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1.发明公开FLEXIBLE PROCESS FOR ENHANCING STEAM CRACKER AND PLATFORMING FEEDSTOCKS 审中-公开卡特彼勒革命叛乱组织VERFAHREN ZUR VERBESSERUNG VON DAMPFCRACKER
公开(公告)号：EP3030634A4
公开(公告)日：2017-03-15
申请号：EP14834026
申请日：2014-05-07
申请人： UOP LLC
CPC分类号： C10G51/06 , C10G9/36 , C10G55/04 , C10G55/08 , C10G61/04 , C10G61/06 , C10G61/10 , C10G63/08 , C10G67/00 , C10G67/06 , C10G67/16 , C10G69/00 , C10G69/06 , C10G69/10 , C10G69/14 , C10G2400/02 , C10G2400/20
摘要： A process for increasing the yields of light olefins or shifting to increase the hydrocarbon components to gasoline blending pools from a hydrocarbon feedstock is presented. The process includes separating a naphtha feedstock to components to a first stream that are more readily processed in a cracking unit and to components in a second stream that are more readily processed in a reforming unit. The process includes the ability to convert components from the cracking stream to the reforming stream, and to convert components from the reforming stream to the cracking stream.
摘要翻译： 提出了一种用于提高轻质烯烃的产率或转移以从烃原料将烃组分增加到汽油混合池的方法。 该方法包括将石脑油原料与组分分离成在裂解装置中更容易加工的第一流和在重整单元中更容易加工的第二流中的组分。 该方法包括将组分从裂化流转化为重整流的能力，并将组分从重整流转化为裂解流。
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公开(公告)号：EP3017024A1
公开(公告)日：2016-05-11
申请号：EP14735909.5
申请日：2014-06-30
CPC分类号： C10G69/02 , C10G65/00 , C10G65/10 , C10G65/18 , C10G67/0445 , C10G69/06 , C10G69/14 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2400/20 , C10G2400/30
摘要： The present invention relates to a process for upgrading refinery heavy residues to petrochemicals, comprising the following steps of: (a) separating a hydrocarbon feedstock in a distillation unit into a to overhead stream and a bottom stream (b) feeding said bottom stream to a hydrocracking reaction area (c) separating reaction products, which are generated from said reaction area of step (b) into a stream rich in mono-aromatics and in a stream rich in poly-aromatics (d) feeding said stream rich in mono-aromatics to a gasoline hydrocracker (GHC) unit, (e) feeding said stream rich in poly-aromatics to a ring opening reaction area.
摘要翻译： 本发明涉及一种将炼油厂重质残渣提炼成石化产品的方法，包括以下步骤：（a）将蒸馏装置中的烃原料分离成塔顶物流，和将塔底料流（b）进料至 加氢裂化反应区域（c）将从步骤（b）的所述反应区域产生的反应产物分离成富含单芳族化合物的流和富含多芳族化合物的流（d）将富含单芳族化合物 到汽油加氢裂化器（GHC）单元，（e）将富含多芳族化合物的物流进料到开环反应区。
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3.发明公开
公开(公告)号：EP2947133A1
公开(公告)日：2015-11-25
申请号：EP15305574.4
申请日：2015-04-16
CPC分类号： C10G67/049 , C10G21/003 , C10G55/06 , C10G65/14 , C10G65/16 , C10G67/0463 , C10G69/14 , C10G2300/301
摘要： L'invention concerne un procédé de conversion d'une charge lourde d'hydrocarbures comprenant les étapes suivantes :a) au moins une étape de désasphaltage sélectif de la charge lourde d'hydrocarbures par extraction liquide/liquide permettant de séparer au moins une fraction asphalte, au moins une fraction d'huile désasphaltée, b) une étape d'hydroconversion de la fraction huile désasphaltée en présence d'hydrogène dans au moins un réacteur triphasique, dans des conditions permettant d'obtenir un effluent comprenant une fraction gazeuse contenant majoritairement les composés H 2 et H 2 S, et une fraction liquide à teneur réduite en carbone Conradson, en métaux, en soufre et en azote, c) une étape de séparation de l'effluent issu de l'étape b) pour obtenir une fraction gazeuse contenant majoritairement les composés H 2 et H 2 S et une fraction liquide à teneur réduite en carbone Conradson, en métaux, en soufre et en azote.
