公开(公告)号：WO2015095561A2

公开(公告)日：2015-06-25

申请号：PCT/US2014/071223

申请日：2014-12-18

Applicant: BATTELLE MEMORIAL INSTITUTE

Inventor： STROMH, James, J. ,  ROBERTS, Benjamin, Q. ,  DENSLOW, Kayte, M.

IPC: B01J19/10 ,  C10G47/32

CPC classification number: C10G45/02 ,  B01J19/10 ,  C10G15/08 ,  C10G31/00 ,  C10G45/22 ,  C10G47/02 ,  C10G47/32 ,  C10G2300/202

Abstract: Hydroprocessing can be performed at low pressure using acoustic energy. For example, hydroprocessing a feedstock having one or more hydrocarbon compounds carried in, or mixed with, a transport gas involves flowing the feedstock through a reaction zone in a reactor that has a bulk pressure less than 68 atm and applying acoustic energy through the reaction zone. The hydrocarbon compounds are chemically reacted with a hydrogen source in the presence of a catalyst, wherein the reacting occurs in the reaction zone.

Abstract translation: 可以使用声能在低压下进行加氢处理。 例如，加载具有携带在输送气体中或与输送气体混合的一种或多种烃化合物的原料包括使原料流过具有小于68atm的整体压力的反应器中的反应区，并且通过反应区施加声能 。 烃化合物在催化剂存在下与氢源化学反应，其中反应在反应区中进行。

公开(公告)号：WO2015076924A1

公开(公告)日：2015-05-28

申请号：PCT/US2014/056866

申请日：2014-09-23

Applicant: UOP LLC

Inventor： THAKKAR, Vasant P. ,  BARGER, Paul T. ,  BRICKER, Maureen L. ,  CHEN, John Q. ,  COUGHLIN, Peter K. ,  FREY, Stanley J. ,  JOHNSON, James A. ,  KOCAL, Joseph A. ,  LIPPMANN, Matthew

IPC: C10G55/06 ,  C10G55/00

CPC classification number: C10G1/002 ,  C10G1/02 ,  C10G31/00 ,  C10G45/02 ,  C10G45/08 ,  C10G45/12 ,  C10G47/00 ,  C10G47/04 ,  C10G65/04 ,  C10G65/12

Abstract: A multifunction hydrotreater includes a particulate removal zone having a particulate trap to remove particulate contaminants from a coal tar stream and a demetallizing zone including a demetallizing catalyst to remove organically bound metals from the de-particulated stream. The demetallizing zone is positioned after the particulate removal zone. The hydrotreater also includes a hydrodesulfurization, hydrodenitrogenation, and hydrodeoxygenation zone positioned after the demetallization zone, which includes at least one hydrodesulfurization, hydrodenitrogenation, and hydrodeoxygenation catalyst to provide a hydrotreated coal tar stream.

Abstract translation: 多功能加氢处理器包括具有颗粒捕集器的颗粒去除区，以从煤焦油流中除去微粒污染物，以及包括去金属催化剂的去金属区，以从脱颗粒流中除去有机结合的金属。 脱金属区位于颗粒去除区之后。 加氢处理器还包括位于脱金属区之后的加氢脱硫，加氢脱氮和加氢脱氧区，其包括至少一种加氢脱硫，加氢脱氮和加氢脱氧催化剂以提供加氢处理的煤焦油流。

公开(公告)号：WO2014008457A2

公开(公告)日：2014-01-09

申请号：PCT/US2013049422

申请日：2013-07-05

Applicant: GENIE IP BV ,  VINEGAR HAROLD ,  NGUYEN SCOTT

Inventor： VINEGAR HAROLD ,  NGUYEN SCOTT

CPC classification number: E21B43/24 ,  C10G7/00 ,  C10G17/00 ,  C10G19/00 ,  C10G21/00 ,  C10G25/00 ,  C10G27/00 ,  C10G29/00 ,  C10G31/00 ,  C10G45/00 ,  C10G45/02 ,  C10L3/12 ,  E21B7/046 ,  E21B43/00 ,  E21B43/25 ,  E21B43/26 ,  E21B49/00

Abstract: An oil production well is drilled into a kerogenous chalk source rock comprising (i) type IIs kerogen and (ii) shallow naturally-occurring unconventional oil derived from the type IIs kerogen that is resident within pore space of the source rock. In some embodiments, the production well is drilled at a location where the geothermal gradient is at least 3 degrees C per 100 m is present at or near the production well. It is believed that the presence of this geothermal gradient accelerated maturation of the type IIs kerogen of the source rock to convert a portion of the type IIs kerogen into the unconventional oil. In some embodiments, the shallow production well is non-vertical. In some embodiments, at depths that are shallow and within the source rock, the production well is cased and perforated. Oil from the source rock may be produced via the production well and the shallow-depth perforated locations thereof.

