公开(公告)号：US09428697B2

公开(公告)日：2016-08-30

申请号：US13885276

申请日：2011-11-15

Applicant: Xiangjin Zhou

Inventor： Xiangjin Zhou

IPC: C07C9/15 ,  C07C7/06 ,  C07C9/21 ,  C10G7/00 ,  C10L1/06 ,  C10L1/08 ,  C10L10/10 ,  C07C7/12 ,  C10L1/04 ,  C10G7/12

CPC classification number: C10G7/00 ,  C07C7/06 ,  C07C7/12 ,  C10G7/12 ,  C10G2300/305 ,  C10G2400/02 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10L10/10 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2290/543 ,  C07C9/21 ,  C07C9/15

Abstract: The present invention relates to a method for joint production of low octane gasoline and high octane gasoline. In the process of oil or light oil rectification, the extraction points of the distillates therein are finely divided, and the temperature ranges for extraction of fractions are narrowed down. Each of the low and high octane components having a high content in the range from C6-C12 (which may be extended to C5-C14 where necessary) is then separately extracted. After that, low octane components are combined into compression ignition low octane gasoline products, while high octane components are combined into high octane gasoline products. The remaining fractions are respectively added as supplementing agents into the low octane gasoline products or high octane gasoline products dependent on their octane ratings. Low octane gasoline is used in compression ignition gasoline engines, while high octane gasoline is used in spark ignition gasoline engines.

Abstract translation: 本发明涉及低辛烷值汽油和高辛烷值汽油联合生产的方法。 在油或轻油精馏过程中，其中馏出物的萃取点细分，萃取馏分的温度范围变窄。 然后分别提取在C6-C12（其可以在需要时延伸至C5-C14）范围内具有高含量的低和高辛烷值组分。 之后，将低辛烷值组分混合成压燃点燃低辛烷值汽油产品，高辛烷值组分组成高辛烷值汽油产品。 分别将其余部分作为补充剂添加到低辛烷值汽油产品或高辛烷值汽油产品中，这取决于它们的辛烷值。 低辛烷值汽油用于压燃点火汽油发动机，而高辛烷值汽油用于火花点火汽油发动机。

公开(公告)号：US09410452B2

公开(公告)日：2016-08-09

申请号：US14426083

申请日：2013-09-05

Applicant: POWERDYNE, INC.

Inventor： Geoffrey Hirson ,  Gus F. Shouse

IPC: C07C27/00 ,  F01K25/06 ,  B01J12/00 ,  C01B3/04 ,  B01D21/00 ,  B01D21/01 ,  B09B3/00 ,  H05H1/42 ,  H05H1/44 ,  C01B3/12 ,  C07C1/04 ,  C10G2/00 ,  B01J19/08 ,  C01B3/02 ,  C10L1/06 ,  C10L1/08 ,  H05H1/34 ,  F02C1/05

CPC classification number: F01K25/06 ,  B01D21/0009 ,  B01D21/01 ,  B01J12/002 ,  B01J19/088 ,  B01J2219/0809 ,  B01J2219/0815 ,  B01J2219/0875 ,  B01J2219/0877 ,  B01J2219/0898 ,  B09B3/005 ,  C01B3/02 ,  C01B3/042 ,  C01B3/12 ,  C01B2203/062 ,  C01B2203/0861 ,  C07C1/04 ,  C10G2/32 ,  C10J3/00 ,  C10J2300/1238 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10L1/06 ,  C10L1/08 ,  C10L2200/0415 ,  C10L2200/0423 ,  C10L2200/043 ,  C10L2200/0446 ,  C10L2290/38 ,  C10L2290/42 ,  F02C1/05 ,  H05H1/34 ,  H05H1/42 ,  H05H1/44 ,  Y02E50/32 ,  Y02E60/364 ,  Y02P20/13

Abstract: Methods of making fuel are described herein. A method may include providing a first working fluid, a second working fluid, and a third working fluid. The method may further include exposing the first working fluid to a first high-voltage electric field to produce a first plasma, exposing the second working fluid to a second high-voltage electric field to produce a second plasma, and exposing the third working fluid to a third high-voltage electric field to produce a third plasma. The method may also include contacting the third plasma, the second plasma, and the first plasma to form a plasma mixture, cooling the plasma mixture using a heat exchange device to form a cooled plasma mixture, and contacting the cooled plasma mixture with a catalyst to form a fuel fluid.

