公开(公告)号：WO2017083085A1

公开(公告)日：2017-05-18

申请号：PCT/US2016/058424

申请日：2016-10-24

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： HO, Suzzy, C. ,  BAKER, Jr., Charles, L. ,  LUO, Shuji ,  OUMAR-MAHAMAT, Halou

IPC: C10M101/02 ,  C10M109/02 ,  C10G50/02 ,  C10M171/02

CPC classification number: C10G7/00 ,  C10G50/02 ,  C10G67/02 ,  C10G69/02 ,  C10G69/12 ,  C10M101/02 ,  C10M109/02 ,  C10M171/02 ,  C10M2203/1025 ,  C10M2205/0285 ,  C10N2220/021 ,  C10N2220/022 ,  C10N2230/02 ,  C10N2230/10 ,  C10N2240/04 ,  C10N2260/02 ,  C10N2270/00

Abstract: Methods are provided for producing Group II base stocks having high viscosity and also having one or more properties indicative of a high quality base stock. The resulting Group II base stocks can have a viscosity at 100°C and/or a viscosity at 40°C that is greater than the corresponding viscosity for a conventional Group II base stock. Additionally, the resulting Group II base stocks can have one or more properties that are indicative of a high quality base stock.

Abstract translation: 提供了用于生产具有高粘度并且还具有指示高质量基础油料的一种或多种性能的II类基础油料的方法。 所得到的II类基础油料在100℃下可具有粘度和/或在40℃下的粘度大于常规II类基础油料的相应粘度。 此外，由此产生的II类基础油料可以具有一个或多个指示高质量基础油料的特性。

公开(公告)号：WO2016081218A1

公开(公告)日：2016-05-26

申请号：PCT/US2015/059816

申请日：2015-11-10

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： XU, Xiaochun ,  WILSON, Keith ,  SOLED, Stuart, Leon ,  MISEO, Sabato ,  LEVIN, Doron ,  BAUMGARTNER, Joseph, Ernest

IPC: C10G45/08 ,  C10G45/50 ,  C10G65/04 ,  C10G65/08

CPC classification number: C10G45/50 ,  B01J23/882 ,  B01J23/883 ,  B01J23/888 ,  B01J23/8885 ,  B01J37/20 ,  C10G35/06 ,  C10G45/08 ,  C10G47/06 ,  C10G65/02 ,  C10G65/04 ,  C10G65/08 ,  C10G65/12 ,  C10G67/04 ,  C10G69/02 ,  C10G69/08 ,  C10G2300/1048 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2400/00 ,  C10M101/02

Abstract: Methods are provided for hydrotreating a feed to generate a product with a reduced or minimized aromatics content and/or an increased distillate product yield. A distillate boiling range feed having an elevated content of sulfur and/or nitrogen can be hydrotreated using at least two hydrotreating stages with intermediate separation to produce a hydrotreated distillate boiling range product with a reduced or minimized aromatics content. Additionally or alternately, a mixed metal catalyst formed from a suitable precursor can be used during the hydrotreating. A mixed metal catalyst formed from a suitable precursor can provide an unexpectedly superior activity for aromatic saturation. A still further unexpected benefit can be achieved by combining a multi-stage hydrotreating process with intermediate separation with hydrotreating in the presence of a mixed metal catalyst formed from a suitable precursor.

Abstract translation: 提供用于加氢处理进料以产生具有降低的或最小化的芳烃含量和/或增加的馏出物产物产率的产物的方法。 具有提高的硫和/或氮含量的馏出物沸程进料可以使用至少两个具有中间分离的加氢处理阶段进行加氢处理，以产生具有降低的或最小化的芳烃含量的加氢处理的馏出物沸点产物。 另外或者替代地，在加氢处理期间可以使用由合适的前体形成的混合金属催化剂。 由合适的前体形成的混合金属催化剂可以提供出乎意料的优异的芳族饱和活性。 在由合适的前体形成的混合金属催化剂的存在下，通过将多级加氢处理方法与中间分离与加氢处理组合可以实现另外的意想不到的益处。

公开(公告)号：WO2015167866A1

公开(公告)日：2015-11-05

申请号：PCT/US2015/026879

申请日：2015-04-21

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： HANKS, Patrick, L. ,  LEWIS, William, Ernest

IPC: C10G31/06 ,  B01J19/00 ,  C10G67/02 ,  C10G69/02 ,  C10G15/08

CPC classification number: C10G15/08 ,  B01J19/008 ,  C10G31/06 ,  C10G67/02 ,  C10G69/02

Abstract: Systems and methods are providing for integrating a cavitation unit to the backend separation system of a hydrotreater to improve conversion.