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4.发明授权
公开(公告)号：EP1421157B1
公开(公告)日：2012-08-15
申请号：EP02755093.8
申请日：2002-06-26
发明人： BENAZZI, Eric , GUERET, Christophe
CPC分类号： C10G65/00 , C10G45/62 , C10G47/14 , C10G65/14 , C10G69/14 , C10G2300/1022 , C10G2300/301 , C10G2300/4018 , C10G2300/4081 , C10G2400/04 , C10G2400/06 , C10G2400/08 , Y10S208/95
摘要： The method comprises the following steps: fractionation of the paraffinic product from a Fischer-Tropsch synthesis into at least three fractions, one intermediate fraction boiling between T1 and T2, with T1 between 120 and 200 °C and T2 greater than 300 °C and less than 410 °C, a light fraction with a lower boiling point and a heavy fraction with a higher boiling point; the intermediate fraction is at least partly hydrotreated, then at least partly passed over an amorphous hydroisomerisation/hydrocracking catalyst; the heavy fraction is passed over an amorphous hydroisomerisation/hydrocracking catalyst with a conversion of products boiling at 370 °C+ into products boiling at less than 370 °C of greater than 80 % by weight; and distillation of products from hydrocracking/hydroisomerisation to give medium distillates (kerosene, diesel). An installation is also disclosed.
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5.发明授权
公开(公告)号：EP1777284B1
公开(公告)日：2008-10-01
申请号：EP06291545.9
申请日：2006-10-02
发明人： Coupard, Vincent , Surla, Karine
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6.发明公开
公开(公告)号：EP1972678A1
公开(公告)日：2008-09-24
申请号：EP08290204.0
申请日：2008-02-27
申请人： IFP
CPC分类号： C10G69/123 , C10G29/205 , C10G45/32 , C10G45/40 , C10G69/14 , C10G2400/02
摘要： La présente invention concerne un procédé de traitement d'une charge correspondant à une essence de pyrolyse comprenant :
a) au moins une étape d'hydrogénation sélective appelée HD1 de la charge
b) un fractionnement dans une ou plusieurs colonnes de distillation de l'effluent de l'étape a) afin de produire, au moins une coupe légère C5, une coupe intermédiaire C6 ou C6-C7 ou C6-C8 destinée à la production d'aromatiques, une coupe lourde C7+ ou C8+ ou C9+ destinée à la production d'essence
c) au moins une étape d'hydrodésulfuration et d'hydrogénation profonde de la coupe intermédiaire appelée HD2
d) au moins une étape d'alkylation de la coupe lourde C7+, C8+ ou C9+ en mélange avec une fraction de la coupe légère C5 consistant en un traitement sur catalyseur acide qui permet un alourdissement des composés soufrés
e) au moins une étape de distillation de l'effluent de l'étape d) destinée à produire une fraction légère directement utilisable comme base essence à basse teneur en soufre, et une fraction lourde C11+ ou C12+ riche en composés soufrés et utilisée comme distillat moyen ou fuel.摘要翻译： 治疗电荷裂解汽油的步骤包括：至少电荷的选择性氢化称为HD1; 在多个蒸馏塔氢化流出物的分馏以产生轻馏分C5，C6中间馏分或C6-C7或C6-C8，以及重馏分C7 + C8或+或C9 +; 加氢脱硫和称为HD2中间馏分的深度加氢; 重馏分C7 +，C8 +和至少烷基化C9 +包括在酸催化剂处理; 和烷基化流出物的蒸馏，以产生低的硫含量和重质馏分的C11 +或C12 +富含硫含量的轻馏分。 治疗的电荷裂解汽油的步骤包括：称为HD1的电荷的至少选择性加氢; 在多个蒸馏塔氢化流出物的分馏以产生至少一个光截止C5，C6中间馏分或C6-C7或C6-C8旨在产生芳烃，和重切C7 +或C8 +或旨在产生汽油C9 +; 加氢脱硫和称为HD2中间切口的深度加氢; 重馏分C7 +，C8 +和至少烷基化C9 +包括在酸催化剂的处理引起的硫化合物的一个沉重; 和烷基化流出物中的至少蒸馏以产生富含用作介质馏出物或燃料硫含量直接用作汽油基料硫含量低的轻馏分和重质馏分的C11 +或C12 +。
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7.发明公开A PROCESS OF PRODUCTION OF LOWER OLEFINS AND AROMATICAS 审中-公开VERFAHREN ZUR HERSTELLUNG VON NIEDEREN OLEFINEN UND AROMATEN
公开(公告)号：EP1734098A1
公开(公告)日：2006-12-20
申请号：EP05714812.4
申请日：2005-03-08
发明人： LONG, Juan , DA, Zhijian , LI, Dadong , WANG, Xieqing , SHU, Xingtian , ZHANG, Jiushun , NIE, Hong , XIE, Chaogang , ZHANG, Zhigang , WANG, Wei
CPC分类号： C10G69/04 , C07C4/06 , C07C5/05 , C07C5/11 , C10G11/18 , C10G69/02 , C10G69/06 , C10G69/14 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4018 , C10G2300/4093 , C10G2300/44 , C10G2300/807 , C10G2400/20 , C10G2400/30
摘要： A process for producing light olefins and aromatics, which comprises reacting a feedstock by contacting with a catalytic cracking catalyst in at least two reaction zones, wherein the reaction temperature of at least one reaction zone among the reaction zones downstream of the first reaction zone is higher than that of the first reaction zone and its weight hourly space velocity is lower than that of the first reaction zone, separating the spent catalyst from the reaction product vapor, regenerating the separated spent catalyst and returning the regenerated catalyst to the reactor, and separating the reaction product vapor to obtain the desired products, light olefins and aromatics. This process produces maximum light olefins such as propylene, ethylene, etc from heavy feedstocks, wherein the yield of propylene exceeds 20% by weight, and produces aromatics such as toluene, xylene, etc at the same time.
