公开(公告)号：US20160040083A1

公开(公告)日：2016-02-11

申请号：US14918746

申请日：2015-10-21

Applicant: Richard Charles Dougherty ,  William J. Novak ,  Stuart S. Shih ,  Stephen John McCarthy ,  Michel Daage

Inventor： Richard Charles Dougherty ,  William J. Novak ,  Stuart S. Shih ,  Stephen John McCarthy ,  Michel Daage

IPC: C10L1/08 ,  C10G65/18 ,  C10L10/12 ,  C10G47/00

CPC classification number: C10L1/08 ,  C10G45/64 ,  C10G47/00 ,  C10G65/10 ,  C10G65/12 ,  C10G65/18 ,  C10G69/10 ,  C10G2300/1055 ,  C10G2300/1059 ,  C10G2300/1074 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2300/305 ,  C10G2300/307 ,  C10G2400/02 ,  C10G2400/04 ,  C10L10/12 ,  C10L2200/0446 ,  C10L2270/026

Abstract: This invention relates to a process involving hydrocracking and dewaxing of a feedstream in which a converted fraction can correspond to a majority of the product from the reaction system, while an unconverted fraction can exhibit improved properties. In this hydrocracking process, it can be advantageous for the yield of unconverted fraction for gasoline fuel application to be controlled to maintain desirable cold flow properties for the unconverted fraction. Catalysts and conditions can be chosen to assist in attaining, or to optimize, desirable product yields and/or properties.

Abstract translation: 本发明涉及一种包含进料流的加氢裂化和脱蜡的方法，其中转化的馏分可以对应于来自反应体系的大部分产物，而未转化的馏分可以表现出改进的性能。 在该加氢裂化过程中，可以有利地控制汽油燃料应用的未转化馏分的产率，以保持未转化馏分的期望的冷流动性能。 可以选择催化剂和条件以帮助实现或优化所需的产物产率和/或性能。

公开(公告)号：US20160024401A1

公开(公告)日：2016-01-28

申请号：US14811745

申请日：2015-07-28

Applicant: FLUOR TECHNOLOGIES CORPORATION

Inventor： Ravi Ravikumar ,  Paul E. Koppel ,  Sanjiv Dabee ,  Johnathon Zychowicz

IPC: C10G67/02 ,  C01B3/34 ,  C10L1/04 ,  C10G2/00 ,  C10L10/12 ,  C10L1/08

CPC classification number: C01B3/34 ,  C01B3/38 ,  C01B3/48 ,  C01B2203/0216 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/062 ,  C01B2203/063 ,  C10G2/32 ,  C10G47/00 ,  C10G2300/1022 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10K1/005 ,  C10K3/04 ,  C10L1/04 ,  C10L10/12 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/148 ,  C10L2290/42 ,  C10L2290/541 ,  C10L2290/542 ,  C10L2290/543

Abstract: A crude oil processing plant that comprises a Fischer-Tropsch reactor is disclosed. The crude oil processing plant comprises a crude oil processing section and a hydrogen production section. The hydrogen production section is coupled to a hydrocracker in the crude oil processing section to deliver a high purity hydrogen stream. The Fischer-Tropsch reactor receives a syngas stream from the hydrogen production section and produces a hydrocarbon stream. When light crude oil is processed, the hydrocracker typically has excess capacities to upgrade the hydrocarbon stream from the Fischer-Tropsch reactor.

Abstract translation: 公开了一种包含费 - 托反应器的原油加工设备。 原油加工厂包括原油加工段和氢气生产段。 氢气生产部分与原油加工部分中的加氢裂化器相连，以输送高纯度氢气流。 费 - 托反应器从氢气生产部分接收合成气流并产生烃流。 当加工轻质原油时，加氢裂化器通常具有过量的能力来升级费 - 托反应器的烃流。

公开(公告)号：US20160002567A1

公开(公告)日：2016-01-07

申请号：US14800032

申请日：2015-07-15

Applicant: Novita Nutrition, LLC

Inventor： Keith Bruinsma ,  Donald Endres ,  Steven J. Furcich

IPC: C11B1/10 ,  C10L1/08 ,  C10G3/00 ,  B01D11/02 ,  C11C1/02

CPC classification number: C11B9/0003 ,  A23J1/12 ,  A23K10/38 ,  B01D11/0288 ,  C10G3/50 ,  C10L1/026 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2200/0476 ,  C10L2270/026 ,  C10L2290/26 ,  C10L2290/544 ,  C11B1/10 ,  C11C1/025 ,  C11C3/00 ,  C11C3/10 ,  Y02E50/13 ,  Y02P30/20 ,  Y02P60/873

Abstract: A process for extraction of crude oil from distillers dried grain solubles and/or distillers dried grains and producing corn distillers meal that may be used as a livestock supplement is disclosed. For example, the corn distillers meal may be used as a crude protein supplement for use in a livestock feed diet or a poultry feed diet. The solvent extracted crude oil may be suitable for oleochemical processing for personal care and home care products, biodiesel production, and/or renewable diesel production from hydro-treating the extracted oil to make green diesel fuel.