Abstract translation: 本文描述了制备燃料的方法。 一种方法可以包括提供第一工作流体，第二工作流体和第三工作流体。 该方法还可以包括将第一工作流体暴露于第一高压电场以产生第一等离子体，将第二工作流体暴露于第二高压电场以产生第二等离子体，并将第三工作流体暴露于 第三高压电场产生第三等离子体。 该方法还可以包括使第三等离子体，第二等离子体和第一等离子体接触以形成等离子体混合物，使用热交换装置冷却等离子体混合物以形成冷却的等离子体混合物，并将冷却的等离子体混合物与催化剂接触 形成燃料流体。

公开(公告)号：US20160222303A1

公开(公告)日：2016-08-04

申请号：US14940027

申请日：2015-11-12

Applicant: CHINA UNIVERSITY OF PETROLEUM-BEIJING

Inventor： JINSEN GAO ,  LIANG ZHAO ,  CHUNMING XU ,  TIANZHEN HAO ,  XIAONA HAN

IPC: C10G67/02 ,  C10L1/06 ,  C10G67/00 ,  C10G57/00 ,  C10G67/06

CPC classification number: C10G67/02 ,  C10G21/16 ,  C10G21/27 ,  C10G25/003 ,  C10G45/08 ,  C10G45/64 ,  C10G45/68 ,  C10G67/00 ,  C10G67/04 ,  C10G67/06 ,  C10G69/00 ,  C10G69/04 ,  C10L1/06 ,  C10L2200/0423 ,  C10L2270/023 ,  C10L2290/24 ,  C10L2290/543

Abstract: A method for upgrading fluid catalytic cracking gasoline includes the following steps: cutting fluid catalytic cracking gasoline into light, medium, and heavy gasoline fractions; subjecting the medium gasoline fraction to an aromatization/hydroisomerization reaction in the presence of a catalyst to obtain a desulfurized medium gasoline fraction; and blending the light gasoline fraction, the desulfurized medium gasoline fraction and the heavy gasoline fraction to obtain upgraded gasoline; where, a cutting temperature of the light and the medium gasoline fractions is 35-60° C., and a cutting temperature of the medium and the heavy gasoline fractions is 70-160° C. The method according to the present invention not only can realize deep desulfurization of fluid catalytic cracking gasoline, but also can improve octane number significantly.

Abstract translation: 一种升级流化催化裂化汽油的方法包括以下步骤：将流化催化裂化汽油切割成轻，中，重汽油馏分; 在催化剂存在下使介质汽油馏分进行芳构化/加氢异构化反应，得到脱硫介质汽油馏分; 并将轻汽油馏分，脱硫介质汽油馏分和重汽油馏分混合得到升级汽油; 其中光和中等汽油馏分的切割温度为35-60℃，介质和重汽油馏分的切割温度为70-160℃。根据本发明的方法不仅可以 实现流化催化裂化汽油的深度脱硫，也可显着提高辛烷值。

公开(公告)号：US09388350B2

公开(公告)日：2016-07-12

申请号：US14269480

申请日：2014-05-05

Applicant: Sunoco Partners Marketing & Terminals L.P.

Inventor： Keith D. Buchanan

IPC: C10L1/02 ,  C10L1/18 ,  C10L1/182 ,  C10L1/04 ,  C10L1/06 ,  C10L1/16

CPC classification number: C10L1/04 ,  C10L1/06 ,  C10L1/1608 ,  C10L1/1824 ,  C10L2290/24

Abstract: Methods and systems for blending multiple batches of mixed hydrocarbons into fuel streams downstream of the refinery are provided that do not compromise the octane value of the fuel and do not cause the volatility of the fuel to exceed volatilities imposed by government regulation.

公开(公告)号：US20160168491A1

公开(公告)日：2016-06-16

申请号：US14571763

申请日：2014-12-16

Applicant: Jianhua Yao ,  Dhananjay Ghonasgi ,  Tushar Choudhary ,  Warren Ewert

Inventor： Jianhua Yao ,  Dhananjay Ghonasgi ,  Tushar Choudhary ,  Warren Ewert

IPC: C10G69/12 ,  C10L1/08 ,  C10L1/06

CPC classification number: C10G69/126 ,  C10G9/36 ,  C10G45/00 ,  C10G50/00

Abstract: A process for converting ethane to liquid fuels may involve directing an ethane stream into an ethane cracking unit to produce an intermediate hydrocarbon stream and a raw ethylene stream; fractionating the intermediate hydrocarbon stream into a gasoline fraction and a diesel fraction; introducing the raw ethylene stream into an oligomerization unit; contacting the raw ethylene stream with an oligomerization catalyst to produce a liquid hydrocarbon stream and an off-gas stream; recycling an off-gas recycle stream from an off-gas stream of the oligomerization unit separation unit to an inlet of the oligomerization reactor; introducing at least part of the off-gas stream into a hydrogenation reactor to remove unconverted olefins; separating a hydrogen component and a plurality of light paraffin components in a post hydrogenation reactor separation unit using a PSA technology or membrane technology; and recycling the light paraffins stream into the ethane cracking unit.

