公开(公告)号：US20110232162A1

公开(公告)日：2011-09-29

申请号：US13038060

申请日：2011-03-01

Applicant: Michael SISKIN ,  Glen E. PHILLIPS ,  Simon R. KELEMEN

Inventor： Michael SISKIN ,  Glen E. PHILLIPS ,  Simon R. KELEMEN

IPC: C10L1/00

CPC classification number: C10G1/00 ,  C10G1/04 ,  C10G1/083 ,  C10G2300/1014 ,  Y02P30/20

Abstract: A lignocellulosic biomass material is converted into precursors for liquid hydrocarbon transportation fuels by contacting the biomass material with water and carbon monoxide at elevated temperature, typically from 280 to 350° C., an elevated pressure, typically a total system pressure of 12 to 30 MPa and a CO partial pressure from 5 to 10 MPa and a weight ratio of water:biomass material from 0.5:1 to 5.0:1, to dissolve the biomass material into the reaction mixture and depolymerize, deoxygenate and hydrogenate the lignocellulose biomass material, so converting the biomass material into liquid transportation fuel precursors.

Abstract translation: 木质纤维素生物质材料通过使生物质材料与水和一氧化碳在升高的温度（通常为280-350℃），升高的压力（通常为12-30MPa的总体系压力）接触而转化为液体烃运输燃料的前体 和5〜10MPa的CO分压和水：生物质材料的重量比为0.5:1至5.0:1，将生物质材料溶解到反应混合物中，解聚，脱氧和氢化木质纤维素生物质材料，从而转化 生物质材料成为液体运输燃料前体。

公开(公告)号：US20110219670A1

公开(公告)日：2011-09-15

申请号：US12989138

申请日：2009-04-24

Applicant: Uwe Berger ,  Thomas Willner ,  Walter Vanselow

Inventor： Uwe Berger ,  Thomas Willner ,  Walter Vanselow

IPC: C10L1/00 ,  B01J19/00 ,  B01J8/08

CPC classification number: B01J8/226 ,  B01J8/003 ,  B01J8/004 ,  B01J8/0045 ,  B01J8/20 ,  B01J8/224 ,  B01J8/228 ,  B01J19/2455 ,  B01J19/246 ,  B01J19/2465 ,  B01J19/26 ,  B01J2208/00106 ,  B01J2208/00442 ,  B01J2208/00752 ,  B01J2208/00902 ,  B01J2219/00247 ,  C10G1/02 ,  C10G2300/1011 ,  Y02P30/20

Abstract: The invent on relates to a device for producing starting materials, combustible suhstances and fuels from organic substances. Said device comprises a reactor (10) that comprises a feeding device (11) for the organic substances, a discharge device (12) tor the reaction products, and a device (13) for supplying reaction energy for the transformation of organic substances into the reaction products. The invention is characterised in that the reactor (10) comprises a device (14) for forming a circulating now inside the reactor.

Abstract translation: 本发明涉及一种用于生产原料，可燃性物质和有机物质燃料的装置。 所述装置包括反应器（10），其包括用于有机物质的进料装置（11），反应产物的排放装置（12）和用于将有机物质转化成反应产物的反应能量的装置（13） 反应产物。 本发明的特征在于，反应器（10）包括用于在反应器内形成循环的装置（14）。

公开(公告)号：US20110179698A1

公开(公告)日：2011-07-28

申请号：US12983313

申请日：2011-01-02

Applicant: Hassan Agha

Inventor： Hassan Agha

IPC: C10L1/19 ,  C10L1/18 ,  C10L1/00 ,  C10G17/02

CPC classification number: C10L1/103 ,  C10L1/1208 ,  C10L1/1266 ,  C10L1/1811 ,  C10L1/182 ,  C10L1/23 ,  C10L1/231 ,  C10L10/12

Abstract: The present invention relates to a process for producing clean petroleum fuel by reducing sulfur content, and raising the Cetane Number to a value above 50, in a process that may be carried out at one atmospheric pressure.

