公开(公告)号：US20130237739A1

公开(公告)日：2013-09-12

申请号：US13885276

申请日：2011-11-15

Applicant: Xiangjin Zhou

Inventor： Xiangjin Zhou

IPC: C10G7/00 ,  C10L10/10

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：US08530715B2

公开(公告)日：2013-09-10

申请号：US13673400

申请日：2012-11-09

Applicant: Energy & Environmental Research Center Foundation

Inventor： Joshua R. Strege ,  Benjamin G. Oster ,  Paul D. Pansegrau ,  Chad A. Wocken ,  Ted R. Aulich ,  Marc D. Kurz

IPC: C07C1/00

CPC classification number: C10G3/50 ,  C10G3/42 ,  C10G3/45 ,  C10G3/46 ,  C10G3/47 ,  C10G3/60 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/4006 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678

Abstract: The present invention relates to production of fuels or fuel blendstocks from renewable sources. Various embodiments provide a method of producing a hydrocarbon product by hydrotreating a feedstock including at least one of a renewable triacylglyceride (TAG), renewable free fatty acid (FFA), and renewable fatty acid C1-C5 alkyl ester (C1-C5 FAE) in the presence of a nonsulfided hydrotreating catalyst to produce a first product including hydrocarbons. In some examples, the first product can be subjected to further chemical transformations such as aromatization, cracking, or isomerization to produce a second product including hydrocarbons. In various embodiments, the first or second hydrocarbon product with minimal or substantially no further processing can be suitable as a liquid transportation fuel or fuel blendstock, including fuels such as gasoline, naptha, kerosene, jet fuel, and diesel fuels.

Abstract translation: 本发明涉及从可再生资源生产燃料或燃料混合料。 各种实施方案提供了通过加氢处理包含可再生三酰基甘油酯（TAG），可再生游离脂肪酸（FFA）和可再生脂肪酸C 1 -C 5烷基酯（C 1 -C 5 FAE）中的至少一种的原料来生产烃产物的方法， 存在非硫化的加氢处理催化剂以产生包括烃的第一产物。 在一些实例中，第一产物可以进行进一步的化学转化，例如芳构化，裂化或异构化，以产生包括烃的第二产物。 在各种实施方案中，具有最小或基本上不进一步处理的第一或第二烃产物可以适合作为液体运输燃料或燃料混合物料，包括燃料如汽油，石脑油，煤油，喷气燃料和柴油燃料。

公开(公告)号：US08524970B2

公开(公告)日：2013-09-03

申请号：US12599554

申请日：2008-04-29

Applicant: Martin Rothaemel ,  Uwe Fincke ,  Holger Dropsch ,  Henning Buchold

Inventor： Martin Rothaemel ,  Uwe Fincke ,  Holger Dropsch ,  Henning Buchold

IPC: C07C1/00 ,  C07C2/00 ,  C07C4/00 ,  C07C5/00 ,  C07C6/00 ,  C10G51/02 ,  C10G55/02 ,  C10B57/02

CPC classification number: C10G50/00 ,  C07C1/20 ,  C10G3/49 ,  C10G3/54 ,  C10G2400/02 ,  C10G2400/04 ,  C10L1/06 ,  C10L1/08 ,  Y02P30/20 ,  C07C11/02

Abstract: In a process for producing synthetic fuels from an educt mixture containing hydrogen and oxygenates, such as methanol and/or dimethyl ether, the educt mixture is reacted on a catalyst in a first process stage to obtain a hydrocarbon product containing olefins with preferably 2 to 8 carbon atoms. In a second process stage the hydrocarbon product is oligomerized to long-chain olefins, from which gasoline and Diesel products are obtained. The hydrocarbon product obtained in the first process stage is separated into a liquid phase and a gaseous phase. The gaseous phase is supplied to the second process stage. The liquid phase is separated into a mixture rich in C6− hydrocarbons and a mixture containing C7+ hydrocarbons and aromatics. The mixture rich in C6− hydrocarbons is supplied to the second process stage. The mixture containing C7+ hydrocarbons −+ and aromatics can be admixed to the gasoline product for quality improvement.

Abstract translation: 在由含有氢和含氧化合物如甲醇和/或二甲醚的溶出混合物制备合成燃料的方法中，在第一工艺阶段中，将催化剂混合物在催化剂上反应，以获得含有优选2至8个 碳原子。 在第二个工艺阶段，烃产物被低聚化成长链烯烃，从中获得汽油和柴油产品。 将在第一工艺阶段获得的烃产物分离成液相和气相。 气相被供给到第二处理级。 将液相分离成富含C6-烃的混合物和含有C7 +烃和芳族化合物的混合物。 富含C6-烃的混合物供应到第二个工艺阶段。 含有C7 +烃+和芳族化合物的混合物可以与汽油产品混合，以提高质量。

公开(公告)号：US20130217906A1

公开(公告)日：2013-08-22

申请号：US13827153

申请日：2013-03-14

Applicant: ELEVANCE RENEWABLE SCIENCES, INC.

