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1. 发明授权

EP3541893B1 PROCESS FOR CONVERSION OF CRUDE OIL TO PETROCHEMICALS AND FUEL PRODUCTS INTEGRATING VACUUM GAS OIL HYDROTREATING AND STEAM CRACKING 有权
公开(公告)号：EP3541893B1
公开(公告)日：2021-10-20
申请号：EP17808716.9
申请日：2017-11-20
发明人： AL-GHAMDI, Mohammed, Saeed
IPC分类号： C10G9/36 , C10G45/00 , C07C7/08 , C10G7/08 , C10G69/06 , C10G69/08 , C10G47/00 , C10G7/06 , C10G21/00 , C10G69/00 , C10G67/00

2. 发明授权

EP2913383B1 OLEFIN AND SINGLE-RING AROMATIC HYDROCARBON PRODUCTION METHOD 有权
公开(公告)号：EP2913383B1
公开(公告)日：2019-08-21
申请号：EP13848235.1
申请日：2013-10-25
申请人： JX Nippon Oil & Energy Corporation
发明人： YANAGAWA Shinichiro , KOBAYASHI Masahide , YOSHIWARA Yukihiro
IPC分类号： C10G51/04 , C07B61/00 , C07C4/06 , C07C7/04 , C07C11/04 , C07C11/06 , C07C11/08 , C07C15/04 , C07C15/06 , C07C15/08 , C10G9/00 , C10G11/05 , C10G45/50 , C10G69/06 , C10G35/095 , C10G63/04 , C10G69/08

3. 发明授权

EP3201296B1 PROCESS FOR PRODUCING AROMATICS FROM WIDE-BOILING TEMPERATURE HYDROCARBON FEEDSTOCKS 失效
公开(公告)号：EP3201296B1
公开(公告)日：2019-06-26
申请号：EP15781261.1
申请日：2015-10-01
申请人： Saudi Arabian Oil Company
发明人： ABUDAWOUD, Raed , AL-AMER, Mohammed
IPC分类号： C10G69/08 , C10G69/10 , C10G59/02 , C10G63/02

4. 发明公开

EP2913383A4 OLEFIN AND SINGLE-RING AROMATIC HYDROCARBON PRODUCTION METHOD, AND ETHYLENE PRODUCTION DEVICE 有权
标题翻译：制备烯烃和芳烃单环烃及乙烯生产装置的方法
公开(公告)号：EP2913383A4
公开(公告)日：2016-07-13
申请号：EP13848235
申请日：2013-10-25
申请人： JX NIPPON OIL & ENERGY CORP
发明人： YANAGAWA SHINICHIRO , KOBAYASHI MASAHIDE , YOSHIWARA YUKIHIRO
IPC分类号： C10G51/04 , C07B61/00 , C07C4/06 , C07C7/04 , C07C11/04 , C07C11/06 , C07C11/08 , C07C15/04 , C07C15/06 , C07C15/08 , C10G9/00 , C10G11/05 , C10G35/095 , C10G45/50 , C10G63/04 , C10G69/06 , C10G69/08
CPC分类号： C10G11/05 , B01J19/245 , B01J2219/24 , C10G35/04 , C10G35/095 , C10G63/04 , C10G69/04 , C10G69/06 , C10G69/08 , C10G2300/1051 , C10G2300/1055 , C10G2400/20 , C10G2400/22 , C10G2400/30
摘要： A method for producing an olefin and a monocyclic aromatic hydrocarbon of the present invention includes a cracking and reforming reaction step of obtaining a product containing an olefin and a monocyclic aromatic hydrocarbon by bringing a feedstock oil which is a thermally-cracked heavy oil obtained from an apparatus for producing ethylene which includes a cracking furnace and a product collection device that separates and collects an olefin and an aromatic hydrocarbon from a cracked product produced in the cracking furnace and which has a 90 volume% distillate temperature, as a distillation characteristic, of 390°C or lower into contact with a catalyst and reacting the feedstock oil; and a product collection step of collecting the olefin and the monocyclic aromatic hydrocarbon respectively by treating the product obtained in the cracking and reforming reaction step using the product collection device in the apparatus for producing ethylene.
摘要翻译：本发明的烯烃和单环芳香族烃的制造方法包括裂化和重整反应步骤，通过将作为热裂化重质油的原料油（由用于生产乙烯的装置包括裂解炉和从裂解炉中产生的裂化产物中分离和收集烯烃和芳烃并且具有90体积％馏出物温度作为蒸馏特性的产物收集装置，其为390 ℃以下与催化剂接触并使原料油反应; 以及通过在乙烯生产装置中使用产品收集装置处理在裂化和重整反应步骤中获得的产物分别收集烯烃和单环芳烃的产物收集步骤。