Abstract translation: 本发明涉及通过在一个大气压下进行的方法，通过降低硫含量，将十六烷值提高到50以上，从而生产清洁石油燃料的方法。

公开(公告)号：US20110167713A1

公开(公告)日：2011-07-14

申请号：US13004304

申请日：2011-01-11

Applicant: Alain Quignard ,  Wilfried Weiss

Inventor： Alain Quignard ,  Wilfried Weiss

IPC: C10L1/00

CPC classification number: C10G1/08 ,  B01J23/40 ,  B01J23/652 ,  B01J23/75 ,  B01J23/755 ,  B01J23/85 ,  B01J23/883 ,  B01J37/20 ,  C10G1/083 ,  C10G3/45 ,  C10G3/46 ,  C10G3/47 ,  C10G3/48 ,  C10G3/50 ,  C10G3/56 ,  C10G2300/1014 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/44 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  Y02E50/10 ,  Y02E50/30 ,  Y02P30/20

Abstract: A process for direct hydroliquefaction of biomass selected from algae, lignocellulosic biomass and/or of one or more constituents of lignocellulosic biomass selected from the group comprising cellulose, hemicellulose and/or lignin for producing fuel bases comprising two successive hydroconversion stages under high hydrogen pressure in ebullating bed reactors. Hydroconversion takes place in the presence of a supported catalyst of the type for hydroconversion of petroleum residue and a suspension composed of the biomass and a solvent, preferably a hydrogen donor solvent and preferably recycled from the process. The biomass can undergo a pretreatment of drying and/or roasting and/or grinding and/or demineralization prior to hydroliquefaction.

Abstract translation: 用于直接氢化选自藻类，木质纤维素生物质和/或木质纤维素生物质的一种或多种木质纤维素生物质成分的生物质的方法，所述木质纤维素生物质选自包含纤维素，半纤维素和/或木质素的组，用于生产燃料基质，包括在高氢压力下两个连续的加氢转化阶段 沸腾床反应器。 加氢转化是在石油残渣加氢转化类型的负载催化剂和由生物质和溶剂（优选氢供体溶剂）组成的悬浮液存在下进行的，优选从该方法回收。 生物质可以在水解液化之前进行干燥和/或焙烧和/或研磨和/或去矿化的预处理。

公开(公告)号：US20110154722A1

公开(公告)日：2011-06-30

申请号：US12972154

申请日：2010-12-17

Applicant: Juben Nemchand CHHEDA ,  Joseph Broun Powell

Inventor： Juben Nemchand CHHEDA ,  Joseph Broun Powell

IPC: C10L1/00 ,  B01J8/00

CPC classification number: C10L1/1826 ,  C10G3/45 ,  C10G3/46 ,  C10G3/47 ,  C10G3/49 ,  C10G2300/1011 ,  C10G2300/4025 ,  C10G2300/44 ,  C10G2300/80 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/1824 ,  Y02E50/13 ,  Y02E50/30 ,  Y02P30/20 ,  Y02T50/678

Abstract: A method comprises providing a bio-based feedstock; contacting the bio-based feedstock with a solvent in a hydrolysis reaction to form an intermediate stream comprising carbohydrates; contacting the intermediate stream with an apr catalyst to form a plurality of oxygenated intermediates, wherein a first portion of the oxygenated intermediates are recycled to form the solvent; and processing at least a second portion of the oxygenated intermediates to form a fuel blend.

Abstract translation: 一种方法包括提供基于生物的原料; 在水解反应中使生物基原料与溶剂接触以形成包含碳水化合物的中间物流; 使中间流与apr催化剂接触以形成多个含氧中间体，其中将氧化中间体的第一部分再循环以形成溶剂; 以及处理所述氧化中间体的至少第二部分以形成燃料混合物。

公开(公告)号：US20110154720A1

公开(公告)日：2011-06-30

申请号：US12917988

申请日：2010-11-02

Applicant: Robert Bartek ,  Michael Brady ,  Dennis Stamires ,  Steve Yanik ,  Paul O'Connor ,  Jacobus C. Rasser

Inventor： Robert Bartek ,  Michael Brady ,  Dennis Stamires ,  Steve Yanik ,  Paul O'Connor ,  Jacobus C. Rasser

IPC: C10L1/00 ,  B01J8/00

CPC classification number: C10G11/18 ,  C10G1/002 ,  C10G1/06 ,  C10G1/08 ,  C10G3/42 ,  C10G3/50 ,  C10G3/56 ,  C10G3/57 ,  C10G3/62 ,  C10G45/02 ,  C10G47/00 ,  C10G47/02 ,  C10G47/30 ,  C10G47/34 ,  C10G49/007 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  Y02P30/20

Abstract: A process for producing fuel from biomass is disclosed herein. The process includes torrefying biomass material at a temperature between 80° C. to 400° C. to form particulated biomass having a mean average particle size between 1 μm and 1000 μm. The particulated biomass is mixed with a liquid hydrocarbon to form a suspension, wherein the suspension includes from 1 weight percent to 40 weight percent particulated biomass. The suspension is fed into a unit selected from the group consisting of a pyrolysis reactor, a fluid catalytic cracking unit, a delayed coker, a fluid coker, a hydroprocessing unit, and a hydrocracking unit, and then at least a portion of the particulated biomass of the suspension is converted into fuel.