Inventor： Linda A. Kunz ,  Tessa M. Pals ,  Steven A. Cohen ,  Melvin L. Luetkens, JR. ,  Chander Balakrishnan ,  Robert B. Snyder

IPC: C10G3/00 ,  C11C3/12

CPC classification number: C11C3/126 ,  C07C1/213 ,  C07C5/03 ,  C07C5/05 ,  C07C6/04 ,  C07C7/13 ,  C07C2523/28 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/46 ,  C07C2523/72 ,  C07C2523/745 ,  C07C2523/755 ,  C10G3/42 ,  C10G3/44 ,  C10G3/50 ,  C10G29/205 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G69/123 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1088 ,  C10G2300/30 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/22 ,  C10L1/00 ,  C10L1/026 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2200/0476 ,  C11B3/00 ,  C11C3/003 ,  C11C3/10 ,  C11C3/12 ,  C11C3/123 ,  Y02P20/582 ,  Y02P30/20 ,  C07C11/02 ,  C07C11/12 ,  C07C9/14 ,  C07C9/22 ,  C07C11/21

Abstract: Methods are provided for refining natural oil feedstocks and partially hydrogenating polyunsaturated olefins and polyunsaturated esters. 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 polyunsaturated olefins from the polyunsaturated esters in the metathesized product. In certain embodiments, the methods further comprise partially hydrogenating the polyunsaturated olefins in the presence of a hydrogenation catalyst, wherein at least a portion of the polyunsaturated olefins are converted to monounsaturated olefins. In other embodiments, the methods further comprise partially hydrogenating the polyunsaturated esters in the presence of a hydrogenation catalyst, wherein at least a portion of the polyunsaturated esters are converted to monounsaturated esters.

Abstract translation: 提供了用于澄清天然油原料和部分氢化多不饱和烯烃和多不饱和酯的方法。 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，所述方法还包括从所述多元不饱和酯中分离所述多不饱和烯烃。 在某些实施方案中，所述方法还包括在氢化催化剂存在下部分氢化多不饱和烯烃，其中至少一部分多不饱和烯烃转化为单不饱和烯烃。 在其它实施方案中，所述方法还包括在氢化催化剂存在下部分氢化多不饱和酯，其中至少一部分多不饱和酯转化为单不饱和酯。

公开(公告)号：US08487149B2

公开(公告)日：2013-07-16

申请号：US13557066

申请日：2012-07-24

Applicant: Patrick R. Gruber ,  Matthew W. Peters ,  Josefa M. Griffith ,  Yassin Al Obaidi ,  Leo E. Manzer ,  Joshua D. Taylor ,  David E. Henton

Inventor： Patrick R. Gruber ,  Matthew W. Peters ,  Josefa M. Griffith ,  Yassin Al Obaidi ,  Leo E. Manzer ,  Joshua D. Taylor ,  David E. Henton

IPC: C10L1/04 ,  C10G3/00 ,  C12P7/02

CPC classification number: C10L1/08 ,  C07C1/24 ,  C07C2/08 ,  C07C2/76 ,  C07C5/03 ,  C07C9/14 ,  C07C9/15 ,  C07C51/265 ,  C10G3/00 ,  C10G50/00 ,  C10G69/126 ,  C10G2300/1011 ,  C10G2300/42 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/30 ,  C10L1/04 ,  C10L1/06 ,  C10L2200/043 ,  C10L2200/0469 ,  C10L2270/04 ,  C10L2290/26 ,  C10L2290/543 ,  C12P5/00 ,  C12P7/04 ,  C12P7/06 ,  C12P7/16 ,  Y02E50/10 ,  Y02E50/13 ,  Y02E50/17 ,  Y02P30/20 ,  Y02T50/678 ,  C07C11/02 ,  C07C15/00 ,  C07C63/26 ,  C07C11/09

Abstract: The present invention is directed to renewable compositions derived from fermentation of biomass, and integrated methods of preparing such compositions.