5. 发明公开

EP2617797A4 AROMATIC HYDROCARBON PRODUCTION PROCESS 有权
标题翻译：方法的芳香族烃
公开(公告)号：EP2617797A4
公开(公告)日：2015-10-28
申请号：EP11825186
申请日：2011-09-14
申请人： JX NIPPON OIL & ENERGY CORP
发明人： YANAGAWA SHINICHIRO , IDA RYOJI , KOBAYASHI MASAHIDE
IPC分类号： C10G65/12 , B01J29/40 , C07B61/00 , C07C4/18 , C07C6/06 , C07C15/02 , C10G9/00 , C10G35/095 , C10G45/68 , C10G47/20 , C10G69/08
CPC分类号： C07C4/06 , B01J23/882 , B01J29/06 , B01J29/061 , B01J29/405 , B01J35/023 , B01J37/0009 , B01J37/0045 , B01J2229/186 , C01B39/065 , C01B39/40 , C07C4/18 , C07C2529/40 , C10G9/00 , C10G29/205 , C10G35/095 , C10G45/68 , C10G51/04 , C10G57/005 , C10G63/04 , C10G65/046 , C10G69/04 , C10G69/06 , C10G69/08 , C10G2300/301 , C10G2300/4012 , C10G2300/4018 , C10G2400/30 , Y02P20/52 , C07C15/02
摘要： Provided is a method for producing aromatic hydrocarbons, by which a feedstock containing a hydrogenation-treated oil of a thermally cracked heavy oil obtainable from an ethylene production apparatus is brought into contact with a catalyst for monocyclic aromatic hydrocarbon production containing a crystalline aluminosilicate, and thereby aromatic hydrocarbons are produced. A raw material having an end point of the distillation characteristics of 400°C or lower is used as the feedstock. The contact between the feedstock and the catalyst for monocyclic aromatic hydrocarbon production is carried out at a pressure of 0.1 MPaG to 1.5 MPaG.

6. 发明公开

EP2554635A1 METHOD FOR PRODUCING AROMATIC HYDROCARBONS, AND AROMATIC HYDROCARBON PRODUCTION PLANT 有权
标题翻译：方法生产芳烃和系统芳烃生产
公开(公告)号：EP2554635A1
公开(公告)日：2013-02-06
申请号：EP11759554.6
申请日：2011-03-25
申请人： Chiyoda Corporation , JX Nippon Oil & Energy Corporation
发明人： MINAMI, Hideki , SUGI, Yoshishige , FUKUI, Atsushi , NAGUMO, Atsuro , YASUI, Susumu , YANAGAWA, Shinichiro
IPC分类号： C10G69/08 , B01J23/08 , C07C4/00 , C07C15/02 , C10G35/10 , C07B61/00
CPC分类号： B01J8/20 , B01D3/143 , B01J21/04 , B01J23/882 , B01J23/883 , B01J23/885 , B01J23/888 , B01J23/8885 , B01J29/068 , B01J29/405 , B01J35/023 , B01J2229/183 , C07C4/06 , C10G35/04 , C10G69/10 , C10G2300/1044 , C10G2300/1059 , C10G2300/42 , C10G2400/28 , C10G2400/30
摘要： A method for producing aromatic hydrocarbons, the method including: (a) bringing a feedstock oil such as an LCO into contact with an aromatic production catalyst to obtain a reaction product containing aromatic hydrocarbons, (b) separating the reaction product into a tower top fraction and a tower bottom fraction using a distillation tower, (c) separating the tower top fraction into a crude aromatic fraction containing an LPG fraction, and an off-gas containing hydrogen, (d) separating the crude aromatic fraction containing an LPG fraction into an LPG fraction and a crude aromatic fraction, (e) separating the off gas containing hydrogen into hydrogen and an off-gas, and (f) using the hydrogen obtained in step (e) to hydrotreat the crude aromatic fraction, thereby obtaining an aromatic fraction.
摘要翻译：一种用于生产芳烃的方法，该方法包括：（a）使原料油：如LCO接触到芳族生产催化剂，得到的反应产物包含芳族烃，（b）反应产物分离成塔顶馏分和塔底部馏分使用蒸馏塔，（c）分离的塔顶馏分分离成粗芳烃馏分含LPG的分数，和氢废气中含有（d）分离粗芳香馏分含到LPG馏分成 LPG馏分和粗芳族级分，（e）分离的尾气含氢成氢气，并在废气，并使用在步骤（e）中得到的氢至（f）加氢处理的粗芳香馏分，由此得到芳族级分的，