Abstract translation: 将乙烷转化为液体燃料的方法可包括将乙烷流引入乙烷裂解装置以产生中间烃流和生乙烯流; 将中间烃流分馏成汽油馏分和柴油馏分; 将原料乙烯流引入低聚单元; 使原始乙烯流与低聚催化剂接触以产生液态烃流和废气流; 将来自所述低聚单元分离单元的废气流的废气再循环流再循环到所述低聚反应器的入口; 将至少部分废气流引入氢化反应器以除去未转化的烯烃; 使用PSA技术或膜技术在后氢化反应器分离单元中分离氢组分和多种轻链烷烃组分; 并将轻质石蜡料流再循环到乙烷裂解装置中。

公开(公告)号：US20160137938A1

公开(公告)日：2016-05-19

申请号：US15005733

申请日：2016-01-25

Applicant: SPINFLIP LLC

Inventor： ROBERT EASTWOOD COX ,  OLIVER HAMILTON BODINE ,  WILLIAM BRINTON COX

IPC: C10L1/06 ,  F02M27/04 ,  C10L1/08 ,  B03C1/02

CPC classification number: B03C1/288 ,  B03C1/02 ,  B03C2201/30 ,  C02F1/005 ,  C02F1/482 ,  C10L2290/40 ,  F02M27/045

Abstract: An apparatus and methodology is presented for magnetically conditioning any hydrocarbon based fluid flowing through a conduit or pipe. The object of the invention is to advance the art by increasing the range of application, the effectiveness, the simplicity and the ease of use of a magnetic fluid conditioning device. The invention accomplishes this by a unique magnetic and mechanical configuration, not taught in the art or previously known to the applicants.

Abstract translation: 提出了用于磁化调节流过导管或管道的任何基于烃的流体的装置和方法。 本发明的目的是通过增加磁性流体调节装置的应用范围，有效性，简单性和易用性来推进该技术。 本发明通过独特的磁性和机械结构实现了这一点，本领域没有教授或者以前为申请人所知。

公开(公告)号：US20160137934A1

公开(公告)日：2016-05-19

申请号：US14548109

申请日：2014-11-19

Applicant: UOP LLC

Inventor： Charles P. Luebke ,  Christopher P. Nicholas

IPC: C10G69/12 ,  C10L1/06

CPC classification number: C10G69/126 ,  C10G50/00

Abstract: A process and apparatus for controlling the amount of gasoline and distillate obtained from an oligomerate product is described. The process includes oligomerizing olefins in a feed stream to produce a mixture of an oligomerate product and unreacted feed. The mixture is separated into a light stream comprising the unreacted feed and the oligomerate product. Some or all of the oligomerate product is hydrogenated to produce hydrotreated oligomerate product. The hydrotreated oligomerate product can be separated into gasoline and distillate. A recycle stream comprising at least one of non-hydrotreated oligomerate product and hydrotreated oligomerate product is introduced into the oligomerization zone. The flow rates of non-hydrotreated oligomerate product and hydrotreated oligomerate product in the recycle stream are controlled to control the amount of gasoline and distillate product produced.

Abstract translation: 描述了用于控制从低聚产物获得的汽油和馏出物的量的方法和装置。 该方法包括在进料流中使烯烃低聚以产生低聚产物和未反应的进料的混合物。 将混合物分离成包含未反应进料和低聚产物的轻质流。 一些或全部低聚产物被氢化以产生加氢处理的低聚产物。 加氢处理的低聚产物可以分离成汽油和馏出物。 将包含非加氢处理的低聚物产物和加氢处理的低聚物产物中的至少一种的再循环物流引入低聚区。 控制循环流中非加氢处理的低聚产物和加氢处理的低聚产物的流速以控制产生的汽油和馏出物的量。

公开(公告)号：US09327279B2

公开(公告)日：2016-05-03

申请号：US13604115

申请日：2012-09-05

Applicant: Benjamin G. Harvey ,  Heather A. Meylemans ,  Roxanne L. Quintana

Inventor： Benjamin G. Harvey ,  Heather A. Meylemans ,  Roxanne L. Quintana

IPC: C10L1/16 ,  C07C1/22 ,  C07C1/24 ,  C07C13/32 ,  C07C9/00 ,  B01J31/18 ,  B01J31/14 ,  B01J31/22 ,  C10G45/00 ,  C10G50/00 ,  C10G69/12 ,  C10L1/08 ,  C10G45/32 ,  C10G45/58 ,  C10G65/04 ,  C10G65/06 ,  C10L1/04 ,  C10L1/06 ,  C10G3/00