Abstract translation: 一个石油生产井被钻入一个角质层的白垩源岩，包括（i）II型干酪根和（ii）源自源岩孔隙空间的II型干酪根的浅天然存在的非常规油。 在一些实施方案中，在生产井处或附近存在地热梯度为至少3℃至100℃的位置钻出生产井。 据信，这种地热梯度的存在加速了源岩II型干酪根的成熟，以将部分II型干酪根转化成非常规油。 在一些实施例中，浅生产井是非垂直的。 在一些实施例中，在浅的并且在源岩内的深度处，生产井是套管和穿孔的。 来自源岩的油可以通过生产井和浅深的穿孔位置来生产。

公开(公告)号：WO2010101293A1

公开(公告)日：2010-09-10

申请号：PCT/JP2010/053929

申请日：2010-03-03

Applicant: 日産自動車株式会社 ,  株式会社本家松浦酒造場 ,  久保賢明 ,  今岡佳宏 ,  松浦一雄

Inventor： 久保賢明 ,  今岡佳宏 ,  松浦一雄

IPC: F02M27/08 ,  C10L1/02 ,  C10L1/06 ,  F02D19/06 ,  F02M31/20

CPC classification number: F02M1/165 ,  C10G7/00 ,  C10G31/00 ,  F02B19/1023 ,  F02B19/12 ,  F02D19/0634 ,  F02D19/0671 ,  F02D19/0692 ,  F02D19/084 ,  F02M25/12 ,  F02M27/08 ,  F02M31/18 ,  F02M31/20 ,  Y02T10/121 ,  Y02T10/126 ,  Y02T10/36

Abstract: 分子量と沸点が互いにほぼ比例関係にある異なる燃料種の集合物である炭化水素燃料に対して、前記異なる燃料種のうち相対的に大きな分子量を持つ燃料種に比べ小さな分子量を持つとともに分子量が略同等の燃料種に比べて沸点が相対的に高い液状の高沸点物質が混入した混合燃料に振動エネルギーを与え、高沸点物質と、高沸点物質の分子量以下の燃料種である軽質燃料とを霧化する霧化装置と、霧化した軽質燃料と高沸点物質との混じったガスから高沸点物質のみを分離する高沸点物質分離装置とを備える。これにより、燃料を気化させるための大きな気化熱を与えることなく、沸点の低い燃料種やアルコールをアルコール混入ガソリンから分離することができる。

Abstract translation: 一种燃料分离器，其装备有：雾化器，其向包含烃燃料和液体高沸点物质的混合物的混合燃料施加振动能量，所述烃燃料是不同燃料成分的混合物，其中分子量大约与沸腾成比例 并且具有比燃料成分分子量低的具有比具有大致相同分子量的燃料成分具有较高分子量且沸点更高的不同燃料成分的高沸点物质，从而将 高沸点物质和由分子量等于或低于高沸点物质的燃料成分组成的轻燃料; 以及高沸点物质分离器，其将高沸点物质与作为雾化轻燃料和高沸点物质的混合物的气体隔离。 通过使用该分离器，可以从酒精汽油中分离出低沸点燃料成分和醇，而不会大大加热燃料以使燃料蒸发。

公开(公告)号：WO2009009887A1

公开(公告)日：2009-01-22

申请号：PCT/CA2008/001295

申请日：2008-07-16

Applicant: RJ OIL SANDS INC. ,  BOZAK, Wade, R. ,  KESSICK, Michael, E. ,  FACEY, Roderick, M.

Inventor： BOZAK, Wade, R. ,  KESSICK, Michael, E. ,  FACEY, Roderick, M.