7. 发明公开

EP2426189A1 Procédé de production de carburants kérosène et diesel à partir de coupes insaturées légeres et de coupes aromatiques riches en BTX 有权
标题翻译：一种用于从光的和不饱和富芳族单元的生产煤油和柴油燃料的过程BTX-
公开(公告)号：EP2426189A1
公开(公告)日：2012-03-07
申请号：EP11290375.2
申请日：2011-08-17
申请人： IFP Energies nouvelles
发明人： Coupard, Vincent , Pucci, Annick , Debuisschert, Quentin
IPC分类号： C10G50/00 , C10G45/02 , C10G45/32 , C10G45/00 , C10G69/12 , C10G69/04 , C10G69/08 , C10G67/06 , C10G25/02
CPC分类号： C10G50/00 , C10G25/02 , C10G45/00 , C10G45/02 , C10G45/32 , C10G67/06 , C10G69/04 , C10G69/08 , C10G2300/104 , C10G2300/1044 , C10G2300/1096 , C10G2300/301 , C10G2300/4018 , C10G2400/04
摘要： Procédé de production de carburants kérosène et diesel à partir d'une coupe dite naphta craqué léger, à laquelle on peut ajouter une quantité quelconque de coupe LPG, et d'une coupe aromatique riche en BTX, faisant appel à une étape d'oligomérisation d'oléfines et d'alkylation des oléfines sur les aromatiques.
摘要翻译：该方法包括执行选择性氢化步骤以启动汽油馏分，在40的温度下处理的流出物从与沸石或氧化硅 - 氧化铝型酸催化剂或离子交换树脂的酸催化剂的加氢步骤中得到至250℃，压力 10-30条和0.3-2 H-1，并在第一蒸馏塔中蒸馏该流出物的烯烃馏分的分离具有60的终沸点的空间速度？和的沸点的分数大于150℃实施，所述方法包括执行选择性氢化步骤以启动汽油馏分，治疗流出物从与沸石或氧化硅 - 氧化铝型酸催化剂或离子交换树脂的酸催化剂的加氢步骤中得到在40至250℃，10〜30巴的压力和0.3-2小时-1的空间速度，馏在第一蒸馏柱的流出物的烯烃馏分的分离具有的终沸点的温度 60？在其顶部和沸点在其底部，在那里大于150 [度]的C沸点的馏分被送至加氢处理单元大于150 [度]的C点，低聚的烯烃馏分与任意混合的一小部分其被发送到朝向加氢处理单元并朝向总加氢单元（HT）的第二部分，和数据流的执行烷基化的第一部分液化石油气馏分含烯烃，提取低聚的烯烃流，蒸馏后，构成一个煤油馏分，所有从对BTX馏分富含含6-9 C.烷基化单元的流出物的芳族化合物的低聚步骤中获得被发送到第二蒸馏塔中提取的级分组成为：小于100 [度]的沸点的汽油馏分 C，其中该馏分被发送到汽油池; 在在100-150 [℃，其中所述级分构成的未反应的BTX的并在循环的烷基化单元的入口与构成烷基化单元的吹扫和馏分的一部分的例外蒸馏中间馏分送入以稳定后汽油池; 和大于150℃，其中该馏分被发送到总加氢单元的期望的柴油被提取的沸点的重质馏分。氢化步骤是在100至350℃，20〜70巴的压力和0.5-5小时-1的空间速度的温度下进行。

8. 发明授权

EP1370629B1 PROCEDE DE PRODUCTION D'ESSENCE A FAIBLE TENEUR EN SOUFRE 有权
标题翻译：程序的生产是一个可靠的地区EN SOUFRE
公开(公告)号：EP1370629B1
公开(公告)日：2011-03-23
申请号：EP02701342.4
申请日：2002-01-29
申请人： Institut Français du Pétrole
发明人： DEBUISSCHERT, Quentin , UZIO, Denis , NOCCA, Jean-Luc , PICARD, Florent
IPC分类号： C10G69/12 , C10G69/08
CPC分类号： C10G69/12 , C10G11/02 , C10G25/00 , C10G29/205 , C10G45/02 , C10G45/32 , C10G65/00 , C10G65/06 , C10G67/08 , C10G69/00 , C10G69/04 , C10G69/08 , C10G69/123 , C10G2300/202 , C10G2300/207 , C10G2400/02
摘要： The invention relates to a method for producing low-sulphur petrol comprising at least one sulphur compound transformation step consisting of the alkylation or adsorption of the sulphur compounds and/or in increasing the weight of the light sulphur compounds; at least one step involving treatment in the presence of an acid catalyst; and at least one step consisting in desulphurising at least one part of the petrol. According to the invention, the method can also optionally comprise at least one step involving the selective hydrogenation of diolefins and, optionally, at least one fractionation of the petrol obtained into at least two fractions: light petrol and heavy petrol.
摘要翻译：本发明涉及生产低硫汽油的方法，其包括至少一个由硫化合物的烷基化或吸附和/或增加轻质硫化合物的重量组成的硫化合物转化步骤; 至少一个涉及在酸催化剂存在下处理的步骤; 并且至少一个步骤包括脱硫汽油的至少一部分。根据本发明，所述方法还可以任选地包含至少一个涉及二烯烃的选择性加氢的步骤，并且任选地将所获得的汽油的至少一个馏分分馏成至少两个馏分：轻质汽油和重质汽油。

