69/10 , C10G2400/30
摘要： The present invention relates to methods and systems useful for producing aromatics -rich products from liquid hydrocarbon condensates. The production system includes a hydroprocessing reactor, an aromatization reactor system and a hydrogen extraction unit. The methods for producing the aromatics-rich products include introducing a wide boiling range condensate into the hydroprocessing reactor and operating the aromatics production system such that the hydroprocessing reactor forms a naphtha boiling temperature range liquid product. The liquid hydrocarbons produced in accordance with the present invention may optionally be further processed using a hydrogen extraction unit to produce a high-purity hydrogen fraction.
摘要翻译：本发明涉及用于从液态烃缩合物制备富含芳烃的产物的方法和系统。生产系统包括加氢处理反应器，芳构化反应器系统和氢气提取单元。生产富含芳烃的产品的方法包括将宽沸点冷凝物引入加氢处理反应器并操作芳族化合物生产系统，使得加氢处理反应器形成石脑油沸点温度范围的液体产物。根据本发明生产的液体烃可以任选地使用氢提取单元进一步加工以产生高纯度氢馏分。

5. 发明申请

WO2022034181A1 PROCESS AND PLANT FOR PRODUCING GASOLINE FROM A TAR-CONTAINING FEED 审中-公开
公开(公告)号：WO2022034181A1
公开(公告)日：2022-02-17
申请号：PCT/EP2021/072523
申请日：2021-08-12
申请人： HALDOR TOPSØE A/S
发明人： BEK-PEDERSEN, Erik , ENEVOLDSEN, Søren Selde
IPC分类号： C10G63/04 , C01B3/34 , C10G65/04 , C10G69/10
摘要： The present invention relates to a process and plant for producing hydrocarbon product boiling in the gasoline boiling range from a tar-containing feedstock, the process and 5plant comprising a hydroprocessing stage which includes hydrotreating and hydrocracking for producing diesel and naphtha, and subsequent aromatization of the naphtha thereby also producing a light hydrocarbon gas as liquid petroleum gas (LPG),from which a hydrogen stream is produced.

6. 发明申请

WO2021247068A1 SYSTEMS AND PROCESSES INTEGRATING HYDROPROCESSING AND AN AROMATICS RECOVERY COMPLEX FOR SEPARATING AND UPGRADING HYDROCARBONS 审中-公开
公开(公告)号：WO2021247068A1
公开(公告)日：2021-12-09
申请号：PCT/US2020/057692
申请日：2020-10-28
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
发明人： KOSEOGLU, Omer Refa , HODGKINS, Robert Peter
IPC分类号： C10G45/00 , C10G35/00 , C10G59/00 , C10G7/06 , C10G45/02 , C10G45/44 , B01D3/10 , B01D3/143 , B01J8/22 , B01J8/26 , C10G2300/1055 , C10G2300/107 , C10G2300/1077 , C10G2300/1096 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/208 , C10G2300/301 , C10G2300/308 , C10G2400/04 , C10G69/10
摘要： A process for separating and upgrading a hydrocarbon feed includes passing the hydrocarbon feed to a distillation unit to separate it into at least a naphtha stream and a residue, passing the naphtha stream to a NHT that hydrotreats the naphtha stream to produce a hydrotreated naphtha, passing the hydrotreated naphtha to a NREF that reforms the hydrotreated naphtha to produce a reformate, passing the reformate to an ARC that processes the reformate to produce at least one aromatic product effluent and an aromatic bottoms stream, passing at least a portion of the residue to a residue hydroprocessing unit that hydroprocesses the portion of the residue to produce a hydroprocessed effluent, and passing a portion of the aromatic bottoms stream to the residue hydroprocessing unit to increase the solubility of the asphaltene compounds and reduce sedimentation. Systems for conducting the process are also disclosed.

7. 发明申请

WO2016054316A1 TWO-STEP PROCESS FOR AROMATICS PRODUCTION FROM NATURAL GAS/SHALE GAS CONDENSATES 审中-公开
标题翻译：从天然气/粉煤气混合物生产芳族化合物的两步法
公开(公告)号：WO2016054316A1
公开(公告)日：2016-04-07
申请号：PCT/US2015/053399
申请日：2015-10-01
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
发明人： ABUDAWOUD, Raed
IPC分类号： C10G69/08 , C10G69/10 , C10G59/02 , C10G63/02
CPC分类号： C10G69/02 , C10G59/02 , C10G63/02 , C10G69/08 , C10G69/10 , C10G2400/30
摘要： The aromatics production system is useful for producing an aromatics-rich system product from a liquid hydrocarbon condensate includes a hydroprocessing reactor, an aromatization reactor system and a hydrogen extraction unit. The method for producing the aromatics-rich system product from the wide boiling range condensate includes introducing the wide boiling range condensate into the hydroprocessing reactor, operating the aromatics production system such that the hydroprocessing reactor forms a naphtha boiling temperature range liquid product, such that the aromatization reactor system forms the aromatics-rich system product, and such that the hydrogen extraction unit forms a high-purity hydrogen.
摘要翻译：芳族化合物生产系统可用于从液体烃冷凝物生产富含芳烃的体系产物，包括加氢处理反应器，芳构化反应器系统和氢气提取单元。从广泛的冷冻浓缩物生产富含芳烃的体系产物的方法包括将宽沸点范围的冷凝物引入加氢处理反应器中，操作芳族化合物生产系统，使得加氢处理反应器形成石脑油沸腾温度范围的液体产物，使得芳构化反应器系统形成富含芳烃的体系产物，并且使得氢提取单元形成高纯度氢。

