公开(公告)号：EP2819780B1

公开(公告)日：2024-06-26

申请号：EP13701665.5

申请日：2013-01-31

IPC: B01J29/70 ,  B01J29/74 ,  C07C5/27 ,  C10G45/64

CPC classification number: B01J29/703 ,  C10G45/64 ,  B01J2229/1620130101 ,  B01J2229/18620130101 ,  B01J2229/3220130101 ,  B01J2229/3720130101 ,  B01J2229/4220130101 ,  C10G73/02 ,  C10G45/62 ,  B01J29/7461

公开(公告)号：EP2781497B1

公开(公告)日：2018-08-08

申请号：EP14305340.3

申请日：2014-03-10

Applicant: IFP Energies nouvelles

Inventor： Marques Mota, Filipe Manuel ,  Bouchy, Christophe ,  Duchene, Pascal ,  Martens, Johan

IPC: C07C5/27 ,  C10G45/62 ,  C07C9/22 ,  C10G45/64 ,  B01J29/80

CPC classification number: B01J29/80 ,  B01J29/7261 ,  B01J29/7284 ,  B01J29/7461 ,  B01J29/7484 ,  B01J37/28 ,  B01J2229/186 ,  B01J2229/40 ,  C07C5/2775 ,  C07C5/2791 ,  C07C2529/70 ,  C07C2529/80 ,  C10G45/60 ,  C10G45/62 ,  C10G45/64 ,  C07C9/22

公开(公告)号：EP1551941B1

公开(公告)日：2018-07-18

申请号：EP03774622.9

申请日：2003-10-07

Applicant: ExxonMobil Research and Engineering Company

Inventor： MURPHY, William, J. ,  CODY, Ian, A.

IPC: C10G45/02 ,  C10G45/08 ,  C10G45/12 ,  C10G45/58 ,  C10G45/60 ,  C10G45/62 ,  C10G45/64 ,  C10G65/04 ,  C10G69/00 ,  B01J29/04 ,  B01J29/068 ,  B01J29/74 ,  C10M171/02

CPC classification number: B01J29/068 ,  B01J29/041 ,  B01J29/74 ,  B01J29/7461 ,  B01J2229/12 ,  B01J2229/34 ,  C10G45/02 ,  C10G45/08 ,  C10G45/12 ,  C10G45/58 ,  C10G45/60 ,  C10G45/62 ,  C10G45/64 ,  C10G65/043 ,  C10G69/00 ,  C10G2300/1062 ,  C10G2300/301 ,  C10G2300/4018 ,  C10G2300/4093 ,  C10G2400/10 ,  C10M171/02 ,  C10M2203/1006 ,  C10M2205/173 ,  C10N2220/022 ,  C10N2220/13 ,  C10N2230/02 ,  C10N2230/54 ,  C10N2230/74 ,  C10N2240/10 ,  C10N2260/02

Abstract: A method to produce high quality lube oil products involving hydrotreating a waxy feed to produce a hydrotreated feed and subsequently hydrodewaxing the hydrotreated feed and hydrofinishing the hydrodewaxed feed.

公开(公告)号：EP3337776A1

公开(公告)日：2018-06-27

申请号：EP16753387.6

申请日：2016-08-18

Applicant: SABIC Global Technologies B.V.

Inventor： KHANMAMEDOVA, Alla ,  SCOTT, Stevenson ,  FICKEL, Dustin

IPC: C07C15/04 ,  C07C5/41 ,  C10G47/18 ,  C07C5/13 ,  B01J29/44 ,  C10G35/095 ,  C10G35/085 ,  C07C4/06 ,  C07C4/14 ,  C10G45/70 ,  C10G45/62 ,  C10G45/64 ,  B01J23/56 ,  C07C4/08 ,  C07C4/18

CPC classification number: C07C15/04 ,  B01J23/56 ,  B01J29/44 ,  B01J35/023 ,  B01J2229/186 ,  B01J2229/20 ,  B01J2229/42 ,  C07C4/06 ,  C07C4/08 ,  C07C4/14 ,  C07C4/18 ,  C07C5/13 ,  C07C5/41 ,  C07C15/06 ,  C07C15/08 ,  C10G35/085 ,  C10G35/095 ,  C10G45/62 ,  C10G45/64 ,  C10G45/70 ,  C10G47/18 ,  C10G2300/1044 ,  C10G2400/30 ,  Y02P20/52

Abstract: The invention relates to a process for producing benzene comprising the steps of: (a) providing a hydrocracking feed stream comprising C5-C12 hydrocarbons, (b) contacting the hydrocracking feed stream in the presence of hydrogen with a hydrocracking catalyst under process conditions including a temperature of 425-580° C., a pressure of 300-5000 kPa gauge and a Weight Hourly Space Velocity of 3-30 h−1 to produce a hydrocracking product stream comprising BTX and (c) separating the BTX from the hydrocracking product stream, wherein the hydrocracking catalyst comprises a shaped body comprising a zeolite and a binder and a hydrogenation metal deposited on the shaped body, wherein the amount of the hydrogenation metal is 0.010-0.30 wt-% with respect to the total catalyst and wherein the zeolite is ZSM-5 having a silica (SiO2) to alumina (Al2O3) molar ratio of 25-75.