9. 发明公开

EP2149594A1 Production of gasoline using new method, blending of petroleum material cuts 审中-公开
标题翻译：天ung on on on itten itten itten itten itten itten itten itten itten itten itten itten itten itten itten itten itten itten itten itten itten itten
公开(公告)号：EP2149594A1
公开(公告)日：2010-02-03
申请号：EP09251755.6
申请日：2009-07-08
申请人： Pircheraghali, Mohammadreza , Pircheraghali, Ali Akbar
发明人： Pircheraghali, Mohammadreza , Pircheraghali, Ali Akbar
IPC分类号： C10G35/04 , C10G69/08 , C10L1/06
CPC分类号： C10G69/08 , C10G35/04 , C10G61/02 , C10L1/06
摘要： A method of producing a reformate suitable for use in the production of gasoline, comprising the steps of: obtaining naphtha heart cut (C5-C10 + ) from the distillation of gas condensate; removing undesired impurities from said naphtha heart cut (C5-C10 + ) by a hydrotreating step to produce hydrotreated naphtha heart cut (C5-C10 + ); and subjecting said hydrotreated naphtha heart cut (C5-C10 + ) to a catalytic reforming step to produce said reformate, wherein the temperature of said catalytic reforming step is selected to be in the range 485-510 °C; and/or an amount of hydrotreated naphtha heart cut (C5-C10 + ) is mixed with said reformate such that said reformate contains up to 45 %volume of hydrotreated naphtha heart cut (C5-C10 + ), so as to reduce the %volume of aromatics in said reformate. In addition, the invention comprises a method of producing a gasoline using such a reformate and also a gasoline comprising such a reformate.
摘要翻译：一种生产适用于生产汽油的重整产品的方法，包括以下步骤：从气体冷凝物的蒸馏中获得石脑油切碎（C5-C10 +）; 通过加氢处理步骤从所述石脑油心脏切口（C5-C10 +）中除去不需要的杂质以产生加氢处理的石脑油心脏切口（C5-C10 +）; 将所述加氢处理的石脑油切碎（C5-C10 +）进行催化重整步骤以制备所述重整油，其中所述催化重整步骤的温度选择在485-510℃的范围内; 和/或加氢处理的石脑油心切（C5-C10 +）的量与所述重整产物混合，使得所述重整产物含有高达45体积％的加氢处理的石脑油心脏切割（C5-C10 +），从而减少体积％的重整油中的芳烃。此外，本发明包括使用这种重整产物生产汽油的方法，以及包含这种重整油的汽油。

10. 发明公开

EP1065255A4 METHOD OF ISOMERIZING LIGHT HYDROCARBON OIL 审中-公开
标题翻译：轻烃油的方法异构化
公开(公告)号：EP1065255A4
公开(公告)日：2003-03-12
申请号：EP98961531
申请日：1998-12-24
申请人： COSMO RES INST , COSMO OIL CO LTD
发明人： MIZUNO KUNIHIKO , KIMURA TAKAO , KAWAMURA TAKAHIRO , DOUTA MASAHIKO , OHSHIO NOBUYASU
IPC分类号： B01J23/88 , B01J27/053 , C10G35/085 , C10G45/06 , C10G45/10 , C10G45/60 , C10G45/62 , C10G65/02 , C10G65/04 , C10G69/08 , B01J21/06 , C10G45/08
CPC分类号： C10G65/043 , C10G45/60
摘要： A process for isomerizing a light hydrocarbon oil which comprises: subjecting the light hydrocarbon oil to a hydrogenation treatment for converting an organosulfur component in the light hydrocarbon oil into hydrogen sulfide to give an organosulfur content of from 0 to 30 mass ppm as a pretreatment step; and isomerizing the light hydrocarbon oil still containing the converted hydrogen sulfide in the presence of a solid super strong acid catalyst under conditions at a temperature of from 190 to 300 DEG C, a pressure of from 1 to 50 kg/cm g, an H2/oil ratio of from 180 to 1800 liter/liter, and an LHSV of from 2 to 10 hr as an isomerization step.

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