公开(公告)号：US20150375190A1

公开(公告)日：2015-12-31

申请号：US14844354

申请日：2015-09-03

Applicant: Caisson Technology Group LLC

Inventor： Alexander E. Kravtsov

IPC: B01J19/00 ,  C10L1/06 ,  C10L1/08 ,  F02M61/16 ,  C10L10/02 ,  C09K15/00 ,  C02F1/34 ,  C10L1/04 ,  C10L1/02

CPC classification number: B01J19/008 ,  B01F5/0688 ,  B01J2219/24 ,  C02F1/34 ,  C09K15/00 ,  C10L1/026 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10L10/02 ,  C10L2200/0423 ,  C10L2200/043 ,  C10L2200/0446 ,  C10L2200/0476 ,  C10L2230/22 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2270/04 ,  F02M61/16 ,  Y10T137/0396

Abstract: An apparatus is disclosed. The apparatus includes a bubble implosion reactor cavitation device. The bubble implosion reactor cavitation device includes a tube-shaped cylindrical body including an upstream, a distal end surface and a downstream, proximal end surface. The tube-shaped cylindrical body defines an axial passage that extends through the tube-shaped cylindrical body between the upstream, distal end surface and the downstream, proximal end surface. The apparatus also includes a bubble generator subassembly connected to the tube-shaped cylindrical body. The bubble generator subassembly is at least partially disposed within the axial passage defined by the tube-shaped cylindrical body. The apparatus also includes a retaining member connected to the tube-shaped cylindrical body for retaining the bubble generator subassembly within the axial passage defined by the tube-shaped cylindrical body.

Abstract translation: 公开了一种装置。 该装置包括气泡内爆反应器空化装置。 气泡内爆反应器空化装置包括管状圆柱体，其包括上游侧，远端表面和下游近端表面。 管状圆柱形主体限定了一个轴向通道，该通道在上游侧远端表面和下游近端表面之间延伸穿过管状圆柱体。 该装置还包括连接到管状圆柱体的气泡发生器子组件。 泡沫发生器子组件至少部分地设置在由管状圆柱体限定的轴向通道内。 该装置还包括连接到管状圆柱体的保持构件，用于将气泡发生器子组件保持在由管状圆柱体限定的轴向通道内。

公开(公告)号：US20150361357A1

公开(公告)日：2015-12-17

申请号：US14764485

申请日：2013-08-01

Applicant: PETROCHINA COMPANY LIMITED

Inventor： Shoutao MA ,  Ran TIAN ,  Zhihua ZHANG ,  Gang WANG ,  Famin SUN ,  Ruiqin ZHANG ,  Chunmei YU ,  Shengbo SUN ,  Xiufang FENG ,  Fengxuan LI ,  Jinling ZHU

IPC: C10G65/08 ,  C10L1/08

CPC classification number: C10G65/08 ,  B01J8/0453 ,  B01J8/0492 ,  B01J2208/00849 ,  B01J2208/00938 ,  C10G45/20 ,  C10G65/04 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/10 ,  C10L1/04 ,  C10L1/08 ,  C10L2270/026 ,  C10L2290/545

Abstract: A hydrogenation method and distillate two-phase hydrogenation reactor in which the size of an upper space of the reactor is greater than that of a lower catalyst bed part. The reactor comprises 2 to 4 catalyst beds. An inner component for gas replenishment and for stripping a liquid-phase stream containing impurities is arranged between at least one adjacent catalyst bed and comprises a separator plate and exhaust pipes. The separator plate is provided with multiple downcomer through holes. The separator plate is connected with a plurality of exhaust pipes. The exhaust pipes are vertically arranged above the separator plate. The top parts of the exhaust pipes are in contact with the lower part of the upper catalyst bed.