公开(公告)号：EP2588570A4

公开(公告)日：2017-11-08

申请号：EP11801370

申请日：2011-06-30

Applicant: EXXONMOBIL RES & ENG CO

Inventor： DOUGHERTY RICHARD CHARLES ,  DAAGE MICHEL A

IPC: C10G31/00

CPC classification number: C10G65/043 ,  C10G45/44 ,  C10G45/48 ,  C10G45/50 ,  C10G45/54 ,  C10G45/58 ,  C10G45/62 ,  C10G45/64 ,  C10G65/08 ,  C10G65/12 ,  C10G2300/1062 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/4081 ,  C10G2400/10 ,  C10M101/02 ,  C10M2203/1025 ,  C10M2203/1045

公开(公告)号：EP3149134A1

公开(公告)日：2017-04-05

申请号：EP15726734.5

申请日：2015-05-27

Applicant: ENI S.p.A.

Inventor： CALEMMA, Vincenzo ,  DE ANGELIS, Alberto Renato ,  ASSANELLI, Giulio

IPC: C11B7/00 ,  C11C1/00 ,  C10G45/02 ,  C10G45/06 ,  C10G45/12 ,  C10G45/58 ,  C10G45/62 ,  C10G45/64 ,  C10G3/00 ,  C11B3/06 ,  C11B13/00

CPC classification number: C10G45/02 ,  C10G3/42 ,  C10G3/50 ,  C10G45/06 ,  C10G45/12 ,  C10G45/58 ,  C10G45/62 ,  C10G45/64 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2400/04 ,  C11C1/04 ,  C11C3/00 ,  Y02E50/13 ,  Y02P30/20

Abstract: The present invention relates to a process for preparing a diesel hydrocarbon fraction, comprising the following steps: (a) reacting at least a renewable feedstock comprising glycerides with water at a temperature within the range of 150–400°C and a pressure within the range of 1-20 MPa, forming at least one mixture of fatty acids and glycerine; (b) separating said glycerine from said mixture of fatty acids; (c) subjecting said mixture of fatty acids to catalytic hydrotreatment in the presence of hydrogen, obtaining a reaction product comprising: (i) at least one gaseous effluent comprising hydrogen, water vapour and CO
2 and possibly CO, (ii) at least one diesel hydrocarbon fraction comprising branched paraffins in a prevalent quantity with respect to the linear paraffins, said catalytic hydrotreatment being carried out in the presence of a catalytic composition comprising at least one metal of group VIIIB dispersed on at least one acid carrier for catalyzing a hydroisomerization reaction of linear paraffins to branched paraffins; (d) separating said diesel hydrocarbon fraction from said reaction product.

Abstract translation: 本发明涉及一种制备柴油烃馏分，所述方法包括以下步骤：（a）至少反应的可再生原料在150-400℃的范围内以及该范围内的压力内的温度包括与水甘油酯 1-20兆帕，形成的脂肪酸和甘油的至少一种混合物; （B）分离的脂肪酸所述混合物所述甘油; （C）的脂肪酸的所述混合物经受在氢的存在下催化加氢处理，得到反应产物包括：（i）至少一种气态流出物包含氢气，水蒸汽和CO 2和可能的CO，（ii）至少一个柴油 烃馏分包含支链烷烃的量普遍存在相对于所述直链烷烃所述催化加氢处理正在执行中的催化组合物，其包括第VIIIB族的至少一种金属的存在下分散在至少一种酸载体用于催化的加氢异构化反应 直链烷烃与支链石蜡; （D）从所述反应产物中分离所述的柴油的烃馏分。

公开(公告)号：EP3078420A1

公开(公告)日：2016-10-12

申请号：EP14867044.1

申请日：2014-12-03

Applicant: Heesung Catalysts Corporation

Inventor： HAN, Hyun-sik ,  YOO, Young-san ,  KIM, Ho-Dong

IPC: B01J37/08 ,  B01J23/42 ,  B01J23/14

CPC classification number: B01J23/626 ,  B01J21/04 ,  B01J23/14 ,  B01J23/42 ,  B01J35/04 ,  B01J35/1014 ,  B01J35/1038 ,  B01J35/1042 ,  B01J35/1061 ,  B01J35/1066 ,  B01J35/109 ,  B01J37/0207 ,  B01J37/0236 ,  B01J37/08 ,  B01J37/16 ,  C07C5/3337 ,  C07C2521/04 ,  C07C2523/62 ,  C10G45/62

Abstract: Disclosed are a catalyst for dehydrogenating a paraffinic hydrocarbon and a method of preparing the same, wherein the catalyst is configured such that a sponge-type alumina support having 3D meso/macro pores is directly impregnated with an active metal, thus decreasing the diffusion resistance of a material, realizing structural stability, and maximizing the distribution of the active metal in the support, thereby significantly increasing olefin conversion and selectivity. In this catalyst, the sponge-type alumina support is directly impregnated with the active metal to thus form an active metal layer inside the support having 3D meso/macro pores that are interconnected to each other.