Abstract translation: 系统和方法提供了将空化单元集成到加氢处理器的后端分离系统以提高转化率。

公开(公告)号：WO2015167864A1

公开(公告)日：2015-11-05

申请号：PCT/US2015/026867

申请日：2015-04-21

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： HANKS, Patrick L. ,  DAAGE, Michel ,  DEGNAN, Thomas F. ,  SMILEY, Randolph J.

IPC: C10G31/06 ,  C10G65/12 ,  C10G67/02 ,  C10G69/02 ,  C10G69/04 ,  C10G69/06

CPC classification number: C10G31/06 ,  C10G65/12 ,  C10G67/02 ,  C10G69/02 ,  C10G69/04 ,  C10G69/06 ,  C10G2300/4012

Abstract: Methods and systems are provided for pretreating a heavy oil feed to a hvdrocracker, such as a slurry hvdrocracker to partially convert the stream and/or to convert catalyst precursors in the stream to catalytically active particles by hydrodynamic cavitation.

Abstract translation: 提供了方法和系统，用于将重油进料预处理到诸如浆料高压分离器的重油进料以通过流体动力学空化部分地转化流和/或将流中的催化剂前体转化成催化活性颗粒。

公开(公告)号：WO2015000841A1

公开(公告)日：2015-01-08

申请号：PCT/EP2014/063849

申请日：2014-06-30

Applicant: SAUDI BASIC INDUSTRIES CORPORATION ,  SABIC GLOBAL TECHNOLOGIES B.V. ,  HOUSMANS, Thomas, Hubertus, Maria ,  OPRINS, Arno, Johannes, Maria

Inventor： HOUSMANS, Thomas, Hubertus, Maria ,  OPRINS, Arno, Johannes, Maria

IPC: C10G65/10 ,  C10G65/18 ,  C10G67/04 ,  C10G69/06 ,  C10G69/14 ,  C10G65/00

CPC classification number: 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

Abstract: 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.

Abstract translation: 本发明涉及一种将炼厂重质残渣升级至石化产品的方法，包括以下步骤：（a）将蒸馏单元中的烃原料分离成塔顶物流和塔底物流（b），将塔底物料送入 （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的所述物流 到汽油加氢裂化器（GHC）单元，（e）将富含多芳族化合物的所述物流加入开环反应区。

公开(公告)号：WO2013019587A2

公开(公告)日：2013-02-07

申请号：PCT/US2012048466

申请日：2012-07-27

Applicant: SAUDI ARABIAN OIL CO ,  KOSEOGLU OMER REFA

Inventor： KOSEOGLU OMER REFA

IPC: C10G69/02 ,  B01D3/06 ,  B01J8/00

CPC classification number: C10G69/02 ,  B01D11/043 ,  B01D11/0457 ,  B01D11/0461 ,  B01D17/0202 ,  B01D17/0217 ,  B01D17/041 ,  B01D17/047 ,  C10G21/12 ,  C10G25/00 ,  C10G65/043 ,  C10G65/12 ,  C10G67/04 ,  C10G67/0418 ,  C10G67/0436 ,  C10G67/06 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/4081 ,  C10G2300/44

Abstract: Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by hydrotreating the feed under mild conditions, and separating the hydrotreated effluent into an aromatic-rich fraction which contains a substantial amount of the aromatic refractory and sterically hindered sulfur-containing compounds, and an aromatic-lean fraction. The aromatic-rich fraction is contacted with isomerization catalyst, and the isomerized aromatic-rich fraction is recycled to the mild hydrotreating process.