Abstract translation: 一种氢化方法和蒸馏二相氢化反应器，其中反应器的上部空间的大小大于下部催化剂床部分的尺寸。 反应器包含2至4个催化剂床。 用于补充气体和用于汽提含有杂质的液相物流的内部部件设置在至少一个相邻的催化剂床之间，并且包括隔板和排气管。 隔板设有多个降液管通孔。 分隔板与多个排气管连接。 排气管垂直布置在隔板的上方。 排气管的顶部与上部催化剂床的下部接触。

公开(公告)号：US09212320B2

公开(公告)日：2015-12-15

申请号：US13479004

申请日：2012-05-23

Applicant: Elizabeth M. Woods ,  Ming Qiao ,  Paul Myren ,  Randy D. Cortright ,  John Kania

Inventor： Elizabeth M. Woods ,  Ming Qiao ,  Paul Myren ,  Randy D. Cortright ,  John Kania

IPC: C07C1/00 ,  C10G3/00 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08

CPC classification number: C10G1/065 ,  C07C1/24 ,  C10G3/42 ,  C10G3/44 ,  C10G3/48 ,  C10G3/49 ,  C10G3/52 ,  C10G3/62 ,  C10G2300/1014 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/305 ,  C10G2300/308 ,  C10G2300/44 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/30 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  Y02E50/13 ,  Y02P30/20

Abstract: Described are methods, reactor systems, and catalysts for converting biomass to fuels and chemicals in a batch and/or continuous process. The process generally involves the conversion of water insoluble components of biomass, such as hemicellulose, cellulose and lignin, to volatile C2+O1-2 oxygenates, such as alcohols, ketones, cyclic ethers, esters, carboxylic acids, aldehydes, and mixtures thereof. In certain applications, the volatile C2+O1-2 oxygenates can be collected and used as a final chemical product, or used in downstream processes to produce liquid fuels, chemicals and other products.

Abstract translation: 描述了在批量和/或连续过程中将生物质转化为燃料和化学品的方法，反应器系统和催化剂。 该方法通常涉及将生物质的水不溶性组分如半纤维素，纤维素和木质素转化成挥发性的C2 + O1-2含氧化合物，例如醇，酮，环醚，酯，羧酸，醛及其混合物。 在某些应用中，挥发性C2 + O1-2含氧化合物可以被收集并用作最终的化学产品，或用于下游工艺生产液体燃料，化学品和其他产品。

公开(公告)号：US20150337220A1

公开(公告)日：2015-11-26

申请号：US14573230

申请日：2014-12-17

Applicant: AUTERRA, INC. ,  CENOVUS ENERGY INC.

Inventor： Kyle E. Litz ,  Jonathan P. Rankin

IPC: C10G27/12 ,  C10M101/02 ,  C10L1/08

CPC classification number: C10G27/12 ,  C10G19/00 ,  C10G27/00 ,  C10G2300/202 ,  C10L1/04 ,  C10L1/08 ,  C10L2200/0446 ,  C10L2270/026 ,  C10M101/02 ,  C10M2203/003 ,  C10N2220/022 ,  C10N2220/031 ,  C10N2230/40 ,  C10N2230/43 ,  C10N2230/52 ,  C10N2230/70 ,  Y02E50/13

Abstract: A hydrocarbon product having at least 0.1 grams per gram of hydrocarbon product having a boiling range distribution from an initial boiling point to approximately 739° C. wherein the hydrocarbon products are further characterized by an infrared spectroscopy reference peak, centered between approximately 1445 cm−1 and 1465 cm−1, a first infrared spectroscopy peak between approximately 1310 cm−1 and 1285 cm−1, wherein the height of the first infrared spectroscopy peak is at least approximately 28% of the height of the infrared spectroscopy reference peak and a second infrared spectroscopy peak between approximately 1135 cm−1 and 1110 cm−1, wherein the height of the second infrared spectroscopy peak is at least approximately 22% of the height of the infrared spectroscopy reference peak.

公开(公告)号：US20150307810A1

公开(公告)日：2015-10-29

申请号：US14653470

申请日：2012-12-21

Applicant: SUNPINE AB

Inventor： Lars Stigsson ,  Valeri Naydenov ,  Johan Lundback

IPC: C11B3/00 ,  C10L1/08 ,  C11B3/12 ,  C10G3/00

CPC classification number: C11B3/006 ,  B01D3/10 ,  B01D3/143 ,  B01D3/28 ,  C07C4/04 ,  C07C51/44 ,  C07C2603/26 ,  C09F1/02 ,  C10G3/00 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2400/04 ,  C10L1/026 ,  C10L1/08 ,  C10L1/1616 ,  C10L1/1888 ,  C10L10/12 ,  C10L2200/0469 ,  C10L2200/0484 ,  C10L2270/026 ,  C10L2290/543 ,  C10L2290/544 ,  C10L2290/545 ,  C11B3/008 ,  C11B3/12 ,  C11B11/00 ,  C11B13/005 ,  Y02E50/13 ,  Y02P30/20 ,  Y02W30/74