摘要翻译： 一种生产轻质烯烃和芳族化合物的方法，其包括使原料与至少两个反应区中的催化裂化催化剂接触反应，其中第一反应区下游的反应区中的至少一个反应区的反应温度较高 与第一反应区相比，其重时空速低于第一反应区，将废催化剂与反应产物蒸气分离，再生分离的废催化剂并将再生催化剂返回反应器，并将 反应产物蒸气得到所需产物，轻质烯烃和芳族化合物。 该方法从重质原料中产生最大的轻质烯烃，如丙烯，乙烯等，其中丙烯的产率超过20％（重量），同时产生芳烃如甲苯，二甲苯等。
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公开(公告)号：EP2658954B1
公开(公告)日：2018-03-21
申请号：EP11852243.2
申请日：2011-12-29
IPC分类号： C10G69/00 , C10G69/04 , C10G69/06 , C10G69/14 , C10L1/02 , C10L1/04 , C10G3/00 , C10L1/12 , C10L1/18 , 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 , Y02E50/32 , Y02P20/145 , 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.
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公开(公告)号：EP3225678A3
公开(公告)日：2018-01-03
申请号：EP17151967.1
申请日：2005-03-08
发明人： Long, Jun , Da, Zhijian , Li, Dadong , Wang, Xieqing , Shu, Xingtian , Zhang, Jiushun , Nie, Hong , Xie, Chaogang , Zhang, Zhigang , Wang, Wei
CPC分类号： C10G69/04 , C07C4/06 , C07C5/05 , C07C5/11 , C10G11/18 , C10G69/02 , C10G69/06 , C10G69/14 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4018 , C10G2300/4093 , C10G2300/44 , C10G2300/807 , C10G2400/20 , C10G2400/30
摘要： A process for producing light olefins and aromatics, which comprises reacting a feedstock by contacting with a catalytic cracking catalyst in at least two reaction zones, wherein the reaction temperature of at least one reaction zone among the reaction zones downstream of the first reaction zone is higher than that of the first reaction zone and its weight hourly space velocity is lower than that of the first reaction zone, separating the spent catalyst from the reaction product vapor, regenerating the separated spent catalyst and returning the regenerated catalyst to the reactor, and separating the reaction product vapor to obtain the desired products, light olefins and aromatics. This process produces maximum light olefins such as propylene, ethylene, etc from heavy feedstocks, wherein the yield of propylene exceeds 20% by weight, and produces aromatics such as toluene, xylene, etc at the same time.
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公开(公告)号：EP2880007A4
公开(公告)日：2016-06-08
申请号：EP13826421
申请日：2013-06-05
申请人： CHEVRON USA INC
发明人： TIMKEN HYE KYUNG CHO , DALVAND IZADYAR , CYR DOUGLAS ROBERT , CHENG MICHAEL TUNG-HAI , LUO HUPING , WINTER SHAWN SHLOMO , DRIVER MICHAEL SEAN , MOHR DONALD HENRY
IPC分类号： C07C7/10 , B01J31/02 , B01J38/10 , C07C7/00 , C10G29/20 , C10G45/00 , C10G67/04 , C10G69/14 , C10L1/06 , C10L1/16 , G01N33/28
CPC分类号： G01N33/225 , B01J31/0277 , B01J38/10 , C10G29/205 , C10G45/00 , C10G67/04 , C10G69/14 , C10G2300/301 , C10G2300/305 , C10G2400/02 , C10L1/06 , C10L1/1691
摘要： We provide an extracted conjunct polymer naphtha (45), comprising a hydrogenated conjunct polymer naphtha, from a used ionic liquid catalyst, having a final boiling point less than 246° C. (475° F.), a Bromine Number of 5 or less, and at least 30 wt % naphthenes. We also provide a blended alkylate gasoline (97) comprising the extracted conjunct polymer naphtha (45), and integrated alkylation processes to make the extracted conjunct polymer naphtha (45) and the blended alkylate gasoline (97). We also provide a method to analyze alkylate products, by determining an amount of methylcyclohexane in the alkylate products (80).
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