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。

公开(公告)号：US20150252278A1

公开(公告)日：2015-09-10

申请号：US14434985

申请日：2013-10-22

Applicant: THE LUBRIZOL CORPORATION

Inventor： James H. Bush ,  Robert H. Barbour ,  David J. Moreton ,  Hannah Greenfield ,  Paul R. Stevenson ,  David C. Arters

IPC: C10L10/04 ,  C10L1/22 ,  C07D207/408

CPC classification number: C10L10/04 ,  C07C235/10 ,  C07D207/408 ,  C07D303/04 ,  C08G63/912 ,  C10L1/08 ,  C10L1/22 ,  C10L1/221 ,  C10L1/2222 ,  C10L1/2225 ,  C10L1/224 ,  C10L1/232 ,  C10L1/238 ,  C10L1/2383 ,  C10L1/2387 ,  C10L10/02 ,  C10L10/06 ,  C10L10/18 ,  C10L2200/0259 ,  C10L2230/22 ,  C10L2270/026

Abstract: The composition of the present invention related to a quaternary ammonium salt detergent and the use of such quaternary ammonium salt detergents in a fuel composition to reduce diesel injector deposits and remove or clean up existing deposits on the diesel injectors.

公开(公告)号：US09115317B2

公开(公告)日：2015-08-25

申请号：US13399186

申请日：2012-02-17

Applicant: Miia Mujunen ,  Ossi Pastinen ,  Ilkka Lehtomaki ,  Simo Laakso ,  Perttu Koskinen

Inventor： Miia Mujunen ,  Ossi Pastinen ,  Ilkka Lehtomaki ,  Simo Laakso ,  Perttu Koskinen

IPC: B01D11/04 ,  C02F1/26 ,  C02F1/66 ,  C10G1/04 ,  C10G17/00 ,  C10G53/04 ,  C11B1/10 ,  C11B3/04 ,  C10G31/09 ,  C10G53/10 ,  C10L1/02 ,  C10L1/08

CPC classification number: C10G53/04 ,  B01D11/0492 ,  C02F1/26 ,  C02F1/66 ,  C10G1/04 ,  C10G17/00 ,  C10G31/09 ,  C10G53/10 ,  C10G2400/04 ,  C10G2400/10 ,  C10L1/026 ,  C10L1/08 ,  C11B1/10

Abstract: The invention relates to a method for the recovery of oil from an aqueous solution containing oil and solids, as well as to the use of products obtained by this method. The method of the invention comprises at least the following steps of: Adjusting the oil- and solids-containing aqueous solution to a pH which is acidic, separating an oil- and solids-containing fraction from the acidic aqueous solution with an separation agent which is hydrophilic or assumes a hydrophilic character in response to water, recovering the oil- and solids-containing fraction separated by means of said separation agent, extracting oil away from the solids with a water-insoluble extraction agent, and recovering the oil-containing water-insoluble extraction agent.

Abstract translation: 本发明涉及从含有油和固体的水溶液中回收油的方法，以及使用通过该方法得到的产物。 本发明的方法至少包括以下步骤：将含油和固体的水溶液调节至酸性的pH，用含有分离剂的分离剂从酸性水溶液中分离含油和固体的级分 亲水或具有响应于水的亲水特性，回收通过所述分离剂分离的含有油和固体的馏分，用不溶于水的萃取剂将油从固体中提取出来，并回收含油的水 - 不溶性提取剂。

公开(公告)号：US20150218466A1

公开(公告)日：2015-08-06

申请号：US14619593

申请日：2015-02-11

Applicant: Krista M. Prentice ,  Michel Daage ,  Ajit B. Dandekar ,  Christopher G. Oliveri ,  Rohit Vijay ,  Stephen J. McCarthy ,  Wenyih F. Lai ,  Bradley R. Fingland

Inventor： Krista M. Prentice ,  Michel Daage ,  Ajit B. Dandekar ,  Christopher G. Oliveri ,  Rohit Vijay ,  Stephen J. McCarthy ,  Wenyih F. Lai ,  Bradley R. Fingland

IPC: C10G67/02 ,  C10M101/02 ,  C10L1/08

CPC classification number: C10G67/02 ,  B01J29/7461 ,  B01J35/026 ,  B01J2229/36 ,  B01J2229/42 ,  C10G45/64 ,  C10G65/043 ,  C10G65/12 ,  C10G2300/202 ,  C10G2300/302 ,  C10G2300/4018 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/10 ,  C10L1/08 ,  C10L2200/0446 ,  C10L2270/026 ,  C10L2290/543 ,  C10M101/02

Abstract: An integrated process for producing naphtha fuel, diesel fuel and/or lubricant base oils from feedstocks under sour conditions is provided. The ability to process feedstocks under higher sulfur and/or nitrogen conditions allows for reduced cost processing and increases the flexibility in selecting a suitable feedstock. The sour feed can be delivered to a catalytic dewaxing step without any separation of sulfur and nitrogen contaminants. The integrated process includes an initial dewaxing of a feed under sour conditions, optional hydrocracking of the dewaxed feed, and a separation to form a first diesel product and a bottoms fraction. The bottoms fraction is then exposed to additional hydrocracking and dewaxing to form a second diesel product and optionally a lubricant base oil product. Alternatively, a feedstock can be hydrotreated, fractionated, dewaxed, and then hydrocracked to form a diesel fuel and a dewaxed, hydrocracked bottoms fraction that is optionally suitable for use as a lubricant base oil.

Abstract translation: 提供了一种在酸性条件下从原料生产石脑油燃料，柴油和/或润滑油基础油的综合方法。 在更高硫和/或氮条件下处理原料的能力允许降低成本处理并增加选择合适原料的灵活性。 酸性饲料可以输送到催化脱蜡步骤，而不会分离硫和氮污染物。 一体化方法包括在酸性条件下进料的初始脱蜡，脱蜡进料的任选加氢裂化和分离以形成第一柴油产物和塔底馏分。 然后将底部馏分暴露于额外的加氢裂化和脱蜡以形成第二柴油产品和任选的润滑剂基础油产品。 或者，可以将原料加氢处理，分馏，脱蜡，然后进行加氢裂化，以形成任选适合用作润滑剂基础油的柴油燃料和脱蜡加氢裂化塔底馏分。