Abstract translation: 含有不希望的有机硫化合物的烃原料的深度脱硫通过在温和条件下加氢处理原料达到硫含量低，即15ppmw或更少的硫的烃产物，并将加氢处理的流出物分离成富含芳烃的馏分 其含有大量的芳族耐火和空间位阻的含硫化合物和贫芳族馏分。 使富含芳烃的馏分与异构化催化剂接触，并将异构化的富含芳烃的馏分循环至轻度加氢处理过程。

公开(公告)号：WO2011046872A3

公开(公告)日：2011-06-16

申请号：PCT/US2010052174

申请日：2010-10-11

Applicant: ELEVANCE RENEWABLE SCIENCES ,  COHEN STEVEN A ,  LUETKENS MELVIN L ,  BALAKRISHNAN CHANDER ,  SNYDER ROBERT

Inventor： COHEN STEVEN A ,  LUETKENS MELVIN L ,  BALAKRISHNAN CHANDER ,  SNYDER ROBERT

IPC: C07C6/02

CPC classification number: C10G3/42 ,  C07C2/862 ,  C07C6/04 ,  C07C51/09 ,  C07C67/03 ,  C07C67/54 ,  C07C2531/14 ,  C07C2531/24 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G69/02 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1092 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/30 ,  C10G2300/301 ,  C10G2300/307 ,  C10G2300/308 ,  C10G2300/44 ,  C10G2400/00 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/22 ,  C10L1/026 ,  C10L1/04 ,  C10L1/08 ,  C10L2200/0469 ,  C11B3/00 ,  C11C1/08 ,  C11C3/003 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678 ,  C07C69/533 ,  C07C57/03 ,  C07C57/12 ,  C07C11/02

Abstract: Methods are provided for refining natural oil feedstocks. The methods comprise reacting the feedstock in the presence of a metathesis catalyst under conditions sufficient to form a metathesized product comprising olefins and esters. In certain embodiments, the methods further comprise separating the olefins from the esters in the metathesized product. In certain embodiments, the methods further comprise hydrogenating the olefins under conditions sufficient to form a fuel composition. In certain embodiments, the methods further comprise transestehfying the esters in the presence of an alcohol to form a transesterified product.

Abstract translation: 提供了用于精炼天然油原料的方法。 所述方法包括在复分解催化剂存在下，在足以形成包含烯烃和酯的复分解产物的条件下使原料反应。 在某些实施方案中，所述方法还包括将烯烃与复分解产物中的酯分离。 在某些实施方案中，所述方法还包括在足以形成燃料组合物的条件下氢化所述烯烃。 在某些实施方案中，所述方法还包括在醇的存在下酯化酯化形成酯交换产物。

公开(公告)号：WO2010011339A3

公开(公告)日：2010-10-21

申请号：PCT/US2009004306

申请日：2009-07-24

Applicant: EXXONMOBIL RES & ENG CO ,  GORBATY MARTIN L ,  COOK BRUCE R ,  FERRUGHELLI DAVID T ,  ENGLISH JASON B ,  LOWENTHAL STEVEN S

Inventor： GORBATY MARTIN L ,  COOK BRUCE R ,  FERRUGHELLI DAVID T ,  ENGLISH JASON B ,  LOWENTHAL STEVEN S

IPC: C10G9/00 ,  C10G11/18 ,  C10G51/04

CPC classification number: C10G69/06 ,  C10G11/18 ,  C10G51/04 ,  C10G69/02 ,  C10G69/04 ,  C10G2300/1074 ,  C10G2300/4081 ,  C10G2400/02

Abstract: The present invention relates to a process for the selective conversion of hydrocarbon feed having a Conradson Carbon Residue content of 0 to 6 wt%, based on the hydrocarbon feed (8). The hydrocarbon feed (18) is treated in a two-step process. The first is thermal conversion (12) and the second is catalytic cracking (26) of the products of the thermal conversion (12). The present invention results in a process for increasing the distillate production (16) from a hydrocarbon feedstream for a fluid catalytic cracking unit. The resulting product slate from the present invention can be further varied by changing the conditions in the thermal (12) and catalytic cracking (26) steps as well as by changing the catalyst in the cracking step (26).