Abstract translation: 本发明涉及来自生物质发酵的可再生组合物，以及制备这种组合物的综合方法。

公开(公告)号：US20130152459A1

公开(公告)日：2013-06-20

申请号：US13327516

申请日：2011-12-15

Applicant: Soumendra M. Banerjee ,  Richard K. Hoehn

Inventor： Soumendra M. Banerjee ,  Richard K. Hoehn

IPC: C10L1/02

CPC classification number: C10G45/02 ,  C10G3/42 ,  C10G3/50 ,  C10G49/002 ,  C10G65/04 ,  C10G2300/1055 ,  C10G2300/4006 ,  C10G2400/04 ,  C10L1/026 ,  C10L1/08 ,  Y02P30/20

Abstract: Hydrotreating methods and hydrotreating systems are provided herein. In an embodiment, a hydrotreating method includes heating a petroleum-based diesel feed. The heated petroleum-based diesel feed is introduced to a hydrotreating process. An unheated carbonaceous feed is introduced to the hydrotreating process separate from the heated petroleum-based diesel feed. The heated petroleum-based diesel feed and the unheated carbonaceous feed are co-processed in the hydrotreating process. In an embodiment of a hydrotreating system, the hydrotreating system includes a hydrotreating unit, and a heating apparatus, with the heating apparatus heating petroleum-based diesel feed prior to introduction to the hydrotreating unit. The unheated carbonaceous feed source is in fluid communication with the hydrotreating unit for introducing an unheated carbonaceous feed to the hydrotreating unit separate from the petroleum-based diesel feed.

Abstract translation: 本文提供加氢处理方法和加氢处理系统。 在一个实施方案中，加氢处理方法包括加热石油基柴油原料。 将加热的石油基柴油原料引入加氢处理工艺中。 将未加热的碳质进料引入与加热的石油基柴油原料分离的加氢处理工艺。 加热的石油基柴油原料和未加热的碳质进料在加氢处理过程中进行共处理。 在加氢处理系统的一个实施方案中，加氢处理系统包括加氢处理单元和加热装置，加热装置在引入加氢处理装置之前加热石油基柴油原料。 未加热的碳质进料源与加氢处理单元流体连通，用于将未加热的碳质进料引入与石油基柴油进料分开的加氢处理装置。

公开(公告)号：US20130146508A1

公开(公告)日：2013-06-13

申请号：US13706713

申请日：2012-12-06

Applicant: IFP Energies Nouvelles

Inventor： Alain QUIGNARD ,  Eric SANCHEZ ,  Jean Francois LE COZ

IPC: C10G1/00

CPC classification number: C10G1/006 ,  C10G1/002 ,  C10G1/06 ,  C10G1/08 ,  C10G35/04 ,  C10G47/02 ,  C10G49/002 ,  C10G63/00 ,  C10G63/04 ,  C10G2400/20 ,  C10G2400/30 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08

Abstract: The invention relates to a process for coal conversion, optionally in co-processing with other feedstocks, notably of the biomass type, comprising at least one liquefaction step, followed by a fixed-bed hydrocracking step and a catalytic reforming step. With this process, aromatic compounds can be obtained from a feedstock containing coal.

Abstract translation: 本发明涉及一种煤转化方法，任选地与其他原料（特别是生物质类型）共处理，包括至少一个液化步骤，随后是固定床加氢裂化步骤和催化重整步骤。 通过该方法，可以从包含煤的原料获得芳族化合物。

公开(公告)号：US20130125453A1

公开(公告)日：2013-05-23

申请号：US13806482

申请日：2011-06-10

Applicant: Xiangjin Zhou

Inventor： Xiangjin Zhou

IPC: C10L1/08 ,  C10L1/182 ,  C10L1/185

CPC classification number: C10L1/08 ,  C10G2300/305 ,  C10G2400/02 ,  C10L1/023 ,  C10L1/06 ,  C10L1/14 ,  C10L1/1616 ,  C10L1/182 ,  C10L1/1824 ,  C10L1/1852 ,  C10L2200/0423 ,  C10L2200/043 ,  C10L2200/0446 ,  C10L2230/22

Abstract: A clean, high efficient and environmentally friendly gasoline product with main fractions of C6-C11 has a low octane rating and a low spontaneous ignition temperature. It can be compressively ignited within an internal combustion engine with a compression ratio of 16-19. Small amount of ethanol or dimethyl ether can be added into the gasoline product.