IPC: B01D21/01 ,  B01D17/035 ,  B01D17/05 ,  B01D21/02 ,  B01F5/02 ,  C10C3/00 ,  C10G1/04

CPC classification number: B03D1/02 ,  B01D17/0205 ,  B01F5/0413 ,  B01F5/043 ,  B09C1/02 ,  C10G1/045 ,  C10G31/00 ,  C10G2300/1003

Abstract: A method of treating tailings comprising a solids fraction and a hydrocarbon fraction is disclosed. A primary flow is supplied to a jet pump, the primary flow comprising water and less than 20% solids by mass. A secondary flow is supplied to a mixing chamber of the jet pump, the secondary flow comprising a slurry of water and tailings, the slurry comprising more solids by mass than the primary flow. The jet pump is operated using the primary flow such that the tailings are agitated to effect at least a partial phase separation of the hydrocarbon fraction from the tailings. The methods disclosed herein may also be applied to treat tailings ponds.

Abstract translation: 公开了一种处理包含固体部分和烃馏分的尾矿的方法。 一次流被提供给喷射泵，主流包含水和小于20质量％固体。 二次流被供应到喷射泵的混合室，二次流包括水和尾矿的浆料，该浆料比主流体包含更多的质量固体。 喷射泵使用初级流动操作，使得尾矿被搅动以使烃馏分与尾矿至少部分相分离。 本文公开的方法也可以应用于处理尾矿池塘。

公开(公告)号：WO2009000062A1

公开(公告)日：2008-12-31

申请号：PCT/CA2008000042

申请日：2008-01-11

Applicant: FRACTAL SYSTEMS INC ,  CHORNET MICHEL ,  CHORNET ESTEBAN

Inventor： CHORNET MICHEL ,  CHORNET ESTEBAN

IPC: C10G99/00

CPC classification number: C10G99/00 ,  B01J19/008 ,  C10G31/00 ,  C10G31/06 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/308

Abstract: A hydrodynamic cavitation treated oil which has a viscosity which is lower than the viscosity of the oil prior to treatment The treated oil and the oil prior to the treatment having distillation curves or boiling point curves which are the same as or approximate to each other.

Abstract translation: 具有比处理前的油的粘度低的粘度的流体动力学空化处理油处理后的油和处理前的油具有彼此相同或相近的蒸馏曲线或沸点曲线。

公开(公告)号：WO2008155730A2

公开(公告)日：2008-12-24

申请号：PCT/IB2008/052398

申请日：2008-06-18

Applicant: THE PETROLEUM OIL AND GAS CORPORATION OF SOUTH AFRICA (PTY) LTD ,  MDLELENI, Masikana Millan ,  KNOTTENBELT, Cyril David ,  MARIPANE, Kgolole David ,  HLOHLOZA, Nkululeko Stewart

Inventor： MDLELENI, Masikana Millan ,  KNOTTENBELT, Cyril David ,  MARIPANE, Kgolole David ,  HLOHLOZA, Nkululeko Stewart

IPC: C10G2/00 ,  C10G17/04

CPC classification number: C10G31/08 ,  B01D21/26 ,  C10G2/30 ,  C10G17/04 ,  C10G31/00

Abstract: This invention relates to processes for removing particles such as catalyst fines from hydrocarbon streams, such as a wax dried from a Fischer Tropsch reaction using centrifugation in combination with a treatment with an aqueous solution preferably containing an acid, or with an acid. According to an aspect of the invention, catalyst particles are removed from a wax derived from a Fischer Tropsch by pre-treating the hydrocarbon stream with an aqueous solution and forming a mixture comprising the hydrocarbon stream and 5-25% v/v organic acid solution; and introducing the mixture to a centrifuge and separating, from the mixture, a hydrocarbon stream, an aqueous solution and particles. The process may be a continuous and/or a batch process.

Abstract translation: 本发明涉及从烃流中除去诸如催化剂细粉之类的颗粒的方法，例如使用离心与由优选含酸的水溶液或酸处理组合的费 - 托反应干燥的蜡。 根据本发明的一个方面，通过用水溶液预处理烃流并形成包含烃流和5-25％v / v有机酸溶液的混合物，从衍生于费托的蜡中除去催化剂颗粒 ; 并将混合物引入离心机中并从混合物中分离出烃流，水溶液和颗粒。 该方法可以是连续和/或分批过程。

公开(公告)号：WO2007103596A3

公开(公告)日：2007-12-21

申请号：PCT/US2007060973

申请日：2007-01-30

Applicant: CONOCOPHILLIPS CO ,  MOCK JON M

Inventor： MOCK JON M

IPC: C10G45/00

CPC classification number: C10G31/00

Abstract: High rate gas stripping for removal of sulfur-containing components such as mercaptans from crude oil may be conducted by feeding sweet gas to the bottom of a tower containing pre-heated mercaptan-containing crude oil feed. The gas bubbles up through the crude becoming enriched with H2S, mercaptans, CO2 and/or hydrocarbons. The rich gas exits the tower, and is treated to produce a sweetened gas, a portion of which is recycled to the tower, and an acid gas. The remainder of the sweetened and/or the acid gas may be used as a fuel or processed to recover a portion of any hydrocarbons that may have been stripped out of the crude oil with the mercaptans, sulfur-containing components, CO2, used for enhanced oil recovery or disposed.