Abstract translation: 本发明涉及一种基于烃进料（8）选择性转化具有0至6重量％的康拉德森碳残余物的烃进料的方法。 烃进料（18）以两步法处理。 第一个是热转化（12），第二个是热转化产物（12）的催化裂化（26）。 本发明导致从用于流化催化裂化装置的烃进料流增加馏出物生产（16）的方法。 通过改变热（12）和催化裂化（26）步骤中的条件以及通过改变裂化步骤（26）中的催化剂，可以进一步改变来自本发明的所得产品板岩。

公开(公告)号：WO2010011339A2

公开(公告)日：2010-01-28

申请号：PCT/US2009/004306

申请日：2009-07-24

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY ,  GORBATY, Martin, L. ,  COOK, Bruce, R. ,  FERRUGHELLI, David, T. ,  ENGLISH, Jason, B. ,  LOWENTHAL, Steven, S.

Inventor： GORBATY, Martin, L. ,  COOK, Bruce, R. ,  FERRUGHELLI, David, T. ,  ENGLISH, Jason, B. ,  LOWENTHAL, Steven, S.

IPC: C10G69/04 ,  C10G47/00

CPC classification number: C10G69/06 ,  C10G11/18 ,  C10G51/04 ,  C10G69/02 ,  C10G69/04 ,  C10G2300/1074 ,  C10G2300/4081 ,  C10G2400/02

Abstract: The present invention relates to a process for the selective conversion of hydrocarbon feed having a Conradson Carbon Residue content of 0 to 6 wt%, based on the hydrocarbon feed. The hydrocarbon feed is treated in a two-step process. The first is thermal conversion and the second is catalytic cracking of the products of the thermal conversion. The present invention results in a process for increasing the distillate production from a hydrocarbon feedstream for a fluid catalytic cracking unit. The resulting product slate from the present invention can be further varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step.

Abstract translation: 本发明涉及一种基于烃进料选择性转化具有0至6重量％的康拉德森碳残余物的烃进料的方法。 烃进料以两步法处理。 第一种是热转化，第二种是热转化产物的催化裂化。 本发明导致用于增加用于流化催化裂化装置的烃进料流的馏出物生产的方法。 通过改变热和催化裂化步骤的条件以及通过改变裂化步骤中的催化剂，可进一步改变本发明产生的产品板条。

公开(公告)号：WO2009031756A2

公开(公告)日：2009-03-12

申请号：PCT/KR2008004125

申请日：2008-07-14

Applicant: KOREA RES INST CHEM TECH ,  DAELIM IND CO LTD ,  DOOSAN MECATEC CO LTD ,  KOREA NAT OIL CORP ,  HYUNDAI ENGINEERING CO LTD ,  SK ENERGY CO LTD ,  JUN KI-WON ,  SONG IN KYU ,  CHO KYUNG MIN ,  PARK SUNYOUNG ,  BAECK SUNG-HYEON

Inventor： JUN KI-WON ,  SONG IN KYU ,  CHO KYUNG MIN ,  PARK SUNYOUNG ,  BAECK SUNG-HYEON

IPC: B01J8/04 ,  C07C1/04

CPC classification number: B01J8/0457 ,  B01J8/0492 ,  B01J8/0496 ,  B01J23/75 ,  B01J23/755 ,  B01J29/0333 ,  B01J37/0201 ,  C10G2/32 ,  C10G2/332 ,  C10G47/14 ,  C10G69/02

Abstract: The present invention relates to a process of preparing liquid-phase hydrocarbon mixture, which comprises continuously conducting Fischer-Tropsch synthesis reaction in the upper part and hydrocracking reaction in the lower part by using a continuous-flow dual-bed reactor which comprises two fixed-bed reactors filled with catalysts and continuously placed in upper and lower parts and a hydrogen-supplying pipe between the upper and the lower fixed-bed reactors and continuously supplying hydrogen in the lower fixed-bed reactor, thereby remarkably increasing the yield of C10-C20 liquid-phase hydrocarbon mixture as compared to the conventional Fischer-Tropsch synthesis reaction.

Abstract translation: 本发明涉及一种制备液相烃混合物的方法，其包括在上部连续进行费 - 托合成反应和下部的加氢裂化反应，使用连续流动双床反应器，其包括两个固定 - 填充催化剂并连续放置在上部和下部的床反应器和上下固定床反应器之间的氢气供应管，并在下固定床反应器中连续供应氢气，从而显着提高了C10-C20的收率 液相烃混合物与常规的费 - 托合成反应相比。