CPC classification number: C07C1/20 ,  B01J31/143 ,  B01J31/189 ,  B01J31/2265 ,  B01J31/2273 ,  B01J31/2278 ,  B01J31/2295 ,  B01J2231/20 ,  B01J2531/48 ,  B01J2531/821 ,  C07C1/24 ,  C07C2/08 ,  C07C5/03 ,  C07C29/00 ,  C07C2523/42 ,  C07C2527/167 ,  C07C2531/22 ,  C07C2601/10 ,  C07C2603/68 ,  C08F110/10 ,  C10G3/42 ,  C10G45/00 ,  C10G45/32 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G65/06 ,  C10G69/126 ,  C10G2300/1011 ,  C10G2300/1092 ,  C10G2300/302 ,  C10G2300/308 ,  C10G2300/44 ,  C10G2300/703 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/22 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2270/023 ,  C10L2270/04 ,  Y02E50/13 ,  Y02P30/20 ,  C07C13/15 ,  C07C13/32 ,  C07C35/06

Abstract: A highly efficient method for the conversion of a natural product into the high density fuel RJ-4 with concomitant evolution of isobutylene for conversion to fuels and polymers, more specifically, embodiments of the invention relate to efficient methods for the conversion of the renewable, linear terpene alcohol, linalool into a drop-in, high density fuel suitable for ramjet or missile propulsion.

Abstract translation: 用于将天然产物转化为高密度燃料RJ-4的高效方法，同时伴随着异丁烯的转化转化成燃料和聚合物，更具体地说，本发明的实施方案涉及转化可再生的，线性的 萜烯醇，芳樟醇成为适用于冲压式或导弹推进的滴灌，高密度燃料。

公开(公告)号：US09273570B2

公开(公告)日：2016-03-01

申请号：US14426093

申请日：2013-09-05

Applicant: POWERDYNE, INC.

Inventor： Geoffrey Hirson ,  Gus F. Shouse

IPC: F23J15/00 ,  F01K25/06 ,  B01J12/00 ,  C01B3/04 ,  B01D21/00 ,  B01D21/01 ,  B09B3/00 ,  H05H1/42 ,  H05H1/44 ,  C01B3/12 ,  C07C1/04 ,  C10G2/00 ,  B01J19/08 ,  C01B3/02 ,  C10L1/06 ,  C10L1/08 ,  H05H1/34 ,  F02C1/05

CPC classification number: F01K25/06 ,  B01D21/0009 ,  B01D21/01 ,  B01J12/002 ,  B01J19/088 ,  B01J2219/00063 ,  B01J2219/00162 ,  B01J2219/00186 ,  B01J2219/0809 ,  B01J2219/0815 ,  B01J2219/0871 ,  B01J2219/0875 ,  B01J2219/0877 ,  B01J2219/0879 ,  B01J2219/0898 ,  B03C3/025 ,  B03C3/16 ,  B09B3/005 ,  C01B3/02 ,  C01B3/042 ,  C01B3/12 ,  C01B2203/062 ,  C01B2203/0861 ,  C07C1/04 ,  C10G2/32 ,  C10J3/00 ,  C10J2300/1238 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10L1/06 ,  C10L1/08 ,  C10L2200/0415 ,  C10L2200/0423 ,  C10L2200/043 ,  C10L2200/0446 ,  C10L2290/38 ,  C10L2290/42 ,  F02C1/05 ,  H05H1/34 ,  H05H1/42 ,  H05H1/44 ,  H05H1/48 ,  Y02E50/32 ,  Y02E60/364 ,  Y02P20/13 ,  Y02T50/678

Abstract: In a first processing chamber, a feedstock may be combined with plasma from three plasma torches to form a first fluid mixture. Each torch may have a working gas including water vapor, oxygen, and carbon dioxide. The first fluid mixture may be cooled and may contact a first heat exchange device. Water in the first heat exchange device may be converted to steam to generate electric power. The output fluid from the first heat exchange device may be separated into one or more components. A syngas may be derived from the one or more components and have a ratio of carbon monoxide to hydrogen of about 1:2. The syngas may be heated in a second processing chamber and then cooled to form a second admixture. The second admixture may contact a second heat exchange device that may make steam to power a second electrical generator.

Abstract translation: 在第一处理室中，原料可以与来自三个等离子体炬的等离子体组合以形成第一流体混合物。 每个手电筒可能具有包括水蒸气，氧气和二氧化碳在内的工作气体。 第一流体混合物可以被冷却并且可以接触第一热交换装置。 第一热交换装置中的水可以被转换为蒸汽以产生电力。 来自第一热交换装置的输出流体可以被分离成一个或多个部件。 合成气可以衍生自一种或多种组分，并且一氧化碳与氢的比例为约1:2。 可以在第二处理室中加热合成气，然后冷却以形成第二混合物。 第二混合物可接触第二热交换装置，其可以使蒸汽为第二发电机供电。

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。