Abstract translation: 具有C6-C11主要馏分的清洁，高效，环保的汽油产品具有低辛烷值和低自燃温度。 可以在内燃机内以压缩比16-19压缩点火。 少量乙醇或二甲醚可加入汽油产品中。

公开(公告)号：US08366907B2

公开(公告)日：2013-02-05

申请号：US12848887

申请日：2010-08-02

Applicant: Richard T. Hallen ,  Karl O. Albrecht ,  Heather M. Brown ,  James F. White

Inventor： Richard T. Hallen ,  Karl O. Albrecht ,  Heather M. Brown ,  James F. White

IPC: C10M101/00 ,  C10M177/00 ,  C10G71/00

CPC classification number: B01J23/6525 ,  B01J21/066 ,  B01J21/18 ,  B01J23/624 ,  B01J23/626 ,  B01J23/6527 ,  B01J37/0203 ,  B01J37/0205 ,  C10G3/44 ,  C10G3/47 ,  C10G3/48 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/205 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/4081 ,  C10G2300/44 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/30 ,  C10L1/08 ,  C10L1/1208 ,  C10L2200/0469 ,  C10L2270/02 ,  C10L2270/04 ,  C11C3/00 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678

Abstract: Embodiments of methods for making renewable diesel by deoxygenating (decarboxylating/decarbonylating/dehydrating) fatty acids to produce hydrocarbons are disclosed. Fatty acids are exposed to a catalyst selected from a) Pt and MO3 on ZrO2 (M is W, Mo, or a combination thereof), or b) Pt/Ge or Pt/Sn on carbon, and the catalyst decarboxylates at least 10% of the fatty acids. In particular embodiments, the catalyst consists essentially of 0.7 wt % Pt and 12 wt % WO3, relative to a mass of catalyst, or the catalyst consists essentially of a) 5 wt % Pt and b) 0.5 wt % Ge or 0.5 wt % Sn, relative to a mass of catalyst. Deoxygenation is performed without added hydrogen and at less than 100 psi. Disclosed embodiments of the catalysts deoxygenate at least 10% of fatty acids in a fatty acid feed, and remain capable of deoxygenating fatty acids for at least 200 minutes to more than 350 hours.

公开(公告)号：US20130015100A1

公开(公告)日：2013-01-17

申请号：US13535983

申请日：2012-06-28

Applicant: Pedro Pereira Almao ,  Gustavo Luis Trujillo ,  Enzo Peluso ,  Carmen Galarraga ,  Clementina Sosa ,  Carlos Scott Algara ,  Francisco Lopez-Linares ,  Lante Antonio Carbognani Ortega ,  Nestor Gregorio Zerpa Reques

Inventor： Pedro Pereira Almao ,  Gustavo Luis Trujillo ,  Enzo Peluso ,  Carmen Galarraga ,  Clementina Sosa ,  Carlos Scott Algara ,  Francisco Lopez-Linares ,  Lante Antonio Carbognani Ortega ,  Nestor Gregorio Zerpa Reques

IPC: C10G55/06 ,  B01J23/755 ,  B01J8/00 ,  C10G51/06 ,  C10G11/02

CPC classification number: C10G55/04 ,  C10G9/36 ,  C10G21/003 ,  C10G2300/1059 ,  C10G2300/1077 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/308 ,  C10L1/08

Abstract: This invention relates to systems and methods for catalytic steam cracking of non-asphaltene containing heavy hydrocarbon fractions. The method enables upgrading heavy hydrocarbons to hydrocarbons capable of being transported through pipelines and/or a pretreated step before further treatment in an upgrading refinery, including the steps of separating the heavy hydrocarbon mixture into a light fraction, a full gasoil fraction and a vacuum residue fraction with or without at least partial reduction or asphaltenes; adding a catalyst to the full gasoil and/or to the blend of this with a reduced asphaltenes fraction and subjecting the catalyst-full gasoil and/or deasphalted oil fraction to catalytic steam cracking to form an effluent stream; separating the effluent stream into a gas stream and a liquid stream; and mixing the liquid stream with the light fraction and the vacuum residue fraction to form an upgraded oil. The system includes hardware capable of performing the method.

Abstract translation: 本发明涉及用于非沥青质含重烃馏分的催化蒸汽裂化的系统和方法。 该方法使重质烃能够在升级炼油厂中进一步处理之前将重质烃升级为能够通过管道运输的烃和/或预处理步骤，包括将重质烃混合物分离成轻馏分，全油馏分和减压渣油 具有或不具有至少部分还原或沥青质的级分; 向完整的油气和/或其共混物中加入催化剂和还原的沥青质馏分，并使催化剂完整的油和/或脱沥青的油馏分进行催化蒸汽裂化以形成流出物流; 将流出物流分离成气流和液体流; 并将液体流与轻馏分和减压渣油馏分混合以形成升级油。 该系统包括能够执行该方法的硬件。