8. 发明申请

WO2008124852A3 FISCHER-TROPSCH JET FUEL PROCESS 审中-公开
标题翻译： FISCHER-TROPSCH喷气式燃料过程
公开(公告)号：WO2008124852A3
公开(公告)日：2009-02-05
申请号：PCT/ZA2008000029
申请日：2008-04-10
申请人： SASOL TECH PTY LTD , DE KLERK ARNO
发明人： DE KLERK ARNO
IPC分类号： C10G2/00 , C10G29/20 , C10G35/04 , C10G47/00 , C10G49/00 , C10G50/00 , C10G69/10 , C10G69/12 , C10G69/14
CPC分类号： C10G50/00 , C10G2/32 , C10G29/205 , C10G35/04 , C10G47/00 , C10G49/00 , C10G69/10 , C10G69/123 , C10G69/126 , C10G69/14 , C10G2300/1022 , C10G2300/4025 , C10G2400/08
摘要： The invention provides a Fischer-Tropsch jet fuel refining process which has a jet fuel yield in excess of 60% by mass, said process including at least four of the following five conversion processes: a. hydrocracking one or more of a FT kerosene and heavier material fraction and a C9 and heavier FT syncrude fraction; b. oligomerising an FT syncrude fraction including hydrocarbons in the range C2 to C8; c. hydrotreating one or more of an FT syncrude fraction, a product from process b.,and an alkylated FT syncrude fraction; d. aromatizing one or more of an FT syncrude fraction including hydrocarbons in the range C2 to C8, a product from process a., a product from process b, a product from process c., and a product from an aromatic alkylation process; and e. alkylating one or more of an FT syncrude fraction including hydrocarbons in the C2 to C6 range, a product from process b., and a product from process d.
摘要翻译：本发明提供了具有超过60质量％的喷气燃料产率的费 - 托喷气燃料精炼方法，所述方法包括以下五种转化方法中的至少四种：a。加氢裂化一种或多种FT煤油和较重物质馏分以及C9和较重的FT合成馏分; 湾使包含C2至C8范围内的烃的FT顺式馏分低聚; C。加氢处理一种或多种FT顺式馏分，来自方法b的产物和烷基化的FT共聚物馏分; 天。将包括C2至C8范围内的烃的FT合成馏分中的一种或多种，来自方法a的产物，来自方法b的产物，来自方法c的产物和来自芳族烷基化方法的产物芳族化; 和e。将包括C2至C6范围内的碳氢化合物的FT合成馏分中的一种或多种，来自方法b的产物和来自方法d的产物烷基化。

9. 发明申请

WO0164816A2 IMPROVED CONVERSION OF SYNGAS FROM FISCHER-TROPSCH PRODUCTS VIA OLEFIN METATHESIS 审中-公开
标题翻译：通过OLEFIN METATHESIS从FISCHER-TROPSCH产品改进SYNGAS
公开(公告)号：WO0164816A2
公开(公告)日：2001-09-07
申请号：PCT/US0106651
申请日：2001-02-28
申请人： CHEVRON USA INC
发明人： O'REAR DENNIS
IPC分类号： C10L1/02 , C07B61/00 , C10G2/00 , C10G47/12 , C10G69/10 , C10L1/08 , C10L10/10 , C10G
CPC分类号： C10G2/30 , C10G2/332 , C10L1/08
摘要： A process for preparing distillate fuel compositions from a C2-6 olefinic fraction and a C20+ fraction via molecular averaging is described. The fractions can be obtained, for example, from Fischer-Tropsch reactions, and/or obtained from the distillation or other processing of crude oil. Molecular averaging converts the fractions to a product that includes a significant fraction in the C5-20 range that can be used for preparing a distillate fuel composition. The product is preferably isomerized to increase the octane value and lower the pour, cloud and smoke point. The product can also be hydrotreated and/or blended with suitable additives for use as a distillate fuel composition.
摘要翻译：描述了通过分子平均从C2-6烯烃级分和C20 +馏分制备馏出物燃料组合物的方法。馏分可以例如从费 - 托反应获得，和/或从原油的蒸馏或其它加工得到。分子平均法将馏分转化成产物，其中可以用于制备馏出物燃料组合物的C5-20范围内的显着部分。产物优选异构化以增加辛烷值并降低倾吐，云和烟点。该产品还可以加氢处理和/或与合适的添加剂共混以用作馏出物燃料组合物。

10. 发明申请

WO2023076013A1 CLEAN LIQUID FUELS HYDROGEN CARRIER PROCESSES 审中-公开
公开(公告)号：WO2023076013A1
公开(公告)日：2023-05-04
申请号：PCT/US2022/045892
申请日：2022-10-06
申请人： CHEVRON U.S.A. INC.
发明人： ZHAN, Bi-Zeng , SONG, Steven Xuqi , OTTO, Trenton , YI, Yaofan
IPC分类号： C10G69/06 , C10G69/10 , C10G69/04
摘要： The present disclosure refers in one embodiment to processes for making and transporting clean hydrogen fuel. The processes may involve hydrotreating, hydrocracking, or both hydrotreating and hydrocracking an aromatic feedstock under conditions to obtain a liquid hydrocarbon fuel. The liquid hydrocarbon fuel is hydrogenated to obtain a hydrogen-rich fuel that is transported to a dehydrogenation facility that may also be at or near a hydrogen station. The hydrogen-rich fuel is used to obtain hydrogen and a second liquid hydrocarbon fuel.

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