Abstract translation: 用于从原油中除去含硫组分如硫醇的高速汽提可以通过将甜气馈送到含预热的含硫醇原油进料的塔的底部来进行。 气体通过粗气体向上膨胀，富含H 2 S，硫醇，CO 2和/或烃。 富氧气体离开塔，并被处理以产生增甜气体，其一部分再循环到塔中，并产生酸气。 甜味气体和/或酸性气体的其余部分可以用作燃料或加工以回收可能用硫醇，含硫组分，用于增强的含硫组分，二氧化碳，可能已被从原油中汽提的任何烃的一部分 油回收或处置。

公开(公告)号：WO2007072005A1

公开(公告)日：2007-06-28

申请号：PCT/GB2006/004834

申请日：2006-12-21

Applicant: INNOSPEC LIMITED ,  SNEDDON, Andrea ,  ÖSTLUND, Jenny-Ann

Inventor： SNEDDON, Andrea ,  ÖSTLUND, Jenny-Ann

IPC: C10G75/04 ,  C08L61/06 ,  C10G31/00

CPC classification number: C10G31/00 ,  C08L61/06 ,  C10G75/04 ,  C10G2300/1033 ,  C10G2300/107 ,  C10G2300/802

Abstract: The present invention provides a process for the treatment of crude oil or aged crude oil residue comprising the steps of (a) contacting the oil or residue with a phenol resin and with a diluent, to provide a diluted phenol resin treated oil or residue; and (b) optionally removing solid material from the diluted phenol resin treated oil or residue.

Abstract translation: 本发明提供一种处理原油或老化原油渣油的方法，包括以下步骤：（a）使油或残余物与酚醛树脂和稀释剂接触，以提供经稀释的酚醛树脂处理的油或残余物; 和（b）任选地从稀释的​​酚醛树脂处理的油或残余物中除去固体物质。

公开(公告)号：WO01062878A1

公开(公告)日：2001-08-30

申请号：PCT/KR2001/000279

申请日：2001-02-23

IPC: F23K5/12 ,  B01F3/08 ,  B01F3/10 ,  B01J19/10 ,  C10G31/00 ,  C10G32/00 ,  C10L1/00 ,  C10L1/32

CPC classification number: B01F3/0819 ,  B01F2003/105 ,  B01F2215/0088 ,  B01J19/10 ,  C10G31/00 ,  C10L1/328

Abstract: According to the present invention, there is provided an ultrasonically operated liquid fuel modifying device for applying an ultrasonic wave to liquid fuel having high viscosity and poor quality, and modifying it into good emulsified oil. The modifying system of the present invention comprises: a fuel tank (10) for storing liquid fuel having high viscosity and poor quality; a water tank (20) for storing water; an agitating device (30) for agitating the liquid fuel and water fed from the fuel and water tanks (10, 20), respectively; and an ultrasonically operated modifying device (40) including an ultrasonic vibration generator (56) for generating an ultrasonic wave so as to apply the ultrasonic wave to the liquid fuel and the water fed from the agitating device (30) and to modify it into good emulsified oil, and ultrasonic wave-generating portions (65).

Abstract translation: 根据本发明，提供了一种超声波操作的液体燃料改性装置，用于向具有高粘度和差质量的液体燃料施加超声波，并将其改性成良好的乳化油。 本发明的修改系统包括：用于储存具有高粘度和差质量的液体燃料的燃料箱（10） 一个用于储存水的水箱（20）; 搅拌装置（30），用于分别搅拌来自燃料和水箱（10,20）的液体燃料和水; 以及包括超声波振动发生器（56）的超声波操作改变装置（40），用于产生超声波，以将超声波施加到液体燃料和从搅拌装置（30）供给的水并将其改为良好 乳化油和超声波发生部（65）。