Abstract translation: 本文公开了一种从生物质生产燃料的方法。 该方法包括在80℃至400℃的温度下焙烧生物质材料，以形成平均粒度为1μm至1000μm的颗粒状生物质。 将颗粒状生物质与液体烃混合以形成悬浮液，其中悬浮液包括1重量％至40重量％的颗粒生物质。 将悬浮液加入到选自热解反应器，流化催化裂化装置，延迟焦化器，流体焦化器，加氢处理装置和加氢裂化装置中的单元中，然后将至少一部分颗粒生物质 的悬浮液转化为燃料。

公开(公告)号：US07964173B2

公开(公告)日：2011-06-21

申请号：US12094222

申请日：2006-12-27

Applicant: Takashi Oyama ,  Kazuhisa Nakanishi ,  Tamotsu Tano ,  Keiji Higashi ,  Ippei Fujinaga ,  Hiromitsu Hashisaka ,  Kiwamu Takeshita ,  Masaki Fujii ,  Hideki Ono

Inventor： Takashi Oyama ,  Kazuhisa Nakanishi ,  Tamotsu Tano ,  Keiji Higashi ,  Ippei Fujinaga ,  Hiromitsu Hashisaka ,  Kiwamu Takeshita ,  Masaki Fujii ,  Hideki Ono

IPC: C01B31/00 ,  C01B31/04 ,  C01B31/02 ,  C01D3/00 ,  C09C1/56 ,  H01G9/00 ,  C10L1/00 ,  C10C3/00 ,  C10G11/00 ,  C10G9/14 ,  H01B1/04 ,  H01B1/24 ,  C10B53/00 ,  C10B51/00

CPC classification number: H01G11/44 ,  C01B32/05 ,  C01B32/342 ,  C10B57/045 ,  H01G11/34 ,  Y02E60/13

Abstract: The present invention provides feedstock compositions for use of the production of an activated carbon for electric double layer capacitor electrodes or the production of needle coke, comprising a first heavy oil with an initial boiling point of 300° C. or higher, an asphalten content of 12 percent by mass or less, a saturate content of 50 percent by mass or more and a sulfur content of 0.3 percent by mass or less, produced as a residue resulting from vacuum-distillation of a petroleum-based oil and a second heavy oil with an initial boiling point of 150° C. or higher and a sulfur content of 0.5 percent by mass or less, produced by subjecting a hydrocarbon oil to fluidized catalytic cracking.

Abstract translation: 本发明提供了用于生产双电层电容器电极的活性炭或生产针状焦的原料组合物，其包括初沸点为300℃或更高的第一重油，沥青含量为 12质量％以下，饱和物含量为50质量％以上，硫含量为0.3质量％以下，作为由石油系油和第二重油的真空蒸馏得到的残留物 初始沸点为150℃以上，硫含量为0.5质量％以下，通过使烃油进行流化催化裂化而得到。

公开(公告)号：US07959888B2

公开(公告)日：2011-06-14

申请号：US12158165

申请日：2006-12-27

Applicant: Takashi Oyama ,  Kazuhisa Nakanishi ,  Tamotsu Tano ,  Keiji Higashi ,  Ippei Fujinaga ,  Hiromitsu Hashisaka ,  Toshitaka Fujii ,  Takashi Noro ,  Akio Sakamoto ,  Kiwamu Takeshita ,  Keizou Ikai ,  Masaki Fujii ,  Hideki Ono

Inventor： Takashi Oyama ,  Kazuhisa Nakanishi ,  Tamotsu Tano ,  Keiji Higashi ,  Ippei Fujinaga ,  Hiromitsu Hashisaka ,  Toshitaka Fujii ,  Takashi Noro ,  Akio Sakamoto ,  Kiwamu Takeshita ,  Keizou Ikai ,  Masaki Fujii ,  Hideki Ono

IPC: C01B31/00 ,  C01B31/04 ,  C01B31/02 ,  C01D3/00 ,  C09C1/56 ,  H01G9/00 ,  C10L1/00 ,  C10C3/00 ,  C10G11/00 ,  C10G9/14 ,  H01B1/04 ,  H01B1/24