Abstract: A process for pre-treatment of a crude tall oil (CTO) for removal of impurities is disclosed. The process comprises a first pre-treatment step involving a CTO wash and a separation of a first oil phase comprising refined CTO and an aqueous phase holding impurities, and a second step involving a separation of a second oil phase from the aqueous phase. A process for refining of crude tall oil (CTO) is also disclosed. The process comprises fractionation under vacuum of a refined CTO into at least one stream of refined tall diesel (RTD) or tall oil fatty acids (TOFA) and at least one stream of resin acid(s) (RA). The stream of RTD or TOFA is deoxygenated forming hydrocarbon compounds in a subsequent step. This invention also relates to a refined tall diesel. Furthermore, a process for the production of a refined tall diesel (RTD) composition, wherein crude sulphate turpentine(s) (CST) is added to the refined tall diesel (RTD) composition, is described.

Abstract translation: 公开了用于去除杂质的粗妥尔油（CTO）的预处理方法。 该方法包括涉及CTO洗涤和分离包含精制CTO和含有杂质的水相的第一油相的第一预处理步骤，以及涉及将第二油相与水相分离的第二步骤。 还公开了粗妥质油（CTO）的精制方法。 该方法包括在精制CTO的真空下将精制高级柴油（RTD）或妥尔油脂肪酸（TOFA）和至少一种树脂酸（RA）流的至少一个流分馏。 RTD或TOFA的流在随后的步骤中脱氧形成烃化合物。 本发明还涉及精制高级柴油。 此外，描述了生产精制高柴油（RTD）组合物的方法，其中将粗硫酸盐松节油（CST）加入到精制高柴油（RTD）组合物中。

公开(公告)号：US09169450B2

公开(公告)日：2015-10-27

申请号：US11864540

申请日：2008-02-12

Applicant: Cong-Yan Chen

Inventor： Cong-Yan Chen

IPC: C10G65/08 ,  C10G65/12 ,  C10G65/04 ,  C10L1/08 ,  B01J23/44 ,  B01J23/883 ,  B01J29/74

CPC classification number: C10G65/08 ,  B01J23/44 ,  B01J23/883 ,  B01J29/74 ,  C10G65/043 ,  C10G65/12 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/08

Abstract: The present invention is directed to a process for converting heavy hydrocarbonaceous feeds to jet and diesel products: using a single reactor, dual catalyst system; or using a single reactor, multiple catalyst system.

Abstract translation: 本发明涉及将重质烃进料转化为喷气和柴油产物的方法：使用单一反应器，双重催化剂体系; 或使用单个反应器，多个催化剂体系。

公开(公告)号：US09145528B2

公开(公告)日：2015-09-29

申请号：US13265508

申请日：2010-04-21

Applicant: Brian L. Goodall ,  Alex M. Aravanis ,  Craig A. Behnke ,  Richard J. Cranford ,  Daniel J. Sajkowski

Inventor： Brian L. Goodall ,  Alex M. Aravanis ,  Craig A. Behnke ,  Richard J. Cranford ,  Daniel J. Sajkowski

IPC: C10L1/04 ,  C10G45/08 ,  C10G65/04 ,  C10G65/12 ,  C10G67/04 ,  C10G69/04 ,  C10G69/06 ,  C10G69/08 ,  C10L1/06 ,  C10L1/08 ,  C10G3/00 ,  C12P7/64 ,  C11B3/02 ,  C11C3/12 ,  C11C3/14

CPC classification number: C10L1/04 ,  C10G3/46 ,  C10G3/47 ,  C10G3/49 ,  C10G3/50 ,  C10G45/08 ,  C10G65/043 ,  C10G65/046 ,  C10G65/12 ,  C10G67/04 ,  C10G69/04 ,  C10G69/06 ,  C10G69/08 ,  C10G2300/1014 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/30 ,  C10G2300/4018 ,  C10G2300/44 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/10 ,  C10L1/06 ,  C10L1/08 ,  C11B3/02 ,  C11C3/12 ,  C11C3/14 ,  C12P7/6463 ,  Y02P30/20

Abstract: Disclosed herein are methods and systems for upgrading (for example, removing heteroatoms, metals, or metalloids) an oil composition derived or extracted from a biomass. The upgraded oil composition can be used to make a desired product, for example, a fuel product.

Abstract translation: 本文公开了用于升级（例如，去除杂原子，金属或准金属）从生物质衍生或提取的油组合物的方法和系统。 改进的油组合物可用于制备所需产物，例如燃料产品。