Abstract translation: 公开了用于脱氢链烷烃及其制备，worin催化剂的方法将催化剂配置的搜索那样具有三维内消旋/大孔海绵型氧化铝载体与活性金属直接浸渍，因此降低的扩散阻力 的材料，实现结构稳定性，和在支撑最大化活性金属的分布，从而显着增加的烯烃转化率和选择性。 在这方面，海绵催化剂型氧化铝载体浸渍有活性金属直接从而形成具有三维的内消旋/大孔载体内的活性金属层的并相互连接以海誓山盟。

公开(公告)号：EP2819780A1

公开(公告)日：2015-01-07

申请号：EP13701665.5

申请日：2013-01-31

Applicant: Shell Internationale Research Maatschappij B.V.

Inventor： GEERINCK, Peter ,  JONGKIND, Hermanus ,  PELGRIM, Bart ,  RIGUTTO, Marcello Stefano

IPC: B01J29/70 ,  B01J29/74 ,  C07C5/27 ,  C10G45/64

CPC classification number: B01J29/7461 ,  B01J21/063 ,  B01J29/703 ,  B01J29/74 ,  B01J2229/16 ,  B01J2229/186 ,  B01J2229/32 ,  B01J2229/37 ,  B01J2229/42 ,  C10G45/62 ,  C10G45/64 ,  C10G73/02

Abstract: Catalyst composition useful in the catalytic dewaxing of a waxy hydrocarbon feedstock which catalyst composition includes a mixture of zeolite EU-2 and titania and may further include a noble metal. The zeolite EU-2 has a molar bulk ratio of silica-to-alumina (SAR) of greater than 100:1. The zeolite or mixture may have been dealuminated such as by acid leaching using a fluorosilicate salt or by steam treating.

公开(公告)号：EP2692429A4

公开(公告)日：2014-09-10

申请号：EP12764926

申请日：2012-03-26

Applicant: JAPAN OIL GAS & METALS JOGMEC ,  INPEX CORP ,  JX NIPPON OIL & ENERGY CORP ,  JAPAN PETROLEUM EXPLORATION CO ,  COSMO OIL CO LTD ,  NIPPON STEEL & SUMIKIN ENG CO

Inventor： TANAKA YUICHI ,  NIITSUMA TAKUYA ,  TASAKA KAZUHIKO ,  IWAMA MARIE

IPC: B01J23/42 ,  B01J21/06 ,  B01J21/12 ,  B01J21/18 ,  B01J23/96 ,  B01J37/00 ,  B01J37/02 ,  B01J37/08 ,  B01J38/02 ,  C10G45/10

CPC classification number: B01J23/42 ,  B01J21/066 ,  B01J21/12 ,  B01J21/18 ,  B01J37/0018 ,  B01J37/0201 ,  B01J37/084 ,  B01J37/088 ,  C10G11/18 ,  C10G45/60 ,  C10G45/62 ,  C10G45/64 ,  C10G45/70 ,  C10G2300/1048 ,  C10G2300/301 ,  C10G2400/30

Abstract: The hydrotreating catalyst of the present invention is a hydrotreating catalyst including a catalyst support including an amorphous composite metal oxide having solid acidity, and at least one active metal supported by the catalyst support and selected from noble metals of Group 8 to Group 10 in the periodic table, wherein the hydrotreating catalyst contains a carbonaceous substance including a carbon atom, and the content of the carbonaceous substance in the hydrotreating catalyst is 0.05 to 1% by mass in terms of the carbon atom.

公开(公告)号：EP2726573A1

公开(公告)日：2014-05-07

申请号：EP12805361.8

申请日：2012-03-23

Applicant: Chevron U.S.A. Inc.

Inventor： KIBBY, Charles L. ,  SAXTON, Robert J. ,  JOTHIMURUGESAN, Kandaswamy ,  DAS, Tapan K.

IPC: C10G2/00 ,  C07C2/00 ,  B01J29/04 ,  C07C5/00

CPC classification number: C10G67/02 ,  C10G2/332 ,  C10G2/333 ,  C10G33/00 ,  C10G45/62 ,  C10G45/64 ,  C10G47/12 ,  C10G47/14 ,  C10G47/16 ,  C10G47/18 ,  C10G49/06 ,  C10G49/08 ,  C10G65/043 ,  C10G65/12 ,  C10G2300/1022

Abstract: A method is provided for converting synthesis gas to liquid hydrocarbon mixtures useful as distillate fuel and/or lube base oil. The synthesis gas is contacted with a synthesis gas conversion catalyst comprising a Fischer-Tropsch synthesis component in an upstream catalyst bed thereby producing an intermediate hydrocarbon mixture containing olefins and C
21+ normal paraffins. The intermediate hydrocarbon mixture is subsequently contacted with a hydroisomerization catalyst and an olefin saturation catalyst, thereby resulting in a product containing no greater than about 25 wt% olefins and containing no greater than about 5 wt% C
21+ normal paraffins. The hydroisomerization and olefin saturation catalysts may be in separate beds or mixed in a single bed downstream of the synthesis gas conversion catalyst.