CPC classification number: H01G11/44 ,  C01B32/05 ,  C01B32/30 ,  C10B57/045 ,  H01G11/34 ,  Y02E60/13

Abstract: The present invention provides a raw coke having such a structure that the graphitized product resulting from graphitization of the raw coke at a temperature of 2800° C. under an inactive gas atmosphere will have ratios of the crystallite size to the lattice constant of 360 or less in the (002) plane and 1500 or less in the (110) plane, as a raw coke providing active carbon produced by alkali-activating the raw coke, which is reduced in remaining alkali content and can simplify washing operation because washing liquid can easily pass through the activated carbon, or as a raw coke for the production of needle coke.

Abstract translation: 本发明提供一种具有这样一种结构的原焦炭，即在惰性气体气氛下，在2800℃的温度下由原焦炭石墨化产生的石墨化产物将使微晶尺寸与晶格常数之比为360以下 在（002）面中，在（110）面中为1500以下的原料焦炭，作为提供通过碱活化生焦炭生成的活性炭的原焦炭，其还原了剩余的碱含量，并且可以简化洗涤操作，因为洗涤液容易 通过活性炭，或作为用于生产针状焦的原焦炭。

公开(公告)号：US20110131867A1

公开(公告)日：2011-06-09

申请号：US13029297

申请日：2011-02-17

Applicant: Tom N. Kalnes ,  John P. Brady ,  Marco Di Stanislao

Inventor： Tom N. Kalnes ,  John P. Brady ,  Marco Di Stanislao

IPC: C10L1/00

CPC classification number: C10G3/45 ,  C10G3/46 ,  C10G3/47 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1022 ,  C10G2300/1037 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/28 ,  C12N2310/30 ,  Y02E50/13 ,  Y02P30/20

Abstract: A process has been developed for producing diesel boiling range fuel or fuel blending component from renewable feedstocks such as plant oils and greases. The process involves treating a renewable feedstock by hydrogenating and deoxygenating i.e. decarboxylating and/or hydrodeoxygenating to provide a hydrocarbon fraction useful as a diesel fuel. The hydrocarbon fraction is isomerized to improve cold flow properties. At least one interstage stream of the hydrogenating and deoxygenating reaction zone is heat exchanged with the feed to the isomerization reaction zone, and/or the effluent of the hydrogenating and deoxygenating reaction zone is heat exchanged with the feed to the isomerization reaction zone.

Abstract translation: 已经开发了用于从可再生原料如植物油和油脂生产柴油沸程燃料或燃料混合组分的方法。 该方法包括通过氢化和脱氧处理可再生原料，即脱羧和/或加氢脱氧以提供可用作柴油燃料的烃馏分。 烃馏分异构化以改善冷流动性能。 氢化和脱氧反应区的至少一个级间流与异构化反应区的进料热交换，和/或氢化和脱氧反应区的流出物与异构化反应区的进料热交换。

公开(公告)号：US20110126448A1

公开(公告)日：2011-06-02

申请号：US12815853

申请日：2010-06-15

Applicant: Jean-Charles Dumenil

Inventor： Jean-Charles Dumenil

IPC: C10L1/00 ,  C12P7/10 ,  C12P7/64 ,  C12M1/00 ,  B01J8/00

CPC classification number: C12P7/649 ,  C10L1/04 ,  C12P7/10 ,  C12P7/14 ,  C12P2203/00 ,  Y02E50/13 ,  Y02E50/16 ,  Y02P20/125

Abstract: This invention relates to a process, a plant, and a biofuel for integrated biofuel production, such as with biogasoline, biodiesel, and/or sugar product. The integrated process includes the step of removing hexose from a feedstock to form a lignocellulosic material. The process also includes the step of converting the hexose to a biogasoline and/or a biodiesel material, and the step of depolymerizing lignocellulosic material to form pentose and a residue. The process also includes the step of converting the pentose to a biogasoline and/or a biodiesel material.

Abstract translation: 本发明涉及用于综合生物燃料生产的方法，植物和生物燃料，例如与生物汽油，生物柴油和/或糖产品。 整合方法包括从原料中除去己糖以形成木质纤维素材料的步骤。 该方法还包括将己糖转化为生物汽油和/或生物柴油材料的步骤，以及解聚木质纤维素材料以形成戊糖和残余物的步骤。 该方法还包括将戊糖转化为生物汽油和/或生物柴油材料的步骤。